SEPA
United Stefos
Environmental Protection
Agency
Control Technology Center
EFA-600/R-98-017
February 1998
EMISSIONS FROM
OUTDOOR WOOD-BURNING
RESIDENTIAL HOT WATER FURNACES
control
technology center
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FOREWORD
The U.S. Environmental Protection Agency is charged by Congress with pro-
tecting the Nation's land, air* and water resources. Under a mandate of national
environmental laws, the Agency strives to formulate and implement actions lead-
ing to a compatible balance between human activities and the ability of natural
systems to support and nurture life.. To meet this mandate, EPA's research
program is providing data and technical support for solving environmental pro*
blems today and building a science knowledge base necessary to manage our eco-
logical resources wisely, understand how pollutants affect our health, and pre-
vent or reduce environmental risks in the future.
The National Risk Management Research Laboratory, is the Agency's center for
investigation of technological and management approaches for reducing risks
from threats to human health and the environment. The focus of the Laboratory's
research program is on methods for the prevention and control of pollution to air.
land, water, and subsurface resources; protection of water quality in public water
systems; remediation of contaminated sites and groundwater; and prevention and
control of indoor air pollution. The goal of this research effort is to catalyze
development and implementation of innovative, cost-effective environmental
technologies; develop scientific and engineering information needed by EPA to
support regulatory and policy decisions; and provide technical support and infor-
mation transfer to ensure effective implementation of environmental regulations
and strategies.
This publication has been produced as part of the Laboratory's strategic iong-
term research plan. It is published and made available by EPA's Office of Re-
search and Development to assist the user community and to link researchers
with their clients.
E. Timothy Oppelt. Director
National Risk Management Research Laboratory
EPA REVIEW NOTICE
This report has been peer and administratively reviewed by the U.S. Environmental
Protection Agency, and approved for publication. Mention of trade names or
commercial products does not constitute endorsement or recommendation for use.
This document is available to the public through the National Technical Information
Service, Springfield, Virginia 22161.
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EPA-600/R-98-Q17
February 1998
EMISSIONS FROM OUTDOOR WOOD-BURNING
RESIDENTIAL HOT WATER FURNACES
Prepared by:
Joseph C. Valenti and Russell K, Clayton
Ac'urex Environmental Corporation
4915 Prospectus Drive
P.O. Box 13109
Research Triangle Park, NC 27709
Prepared under EPA Contract 68-D4-0005
Work Assignments 1-043 and 2-041
EPA Project Officer:
Robert C. McCrillis
National Risk Management Research Laboratory
Air Pollution Prevention and Control Division
Research Triangle Park, NC 27711
Prepared for:
U.S. Environmental Protection Agency
Office of Research and Development
Washington, DC 20460
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ABSTRACT
Modern outdoor residential wood-burning hot water furnaces
are freestanding units situated outside the envelope of the
structure to be heated. They typically consist of a firebox and
water reservoir, assembled in a horizontal configuration. Hot
combustion gases flow from the firebox at one end, through
channels or tubes in the water reservoir, to the stack. The
gases may pass through the water reservoir once to the stack at
the end opposite the firebox (one pass) or an additional set of
pipes may bring the gases back to the stack located above but
isolated from the combustion chamber (double pass). The heated
water is pumped through radiators in the dwelling or through a
heat exchanger in the HVAC duct in response to the home
thermostat. A separate pipe coil in the water reservoir may be
used to provide domestic hot water, year round if desired. The
furnace draft is controlled by a thermostat monitoring the
temperature of the water in the reservoir. Central heating
furnaces of all types are exempt from the EPA wood heater (wood
stove) standard. In this project, emissions were measured from
one single pass and one double pass furnace at average heat
outputs of 15,000 and 30,000 Btu/hr while burning typical oak
cordwood fuel. One furnace was also tested once at each heat
output while fitted with a prototype catalytic unit installed in
the combustion chamber. Emissions measured included: EPA Method
5G particulate, semivolatile and condensible organics, 20 target
PAH compounds, and carbon monoxide. Emission results are
presented in terms of rate per hour, quantity per unit weight of
wood burned, and quantity per unit of heat delivered. Delivered
efficiencies are also presented. Compared to a wide range of
residential heating options, these furnaces' emissions were of
the same order as other stick wood burning appliances.
11
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TABLE OF CONTENTS
Section Page
ABSTRACT ii
LIST OF TABLES iv
LIST OF FIGURES iv
CONVERSION TABLE ........ V
SECTION 1.0- INTRODUCTION , 1
SECTION 2.0- PROJECT DESCRIPTION 3
2.1 EXPERIMENTAL APPROACH 3
2.2 EXPERIMENTAL SET-UP 4
2.3 EXPERIMENTAL AND SAMPLING PROCEDURES 8
2.4 ANALYSIS 11
SECTION 3.0 - QUALITY ASSURANCE AND QUALITY CONTROL ..... 13
3.1 PREPARATION OF SAMPLING MEDIA 13
3 . 2 MEASUREMENTS 13
3 .3 DATA QUALITY INDICATOR GOALS 14
SECTION 4.0 - DATA, RESULTS AND DISCUSSION 17
4.1 GENERAL DISCUSSION 17
4.2 CALCULATED RESULTS ...... 18
4.3 EVALUATION OF RESULTS 18
SECTION 5.0 - CONCLUSIONS ....... 31
Appendix A - Thermocouple Calibration Data Al
Appendix B - CEM Calibration Data Bl
Appendix C - Water Meter Calibration Data Cl
Appendix D - CEM Run Data Dl
Appendix E - Method 5G Meter Box Data El
Appendix F - Method 5G Summary Data Fl
Appendix G - Organic Analyses Data Sheets . Gl
in
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Table
LIST OF TABLES
TEST MATRIX FOR WOOD-FIRED FURNACE TESTING 6
2-1.
2-2. PROXIMATE AND ULTIMATE ANALYSES FOR RED OAK 9
2-3. PAH TARGET ANALYTE LIST 12
3-1. PRECISION, ACCURACY AND COMPLETENESS OBJECTIVES ... 16
4-la. SUMMARY OF TEST RESULTS - FURNACES A AND B COMPARATIVE
DATA .............. 22
4-lb. SUMMARY OF TEST RESULTS - FURNACE A SCOPING AND
PROTOTYPE CATALYST DATA 23
4-2a. ORGANIC EMISSIONS SUMMARY - FURNACES A AND B
COMPARATIVE DATA 24
4-2b. ORGANIC EMISSIONS SUMMARY - FURNACE A SCOPING AND
PROTOTYPE CATALYST DATA ............... 25
4-3a. GAS CONCENTRATIONS - FURNACES A AND B COMPARATIVE DATA .26
4-3b. GAS CONCENTRATIONS - FURNACE A SCOPING AND PROTOTYPE
CATALYST DATA 26
4-4. COMPARATIVE DATA AGGREGATED BY OPERATING MODE AND
FURNACE [RANGE IN ( ) ] 26
4-5. OVERALL COMPARISON OF RESIDENTIAL WOOD, OIL, AND GAS
COMBUSTION EMISSIONS 27
LIST OF FIGURES
Figure
2-1
2-2
2-3
4-1
4-2
4-3
Double pass furnace schematic 7
Single pass furnace schematic 7
Typical furnace test setup 10
Summary of particulate and organic emissions data for
wood -fired furnaces A and B 28
PAH results for Furnace A ....... 29
PAH results for Furnace B 30
IV
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CONVERSION TABLE
Most quantities in this report are in nonmetric units. Readers
more familiar with metric units may use the following values to
convert to that system.
Nonmetric
Btu/hr
Btu/lb
Btu/ (lb-°F)
degree Fahrenheit (TF)
cfm
ft
gpm
Ib
lb/ft3
Ib/gal
Ib/min
in. H20 i 60°F
Multiply by
1.055 x 103
2.326 x 103
4.187 x 103
(TP+459.67} /I. 8
4.719 x 10'4
3.048 x 10"1
6.309 x 10~5
4.536 x 10'1
1.602 x 10
1.198 x 102
7.560 x 10~3
2.488 x 102
Yields metric
joule (J)
J/kg
J/kg-K
K
m3/s
m
m3/s
kg
kg/m3
kg/m3
kg/s
pascal (Pa)
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SECTION 1.0 - INTRODUCTION
In the early 1980's, the state of Oregon began developing
methods for characterizing source emissions from residential wood
combustion units. The developed methods have since blossomed
into test methods used to audit and certify wood-burning heaters.
From these beginnings, the U.S. Environmental Protection Agency
(EPA) has established emission performance standards for
residential wood heaters.
The federal regulations established by the EPA in 1988 limit
emissions from residential wood heaters, such as wood stoves,
pellet-stoves, and factory built fireplace inserts. These
regulations, however, do not include all wood-fired heating
appliances. For example, central heating furnace/boilers are not
covered under the current regulations.
In general, emissions from the combustion of wood in stoves
and furnaces contain significant levels of carbon monoxide (CO)
and fine particulate matter consisting, in part, of mutagenic
polycyclic aromatic hydrocarbons (PAH). If atmospheric
conditions are conducive for accumulating smog-like clouds of
emissions, the wood smoke could pose a health hazard. With the
potential for such a condition under consideration, the EPA
established maximum acceptable emissions levels for the
certification of most residential wood-fired heaters.
Typically, the modern outdoor residential wood-burning hot
water furnace is a freestanding unit situated outside the
envelope of the structure to be heated. The unit consists of a
closed combustion chamber surrounded by a water tank and vented
through a stack. A wood burning fire is contained and controlled
in the combustion chamber or fire-box of the furnace. During the
combustion process, heat is transferred through the walls of the
chamber into the water. The hot water from the furnace tank can
then be circulated through radiators or air-handling heat
exchangers to transfer heat into a residence. Some central
heating furnaces are equipped with additional plumbing to provide
domestic hot water.
Most commercial central heating furnaces are supplied with
an 8- to 10-foot stack. Typical indoor wood burning stoves have
chimneys which extend through the roof of a home to heights of 20
to 30 feet. The relatively low chimney height of the central
heating furnace/boiler, compared to the conventional wood stove
installations, creates a greater potential for the localization
of objectionable emissions in and around residences.
Additionally, concerns have been raised about the manner in which
1
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the combustion process is controlled and how the control affects
the emissions.
The State of Wisconsin has asked the Control Technology
Center of EPA's Air Pollution Prevention and Control Division
(APPCD) for assistance in determining whether the need exists to
regulate these furnaces. Therefore, the EPA has undertaken the
task of evaluating the emissions from the central heating
furnaces and the manner in which the combustion is controlled.
The objective is to develop baseline emission factors for
comparison with other residential heating systems.
Section 2 provides a description of the experimental
approach and sampling and analytical methods employed. Steps to
ensure project quality are described in Section 3. Data, results
and discussion are presented in Section 4. The appendices
contain the detailed data.
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SECTION 2.0- PROJECT DESCRIPTION
2.1 EXPERIMENTAL APPROACH
In order to determine whether the need exists to regulate
the central heating furnace/boilers, the EPA needs to establish
baseline emission factors. The subject investigation was
undertaken as a means of "scoping" the performance of typical
furnace types under normal operating conditions. The objective
of the investigation was to gather emissions data using standard
EPA test methods developed for certifying and auditing wood-fired
heaters (wood stoves). These results could then be compared to
the emission factors established for other gas-, oil, and wood-
fired residential"heating equipment. There are significant
differences in the way these home heating furnaces are designed
and operated which produce widely different emission properties
and levels. For example, the wood-fired furnaces tested in this
project used thermostats to deliver a more constant amount of
heat, compared to wood stoves which usually have manual draft
controls.
The outdoor residential wood-burning hot water furnaces were
tested following EPA Reference Method 28 (M28-40 CFR Part 60,
Appendix A). Method 28 is the test method used to certify and
audit wood-fired heaters (stick and pellet burning woodstoves).
The method specifies fuel preparation, furnace operation, and the
reporting of the results. Method 28 requires Method 5G or 5H
{CFR Part 60, Appendix A) to determine the concentrations of
oxygen (02) , carbon dioxide (CO2) , carbon monoxide (CO), and
particulate matter (PM) in the emissions.
For the purposes of these tests, some of the fuel
preparation procedures under Method 28 were modified in favor of
preparing the fuel and operating the furnace as recommended by
the manufacturer. Cordwood was used instead of the dimensioned
lumber specified for wood heater certification. Method 28A was
used to calculate the stack gas dry molecular weight, as required
for flow measurements. Method 5G was the primary sampling method
used for the test. The sampling method, Method 5G, was modified
with the addition of an XAD-2 absorbent trap to collect organics;
this modified sampling method will hereafter be referred to as
Modified Method 5G (MM5G). The collected MM5G samples were
analyzed for total particulate matter (PM), total semivolatile
organics [sometimes referred to as total chromatographable
organics (TCO)], condensible organics as measured by gravimetric
analysis (GRAV), and polycyclic aromatic hydrocarbons (PAHs).
3
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The efficiencies of the units were measured as a secondary
objective for reporting emissions relative to the input heating
value of the wood and to their heat output from the furnace.
The stack test location and MM5G probe location were
selected according to the criteria established by EPA methods for
the testing of wood-fired heaters. The emissions sampling system
consisted of a dilution tunnel and hood. The hood, or bell, is
positioned inches above the stack exit. The released emissions
plus dilution air are captured and drawn into the hood and
dilution tunnel by an induced draft (ID) fan. A draft
differential pressure of <0.005 in H20 was maintained on the
wood-fired furnace as required by Method 28. The MM5G samples
were taken from the dilution tunnel duct. The flue gas
concentrations as measured by the CEM's were sampled from the
chimney. The various protocols for sampling in small ducts as
described in EPA Methods 1A, 2C» and 5C (CFR Part 60, Appendix A}
were followed. An additional CO monitor was positioned to sample
CO concentrations in the dilution tunnel. This allowed the
furnace stack flow to be calculated by multiplying the dilution
tunnel flowrate by the ratio of dilution tunnel CO to furnace
stack CO.
Furnace Stack Flow = dilution tunnel flow x C0dilution /C0scack
The MM5G sampling train consisted of a pump which draws gas
from the dilution tunnel through a system of filters, an XAD-2
organics trap, a condenser and a gas meter. Sampled gas
temperatures were measured, and recorded, throughout the train.
Also, the velocity head and temperature in the dilution tunnel
were measured at the point of average velocity (as determined by
a preliminary velocity and temperature traverse). Sampling
rates were controlled to maintain a constant ratio of
proportionality between dilution tunnel flow and flow pulled
through the probe.
2.2 EXPERIMENTAL SET-UP
The combustion rate of the central heating furnaces
investigated is controlled by a thermostat that maintains the
temperature of the water within a specified temperature range.
When the temperature of the water increases to the upper limit of
the range, the temperature switch will stop or slow the
combustion air supply into the combustion chamber. The
combustion process will be stalled, slowing the amount heat being
transferred to the water. During this period of stalled
combustion, the temperature in the tank will drop as heat is
removed via the water circulated from the tank through the
external space heating heat exchanger. Once the water
temperature falls to the lower limit of the temperature range,
the temperature switch will allow combustion air to enter the
combustion chamber. The combustion process will increase,
boosting the heat transfer to the water.
For these scoping tests, two types of furnaces were
selected as representative of the industry. One of these
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furnaces was tested with a pre-production prototype catalyst
designed to reduce emissions. The type of furnace is defined by
the configuration of the unit. The flue gases exit the
combustion chamber by way of a flue that passes through the water
tank. In general, a single pass furnace allows the flue gases to
pass once through the flue in the water tank before exiting
through the chimney. As the hot flue gases pass through the
flue, heat is transferred to the water in the tank. In a double
pass furnace, flue gases pass through the water tank twice before
exiting through the chimney. The second pass of the stack is
designed to provide more surface area and more contact time
between the hot flue gases and the water in the tank.
Representative furnaces of both types were provided to EPA/APPCD
for testing.
The double pass furnace tested consists of a plate steel
combustion chamber surrounded by a water tank on all sides but
one. As shown schematically in Figure 2-1, a door on the exposed
surface of the chamber provides the only access to the fire-box
for fuel loading and ash removal. Combustion air is supplied to
the fire-box by a forced draft fan on the door. The forced draft
fan is controlled by the previously mentioned thermostat switch
on the front of the unit. A damper on the fan intake was used to
adjust the air supplied to the combustion chamber. The flue
gases produced during the combustion process exit the fire-box
through four flue pipes at the rear of the combustion chamber.
The flue pipes extend through the water tank to a chamber at the
rear of the unit. In the secondary chamber, flue gases travel
upward toward two flue pipes, where they pass back through the
water tank to the front of the unit. The upper two flue pipes
empty into the chimney where the flue gases exit the furnace.
The exterior of the water tank is insulated and covered with
exterior metal sheeting. The rear of the water tank is equipped
with a pump and plumbing from which the heated water can be
circulated. Additional pipe connections and valves are located
on the rear of the furnace to fill the water tank. The
manufacturer provided the furnace with an air-handling exchanger
for heat removal.
Similar to the double pass furnace, the single pass unit
shown schematically in Figure 2-2 contains a steel plate fire-box
surrounded by a water tank. Several transverse water filled
tubes and a water filled transverse baffle provide additional
heat transfer surfaces. A door on the front of the unit provides
access to the fire-box. The combustion air is controlled by a
thermostat and an electrically controlled damper. The hot gases
flow around the tubes and baffle to the rear of the furnace and
empty into the chimney. The pump and plumbing for circulating
the water are located on the rear of the furnace. The single
pass furnace was equipped by the manufacturer with a water cooled
heat exchanger for the test.
The furnaces were tested at two conditions. Under the
first condition, heat was removed from the furnaces at a rate
typical of the average winter heat demands for homes in warmer
climate regions (15 to 20 kBtu/h). At the second condition, heat
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was removed at a higher rate (30 to 40 kBtu/h) to simulate colder
climate requirements. The heat extracted from the furnaces
during the testing was well below the possible heating output of
the furnaces when fully charged. Testing under these conditions
caused cycling of the controlled combustion process.
Each furnace was tested twice at each of the test
conditions. One of the units, equipped with a prototype
removable catalyst, was additionally tested once at the high heat
removal rate and once at lower heat removal rate. Blank MM5G
samples were also collected for each furnace. The test matrix
for this study is shown in Table 2-1.
The project generated sample sets representing 12 tests and
three blanks. Each of the test runs spanned the time to burn a
full wood charge at a set heat output rate, as defined by the
test matrix shown in Table 2-1. Each furnace was connected to an
exchanger through which its heated water was circulated. One
unit was provided with a forced-air (air-to-air) heat exchanger.
The other unit utilized a water-to-water heat exchanger. The
heat output rate through the exchanger was determined by
measuring the flow rate and the inlet and outlet temperatures of
the circulated water. The heat output rate was controlled by
regulating the water flow rate being circulated from the furnace
and by regulating the flow of the cooling medium across the
exchanger. This measurement isolated the deliverable efficiency
of the furnace from the deliverable efficiency of the exchanger.
The delivered efficiency was defined as the energy removed from
the hot water divided by the energy in the wood burned as
TABLE 2-1. TEST MATRIX FOR WOOD-FIRED FURNACE TESTING
Furnace
Furnace A Scoping test
Furnace A without catalyst
Furnace A without catalyst
Furnace A with catalyst
Furnace A with catalyst
Furnace B
Furnace B
Furnace A without catalyst
Furnace A with catalyst
Furnace B
Test Condition
High Heat Removal Rate {30 to 40 kBtu/hr)
High Heat Removal Rate (30 to 40 kBtu/hr)
Low Heat Removal Rate (15 to 20 kBtu/hr)
High Heat Removal Rate (30 to 40 kBtu/hr!
Low Heat Removal Rate (15 to 20 kBtu/hr)
High Heat Removal Rate (30 to 40 kBtu/hr)
Low Heat Removal Rate (15 to 20 kBtu/hr!
Dilution Tunnel Blank
Dilution Tunnel Blank
Dilution Tunnel Blank
Test Number
A-l", A-2
A-3, A-4
A-5, A-6
A-7»
A~8b
B-l, B-2
B-3, B-4
A- 9
A- 10
B-5
a Water temperature significantly below manufacturer's
recommendation (see text).
b Substantial smoke spillage when draft fan on.
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Loading
door
Figure 2-1. Double pass furnace schematic.
Loading
door
supporting
legs
Figure 2-2, Single pass furnace schematic.
Shading key for Figures 2-1 and 2-2.
I i water storage E3 smoke path
•I wood fuel IB insulation
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determined using the lower heating value (see Sample A, Table 2-
2). Specifically:
Delivered efficiency = 100 x ^energy removedt/energy input (1)
where:
Energy removed,. = (watert/60) x density,, x (T2 - Tx) x [(t+1) - t]
x specific heatt
watert = corrected water flow, gpm
density,. = corrected water density, Ib/gal
T2 = temperature of water leaving furnace
Ti = temperature of water entering furnace
t+1 = time at end of recording interval, sec.
t = time at start of recording interval, sec.
specific heat = 1 Btu/(lb-°F)
and:
Energy input = (wood weightstart - wood weightend) x lower heating
value/(1 + wood moisture content)
wood weight, Ib
lower heating value, Btu/lb dry
moisture content, %
The furnaces were tested at separate wood stove testing
facilities. Both facilities are designed specifically for Method
5 dilution tunnel sampling and should, therefore, have produced
similar quality results. The Method 5G facility specifications
are restrictive enough to ensure that there were no substantial
differences in the dilution tunnel arrangement. The testing at
both facilities adhered to the guidance provided by the Quality
Assurance Project Plan (QAPP) developed under the EPA Work
Assignment entitled "Emissions from Wood-Fired Residential
Central Heating Furnaces." A representative from EPA/APPCD's
Technical Services Branch audited both facilities during testing
to determine any deviations from the QAPP.
The unsplit, mixed hardwood used for the two scoping tests
on Furnace A was supplied by Furnace A's manufacturer. The red
oak fuel used at both test facilities for all other tests came
from the same seasoned lot of cordwood. Samples of the red oak
fuel were sent to Commercial Testing and Engineering for an
ultimate and proximate Analysis. The results of the analysis are
shown in Table 2-2. The results from Sample B reflect the
analysis of a wood chip taken from the surface of a typical piece
of test fuel at one facility. The analysis of Sample A reflects
the results from core samples taken from a number of pieces of
typical test fuel at the other facility.
2.3 EXPERIMENTAL AND SAMPLING PROCEDURES
Each furnace was installed per manufacturers' installation
instructions at its respective test facility upon an electronic
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weighing scale as shown in Figure 2-3. The manufacturers also
provided the testing facilities with instructions on loading and
operating the furnace. Once installed and visually inspected,
the furnaces were pre-burned and checked with the assistance of
representatives from the manufacturers.
TABLE 2-2. PROXIMATE AND ULTIMATE ANALYSIS FOR RED OAK
% Moisture
% Ash
% Volatile
% Fixed Carbon
Total
Btu/lb
% Sulfur
MAF Btu
SAMPLE A
PROXIMATE ANALYSIS
As Dry
Received Basis
21.98
0.27
69.03
' 8.72
100.00
6295
0.02
xxxxx
0.35
88.48
11.17
100.00
8069
0.03
8097
ULTIMATE ANALYSIS
% Moisture
% Carbon
% Hydrogen
% Nitrogen
% Sulfur
% Ash
% Oxygen
Total
AS
Received
21.98
39
,09
89
.18
,02
27
100.00
Dry
Basis
XXXXX
50.10
6.27
0.23
0.03
0.35
43.02
100.00
SAMPLE B
PROXIMATE ANALYSIS
ULTIMATE ANALYSIS
As
Received
% Moisture
% Ash
% Volatile
% Fixed Carbon
Total
Btu/lb
% Sulfur
MAF Btu
9.
0.
79.
10.
100.
7680
0
29
77
26
68
00
.02
Dry
Basis
xxxxx
0
87
11
100
8467
0
8540
.85 '
.38 '
.77 '
.00 '
!
1
.02
% Moisture
% Carbon
% Hydrogen
% Nitrogen
% Sulfur
% Ash
% Oxygen
Total
As
Received
9
45
5
0
0
0
38
100
.29
.21
.60
.27
.02
.77
.84
.00
Dry
Basis
xxxxx
49
6
0
0
0
42
100
.84
.17
.30
.02
.85
.82
.00
As noted above, the fuel burned during all the tests, except
the two scoping tests on Furnace A, was seasoned, cut and split
cordwood purchased from the same source. For all tests, a test
charge of 7 Ibs of wood/ft3 of useful combustion chamber volume
was selected from the cordwood. For Furnace A, each piece was
weighed and measured in three locations for moisture content.
The weighted average of the moisture content was determined for
the combined test charge. For Furnace B, moisture measurements
were averaged without weighting. As specified by the test
method, the average moisture content of the test fuel was between
15- and 25-percent moisture dry basis.
Prior to the testing, the furnace was pre-loaded with a
warm-up charge consisting of 40 to 80 Ib of cordwood similar to
the test fuel charge. The pre-load was to be sufficient enough
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Dampers
15'
Boil
Fuel
oadin
door
loadinj h*
Weigh
seal
ler
XX X
Dilution
air
THC
CO
CO2
02
X X
To atmosphere
11
Boiler
water
thermostat Heat
exchanger
Hot
water
out
Cold water
return
\
T
Automatic draft
control
^Method
5G probe
JDamper
^Blower
JFIoor
Figure 2-3. Typical furnace test setup.
10
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to raise the water temperature in the tank to the operating
temperature of -180 °F. At least one hour before the sampling
was to begin, the heat removal rate and the furnace were adjusted
to the test conditions. During the pre-burn period the continuous
emissions monitors (CEMs) were calibrated to appropriate zero and
span values. After the two-point calibration, the CEMs were set
to sample. Also during this time, the MM5G sampling train was
assembled and checked for leakage. Upon passing the leak check
as specified by the test methods, the sampling trains were set to
sample.
Once the pre-load fuel had been reduced to hot coals, the
MM5G sampling pumps and CEM pumps were started. The furnace was
stoked to its specified fuel charge. The initial scale readings
were recorded along with the process temperatures, flue gas
concentrations, and ambient temperature and humidity. The
critical parameters were continually monitored and recorded at
regular intervals throughout the test. During the test, the
systems were continually monitored. The water flow rate was
adjusted during the test, as needed, to maintain the desired heat
removal rate. The .furnace's built-in temperature controlling
thermostat continually measured the temperature in the water tank
and adjusted the combustion process to suit the heat removal
rate.
The sampling was ceased when the entire test fuel charge had
been expended as measured by the weight. A post-test, leak check
of the MM5G sampling train and verification of the CEM's zero and
span calibration values were conducted. The MM5G sample filters
were recovered by returning the filters to their labeled petri
dishes and returning them to a desiccator. The XAD-2 absorbent
trap was sealed and stored in a freezer. The probe and glassware
were triple rinsed with acetone into a clean, tare weighed pan
and placed into a fume hood for reduction. The sample fractions
and XAD-2 were stored for later semivolatile, polycyclic aromatic
hydrocarbon (PAH), and condensible organic analyses. These terms
are described in more detail below.
2.4 ANALYSIS
Upon recovery of sample at the conclusion of a test, the
filters and the pan from the probe rinse were transferred to a
desiccator. After a minimum of 24 hours in a desiccator, the
filters and pan rinse were weighed. The collected particulate
matter was calculated as the difference between the filter and
pan final weight and the tare weight. The total particulate
matter was calculated as the sum of all the values from each of
the components for each test.
The collected particulate and organics from the filters, pan
rinses, and XAD-2 canisters were then extracted with methylene
chloride and reduced to a volume of 5mL. This reduced sample was
used to measure the organic composition of the particulate.
The condensible fraction represents compounds with boiling
points greater than 30Q°C. A 1 mL aliquot was removed from the
5mL extract solution. The aliquot was added to prepared and
tared micrograv pans. The pan weights were measured and repeated
11
-------
at 24-hour intervals until a 1-percent or less relative
difference was recorded between consecutive weighings. Between
weighings, the pans were stored in a desiccator over activated
carbon and silica gel. The net weight of the reduced aliquot was
calculated by subtracting the tare weight. The net weight was
multiplied by five to obtain the total extracted condensible
organics sampled.
A second ImL aliquot was removed from the extracted solvent
solution for total chromatographable organic (TCO) analysis. TCO
compounds are defined as semivolatile organics with boiling
points between 100 and 300°C. The TCO determinations were
measured with a gas chromatograph. The aliquot was sealed in a.
glass autosampler vial. The samples were injected into a fused-
silica capillary column heated to a final temperature of 250°C.
The column was connected to a flame ionization detector (FID)
that produced a response approximately proportional to the weight
of organic material present in the sample. The analyzer then
used algorithms to calculate and validate data. The TCO program
summed together all valid data from duplicate runs of each
sample. The TCO program then used storage parameters to
calculate TCO mass per sample and statistical information about
the replicate results.
The polycyclic aromatic hydrocarbons were analyzed using a
mass spectrometer (MS). The MS was tuned for better resolution
around a list of target analytes. The target analytes are listed
in Table 2-3.
TABLE 2-3.
PAH Target Analyte List [number in ()
Figures 4-2 and 4-3].
refers to
Naphthalene (1)
2 -methyl naphthalene (2)
Acenaphthylene ( 3 )
Acenaphthene (4)
Dibenzofuran (5)
Fluorene (6)
Phenanthrene (7)
Anthracene (8)
Fluoranthene (9)
Pyrene (10)
Chrysene (11)
Benzo (a) anthracene (12)
Benzo (b) f luoranthene (13)
7, 12-Dimethylbenz (a) anthracene
(14)
Benzo (k) f luoranthene (15)
Benzo (a)pyrene (16)
3 -methyl cholanthrene (17)
Indeno(l,2, 3-cd)pyrene (18)
Dibenz (a, h) anthracene (19)
Benzo (ghi)perylene (20)
12
-------
SECTION 3.0- QUALITY ASSURANCE AND QUALITY CONTROL
3.1 PREPARATION OF SAMPLING MEDIA
All MM5G sampling glassware was acetone rinsed, scrubbed
with a nylon brush if necessary, and left under a fume hood for
24 hours prior to assembling the sampling trains. The quartz
fiber filters were desiccated for a minimum of 24 hours. An
average tare weight was recorded for each filter after three
consecutive weight measurements. The filter casings were then
assembled and sealed with aluminum foil until the final assembly.
The XAD-2 canister and resin were cleaned prior to
assembling. Impurities were extracted from the resin by
sequentially pumping toluene and dichloromethane through the
media. The solvents were then removed from the resin by
evaporation with a stream of nitrogen. The XAD canister was
baked in an oven for 24 hours to remove impurities. Once
cleaned, the canister was filled with the XAD-2 resin and sealed.
The sealed containers were refrigerated until the final assembly
in the sample trains.
When all the components for the sampling train were ready
for assembling, the components were visually inspected and
assembled. Once the sampling train was assembled, a vacuum leak
check was performed on the system. The assembly was accepted if
less than 0.02 ft3/rain, or approximately two-percent of the
normal sampling rate, could be pulled through the sampling train
while the probe was capped or plugged. If the sampling train did
not pass the leak check, it was disassembled, reassembled, and
checked again until the leakage was reduced to the acceptable
level. The sampling train was also checked for leaks at the
completion of the test. If the sampling train did not pass the
post-test leak check, the test was disregarded.
The MM5G dry gas meters have been calibrated semi-annually
against a spirometer. Temperature and pressure measurements are
taken before and after the meter, so as to convert the measured
dry gas volume flow rates to standard pressure and temperature,
3.2 MEASUREMENTS
All thermocouples used for measuring temperatures were
calibrated at the end of the test period. The thermocouples were
calibrated at two points, in freezing water and in boiling water.
All of the thermocouples measured the two calibration standards
to within 1F°. The results of the calibration are reported in
Appendix A.
13
-------
The continuous emission monitors (CEMs) used to measure the
gas concentrations in the stack and dilution tunnel were zeroed
and spanned prior to and following each test. The CEMs were
calibrated to two values. First, the CEMs were calibrated to
zero with nitrogen. The other value for the calibration, the
instrument span, was measured against bottled gases of known
concentrations. At one facility, a three-point calibration was
conducted prior to testing. The other facility performed a five
point calibration at the completion of all the tests. The daily
zero and span calibration checks are reported with the test
information data. The post-test calibrations are reported in
Appendix B.
The volume flow rate of the water circulated from the tank
of the furnace was measured with either a rotameter (Furnace A)
or a totalizing flow meter (Furnace B). The meters were
calibrated by weighing the water collected in a container over a
set flowrate and timed interval. The total volume of water as
determined from the weight was then compared to the measured
volume flow as measured by the meter. The results from the water
meter calibrations are reported in Appendix C.
The method used to determine the average moisture content of
the fuel differed between the two facilities. One facility
determined the average moisture content of the fuel in a manner
consistent with Method 28. Each individual piece of test fuel
was weighed and measured for moisture content. The weight and
moisture content of the individual pieces of test fuel ranged
from 1.5 to 5 Ibs and 10- to 35-percent respectively. The
moisture content value used in the calculations was determined as
the average measured moisture content. Because the test fuel
used was not dimensioned lumber as per Method 28, the other
facility determined the moisture content of the fuel as a
weighted average. Each individual piece was weighed and measured
for moisture content. The total weight and moisture weight was
determined. The resulting weighted average was determined as the
fraction of total moisture per total dry weight of the fuel
charge. Both laboratories used the Delmhorst electric
conductivity instrument to measure the moisture content of the
individual pieces of wood. This instrument provides a direct
reading of the moisture content on a dry wood basis.
The fuel charges were also loaded differently at the two
facilities. This investigation was undertaken to determine
baseline emission factors for these furnaces at normal operating
conditions. The furnaces were therefore loaded in a manner
recommended by the respective manufacturers. One facility loaded
the test fuel into the firebox in a latticed fashion. Each layer
of fuel was turned perpendicular to the preceding layer. The
other facility loaded fuel into the firebox in a more compact
stack of parallel layers.
3.3 DATA QUALITY INDICATOR GOALS
Despite their differences, both facilities were able to
remain (with minor exceptions) within the guidelines of the
technical objectives and data quality indicator goals established
14
-------
in the Quality Assurance Project Plan. The EPA audited the test
procedures and equipment at each of the testing facilities.
Through the Technical Systems Audit (TSA), the EPA identified all
procedural modifications and differences. The EPA concluded that
"The TSA did not identify any major problems associated with the
implementation of the QAPP ... The quality of data generated is
expected to satisfy the project's technical objectives."
The manufacturer of Furnace A recommended a water reservoir
set point (temperature at which the draft is turned off) of 160
°F. Scoping Test A-l set point was incorrectly set at 120 °F.
Average water outlet temperature for test A-l was 124 °F. The
set point for the remaining tests on Furnace A was 160 °F; the
water outlet temperature for these tests ranged from 156 to 172
°F. Average Furnace B water reservoir outlet temperature ranged
from 180 - 182 °F for the four tests. Although the QAPP was
written with the concept of requiring a set point temperature
>180 °F, this requirement was abandoned for the tests on Furnace
A in favor of the manufacturer's recommendation. Manufacturer
of furnace B recommended a set point of 180 °F as being typical
of field operation..
Scoping Tests A-l and A-2 on Furnace A burned mixed hardwood
fuel. All the remaining tests on Furnace A, and all tests on
furnace B, used seasoned red oak fuel from the same source.
The data quality indicator goals from the QAPP are
identified in Table 3-1. It should be noted that due to the
length of these tests, and the fact that tests were not intended
as certification tests, the DQI goals for 02, C02, and CO
measurements were relaxed from the standards of Method 5H to the
less stringent standards set forth in Methods 3A and Method 10.
15
-------
TABLE 3-1. PRECISION, ACCURACY, AND COMPLETENESS OBJECTIVES
Measurement Precision
Method or Experimental Standard
Parameter Reference Conditions Deviation Accuracy Completeness
Velocity-Pi tot/
Manometer
Moisture-Condenser
Moisture-Wet Bulb/
Dry Bulb Thermocouple
Moisture-Condenser
Stack Temperature
Boiler Water Temperature
(In & Out)
Stove Surface
Temperature
Stove Combustion
Temperature
O2-Paramagnetic Monitor
CO / C02 -Nondi spers i ve
Infrared Monitor
CO-NDIR
THC-FID
Particulate Emissions
Total Chromatographic
Organics
Semivolatile Organics
Test Fuel Weight
Electronic Weight
Scale
Test Fuel Moisture
Electrical
Resistance
Test Fuel Moisture ASTM
EPA- 2
EPA- 4
EPA- 4
EPA- 2 8
EPA-28
44FR58625
44FR58625
44FR58625
EPA-MM5 , 5G
EPA-MM5G
EPA-MM5G
EPA-28
EPA-28
Stack
Stack
Ambient
Dilution
Tunnel
Stack
Furnace
External
Surface
Firebox
Stack
Stack
Dilution
Tunnel
Stack
Dilution
Tunnel
Dilution
Tunnel
Dilution
Tunnel
_
—
—
10%
5%
±5%
±5%
±5%
±5%
±5%
±5%
±10%
±2%
—
±10%
±10% RPD*
±10% RPD*
±10%
±5%
±5%
—
None
None
None
None
±1°F
±1°F
±10% Bias
±5% Bias
—
±10% Bias
±15%
±25%
±20%
±0.5
±3% Bias
—
100%
100%
100%
100%
100%
100%
100%
100%
100%
100%
—
100%
100%
100%
100%
100%
100%
_
Relative Percent Difference
16
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SECTION 4.0 - DATA, RESULTS AND DISCUSSION
4.1 GENERAL DISCUSSION
The two furnaces were tested at separate wood stove
testing facilities following prescribed EPA test methods. One of
the laboratories is EPA-accredited for certification testing wood
heaters. The test methods provided sufficient controls to ensure
that the testing results were comparable. The test methods did,
however, allow for some flexibility in the equipment and means in
which the data were collected.
Both facilities were equipped with similar dilution
tunnel arrangements. The position of the dilution tunnel "bell"
relative to the stack is set so that the negative pressure in the
tunnel does not affect the stack pressure. The Method 28
criteria require that, with the tunnel turned on, the effect on
stack pressure must be <0.005 in. of H20. The negative pressures
maintained in the dilution tunnel pull the stack emissions into
it along with ambient (dilution) air. A greater or lesser amount
of excess air may have been pulled into the dilution tunnel
depending upon the stack flow, so that the total tunnel
volumetric flow remains relatively constant. The sampling rate
was related to the volume flow rate within the dilution tunnel.
The resulting calculation yielded a value of total measured
emissions independent of the quantity of the excess air.
At one of the testing facilities, the dilution tunnel
flow rate was sized for normal wood stove testing which easily
accommodates stack flows in the 10-30 cfm range. During
preliminary firing of Furnace A, it was found that with the draft
setting at its maximum, a significant fraction of the stack
emissions were not captured by the tunnel. However, during
actual testing, the draft setting was reduced per the
manufacturer's direction to a nearly closed position, limiting
air flow into the furnace. Under these reduced draft flow
conditions, all stack emissions were captured during tests of the
standard furnace. When testing Furnace A with the prototype
catalyst (tests A-7 and A-8), the draft setting was closed down,
again at the manufacturer's direction. However, when the draft
was on, significant emissions escaped the furnace and were not
captured by the tunnel. The draft was on for a small fraction of
the total test period. The effect on the measured emissions
cannot be quantified; the final emission numbers presented in
this report may be under estimated by as much as 20% for tests A-
7 and A-8.
17
-------
Another variance between the testing facilities was the
manner in which the data were recorded. One facility utilized a
data acquisition system (DAS) to record, at one minute intervals,
the temperatures, the GEM measured gas concentrations, and the
weight of the remaining fuel. The other facility manually
recorded the same information at ten-minute intervals. During
the ten minute intervals, significant excursions in the measured
gas concentrations may have occurred without being recorded. The
data were averaged over the duration of the test to minimize the
affects the excursions might have on the resulting data. In
addition, the difference in the manner in which this portion of
the data was recorded did not affect the MM5G particulate
measurements.
Scoping tests A-l and A-2 with Furnace A were conducted
as preliminary runs to evaluate the test methods and collect data
to predict heat load maintenance operations, and filter and XAD-2
loadings. Both of these scoping tests were run using a different
fuel (mixed hardwoods) than the remaining tests. In addition,
Scoping Test A-l was run at the incorrect water reservoir
temperature set point. The results from scoping tests A-l and A-
2, and from the two tests with the preproduction prototype
catalyst (tests A-7 and A-8) are presented separately from the
other tabulated test results.
4.2 CALCULATED RESULTS
The MM5G sampling train was used to calculate the total
particulate matter (PM) in the emissions. The total PM was
divided by the sampling time to calculate the average emissions
in grams per hour. The burn rate of the fuel was determined from
the dry weight of the initial fuel charge and the sampling time.
The input fuel energy was determined from the dry charge weight
and the dry basis heating value of the wood as determined by the
ultimate and proximate analyses. The ratio of particulate weight
to dry fuel weight was determined from the average PM emission
rate and the burn rate. The total PM was then compared to the
total input heat; the result was a calculation of milligrams of
particulate matter per Btu of input heat. This value was also
converted to milligrams of PM per megajoule (MJ) of input heat.
The total PM was also compared to the furnace output in units of
milligram per Btu of output heat. The MM5G particulate results
for the comparable tests on both furnaces are presented in Table
4-la. The organics results in the samples, measured as GRAV,
TCO, and PAH fractions, are reported in Table 4-2a. The PAH
results shown in Table 4-2a are based on the target compounds
listed in Table 2-3. The gas concentrations shown in Table 4-3a
are reported as averages over the duration of the tests.
4.3 EVALUATION OF RESULTS
The first two tests on Furnace A (scoping tests A-l and
A-2) were performed as an evaluation of the test methods. As
previously stated, the test methods were developed for the
testing and certification of wood stoves and had to be modified
for testing the central heating furnaces. These two initial
18
-------
scoping tests were therefore used for methods evaluation and
development. These data, reported separately in Tables 4-lb
through 4-3b, indicate that the developmental tests results, even
with different, somewhat higher moisture cordwood as fuel, are
consistent with the other tests, Note also that scoping test A-l
was run at a lower water temperature set point (120° F compared
to 160° F for all the rest of Furnace A tests). The results from
the prototype catalyst tests on Furnace A are also presented in
Tables 4-lb through 4-3b.
In all test cases, the furnaces delivered heat at an
efficiency of about 50 percent, plus or minus 10 percent, of the
input heating value of the wood. This measurement reflects the
combustion of the fuel and transfer of the heat to the water in
the tank to be circulated. This does not account for the
efficiency of the heat exchanging device or electrical energy
required for the draft fan, the draft damper or the thermostats.
As noted previously one furnace (Furnace A) was supplied
by the manufacturer with a water-air heat exchanger to simulate
the home heat demand. Furnace B's manufacturer provided a water-
water heat exchanger for this purpose. Appendices D and E,
respectively, show that this had a significant effect on the
draft on/off cycle times. Furnace A's cycle was quite variable.
Typically, it cycled on for about 120 min. At the higher burn
rate, it then cycled off for about 60 min. At the lower burnrate
it cycled off for about 80 min. Furnace B exhibited a typical on
cycle of 8 minutes, followed by 30 and 60 min. off cycles at
higher and lower burn rates, respectively.
The MM5G data were analyzed to see if a relationship
existed between the measured emissions, in grams per MJ heat
input rate, and the average burn rate, in dry kilograms of fuel
burned per hour. The relationships are illustrated in Figure 4-
1. The particulate matter emission factor does not show a clear
trend as a function of the burn rate. At a glance, the organic
measurements do not show any trend, either. For a given furnace
configuration, the emission factors derived from Figure 4-1
appear to be relatively constant across the burn rate range
studied. Furnace A with the prototype catalyst showed higher
levels of TCO and PAH emissions, especially at the lower burn
rate. This may have been due to cracking of the larger organic
molecules as they passed through the catalyst but not complete
oxidation due to a lack of excess air.
The difference in the catalyst versus noncatalyst results
from Furnace A can be explained in two possible ways. The
catalyst could have greatly changed the combustion process and
therefore, the emissions composition. For example, it was noted
that the furnace operated much differently with the catalyst
installed. The heat was transferred to the furnace's water tank
at a much higher rate with the catalyst. Also, the excess oxygen
level fell to nearly zero when the draft was on (see runs TTCD-1
and 2 in Appendix D). But when the temperature in the tank
reached the maximum of the set range, the thermostat would stall
the combustion. During the periods of stalled combustion, the
temperatures at the catalyst were not sufficient for the catalyst
19
-------
to be effective. The overall process resulted in the furnace
cycling "on and off" more frequently.
Another possible explanation for the difference in
catalyst versus noncatalyst results was the timely manner in
which the samples were analyzed. All samples for all tests were
measured for total particulate within 24 to 36 hours after the
tests. The separate components were then stored for analytical
analysis. The samples were then extracted within 30 days after
the measurements for total particulate. The extracted samples
were then stored in a freezer until all the tests were completed.
The non-catalyst samples were stored for nearly 6 months while
the catalyst samples were stored for 45 days. The non-catalyst
samples were analyzed well outside the test method specified hold
times. Based on experience on a number of prior projects,
however, it is believed that the without catalyst PAH data were
not severely compromised by this delay.
Furnace A results for the low heat output without
catalyst runs (tests A-5 and A-6) and both tests with the
catalyst in place (tests A-7 and A-8) are suspect because the
weigh scale showed.periods of weight gain near the end of each
test (see Appendix D, Run TTD-1A, for example). These tests were
continued until the scale reached zero as specified in the
method. The reasons for the weight increases are not known;
possibilities include a shift in the plumbing to the heat
exchanger which placed more weight on the scale or moisture
condensation in the furnace-stack system (although the latter
seems highly unlikely). The plastic plumbing looped from the
back of the furnace, across the laboratory floor, and then up to
the heat exchanger mounted on an 8 ft high shelf. It is very
possible that the piping was bumped or changed position due to
thermal stresses during the suspect tests. The data from these
tests are consistent with the other results so they are included
in the tables, but should be treated with caution, especially the
values calculated on a emission per hour basis. The values
calculated on an emissions per unit weight of fuel and per unit
heat value are less likely to have been affected by the weigh
scale anomaly. These anomalies occurred late in each test during
the final phase of the charcoal burn when very little particulate
was being generated.
The laboratory which tested Furnace A was equipped with
two CO monitors in the stack, one calibrated over a 0-5000 ppm
range, the other over a 0-5% range. A third CO monitor,
calibrated over a 0-2000 ppm range analyzed samples from the
dilution tunnel. At some point during all tests on Furnace A,
the stack low range instrument and the dilution tunnel CO monitor
experienced CO concentrations exceeding their respective high
limits. Under this condition, the instruments are effectively
pegged and the readings are useless. Therefore, the Furnace A
CEM data in Appendix D include the minute readings on these two
monitors but no average is shown since it would be incorrect.
Two basic furnace designs (single and double pass boiler
heat exchanger) were chosen for these tests to see if this
impacted emissions. Table 4-4 presents the particulate and PAH
20
-------
emission factor data and efficiency aggregated by furnace and
operating mode. Furnace A with the prototype catalyst showed
markedly higher PAH emissions compared to the standard Furnace A.
Furnace B showed much less variability in operation and emissions
data compared to Furnace A, Whether this is due to (1) furnace
design, (2) the way the fuel was loaded, and/or (3) the
differences in the draft on/off cycles cannot be determined
without further tests; more than likely, all three variables
exerted significant influences.
Table 4-5 lists the emission results for various
residential combustion devices. Furnace A test results (the next
to last line in Table 4-5) are the average of the four tests(A-3
through A-6) shown in Table 4-la. The test results from Furnace
B (the last line in Table 4-5) are included as an average from
all four tests (B-l through B-4). Note that all particulate
emission values have been converted to the EPA Method 5H
equivalents. The levels of PAHs in the emissions are comparable
to EPA-certified wood stoves. The data presented in Table 4-5
were originally generated by different researchers using a
variety of sampling and analytical methodologies. A number of
assumptions had to be made to "normalize" the data for
comparison. Consequently, only order of magnitude differences
should be considered significant. Readers are encouraged to
review the reference cited in the footnote for a more thorough
understanding of the data.
Figures 4-2 and 4-3 present results for the individual
PAH compounds for each test on Furnaces A and B, respectively.
In testing Furnace B, dual MM5G sampling trains were used and the
PAH results from each train are presented separately in Figure 4-
3 to illustrate the excellent precision achieved. The target
compounds•are listed in order in Table 2-3.
These tests were designed to provide Wisconsin DNR with a
first look at emissions from residential wood burning furnaces.
The differences in fuel load configuration and draft on/off
cycling time make it difficult to discern any significant
difference between the results from the two furnaces. If further
emissions testing is conducted, it should be designed to verify
the measured results and further investigate the effects of
variations in furnace design (including the draft on/off cycle
time) and operating protocol.
21
-------
TABLE 4-la. SUMMARY OF TEST RESULTS - FURNACES A AND B COMPARATIVE DATA.
Furnace / Test /
Condition
Furnace A/A-3/high
heat removal
Furnace A/A-4/high
heat removal
Furnace A/A-5/low
heat removal"
Furnace A/ A- 6 /low
heat removal3
Furnace B/B-1/high
heat removal
Furnace B/B-2/high
heat removal
Furnace B/B-3/low
heat removal
Furnace B/B-4/low
heat removal
Wood
Load
(wet
Ibs)
87.0
81.2
80.5
83.0
133.0
136.9
125.3
139.5
Coal
Bed
(Ibs
)
21.3
12.0
30.0
18.5
29.5
29.5
28.0
28.0
Moisture
{% dry
basis}
23.9
22.1
21.8
20.4
23.7
23.7
24.7
23.6
Average
Burnrate
(dry
kg/hr)
5.86
4.11
2.42
2.81
3.36
2.84
1.51
1.68
Average
Delivered
Efficiency
(%)
38.8
53.4
46.4
42.4
50.5
57.1
55.4
55.1
Particulate, SPA Method 5G
g/hr
143.2
61,0
38.5
48.6
36.5
37.6
14.3
15.5
g/kg
of dry
fuel
24.5
14.8
15.9
17.3
10.8
13.3
9.5
9.2
mg/Btu
output
3.55
1.56
1.93
2,30
1.21
1.31
.0.96
0.94
mg/MJ
output
3361
1482
1829
2177
1145
1238
911
892
mg/MJ
input
1305
791
849
924
579
707
505
491
a. Weigh scale data suspect; per hour data therefore suspect. Per kg and per heat unit data not as likely
to have been affected.
-------
TABLE 4-lb. SUMMARY OF TEST RESULTS - FURNACE A SCOPING AND PROTOTYPE CATALYST DATA.
Furnace/Test/
Condition
Furnace A/scoping
test A-l/high heat
removal
Furnace A/ scoping
test A-2/ high heat
removal
Furnace A/with
catalyst test A-7/
high heat removalb
Furnace A/with
catalyst test A-8/
low heat removal13
Wood
Load
(wet
Ibs)
82.5
83.5
84.0
87.5
Coal
Bed
(Ibs)
NAa
NA
NA
NA
Moisture
(% dry
basis)
29.0
25.1
21.7
18.9
Average
Burnrate
(dry
kg/hr)
4.14
3.95
4.73
2.49
Average
Delivered
Efficiency
(%)
58.9
58.2
47.6
54.4
Particulate, EPA Method 5G
g/hr
35,1
49.9
53.8
37.8
g/kg
of dry
fuel
8.5
12.6
11.4
15.2
mg/Btu
output
0.81
1.22
1.35
1.58
mg/MJ
output
767
1158
1276
1492
mg/MJ
input
452
674
583
812
*^> a. Data not available for these tests.
b. Weigh scale data suspect; per hour data therefore suspect. Per kg and per heat unit data not as likely
to have been affected.
-------
TABLE 4~2a. ORGANIC EMISSIONS SUMMARY - FURNACES A AND B COMPARATIVE DATA.
Furnace/lest/
Condition
Furnace A/A-3/high
heat removal
Furnace A/A-4/high
heat removal
Furnace A/A-5/low
heat removal"
Furnace A/A-6/low
heat removal*
Furnace B/B-1/high
heat removal
Furnace B/B-2/high
heat removal
Furnace B/B-3/low
heat removal
Furnace B/B-4/low
heat removal
Gravimetric Analysis
g/h
90.5
42.0
27.1
33.3
23.2
21.6
9.41
10.0
mg/MJ in
823
546
597
632
370
407
329
319
Total Chromatographable
Organics
g/h
3.75
2.84
8.31
4.53
3.83
5.40
3.00
2.33
mg/MJ in
34.2
36.8
183
85.9
61.0
102
105
74.1
Polyeyelic Aromatic
Hydrocarbons
g/h
2.80
0.890
0.594
0.641
1.09
0.893
0.356
0.557
mg/MJ in
25.5
11.6
13.1
12.2
17.5
16.8
12.5
17.7
a. Weigh scale data suspect; per hour data therefore suspect,
been affected.
Per heat unit data not as likely to have
-------
TABLE 4-2b. ORGANIC EMISSIONS SUMMARY - FURNACE A SCOPING AND PROTOTYPE CATALYST DATA.
Furnace/Test/
Condition
Furnace A/scoping
test A-l/high heat
removal
Furnace A/ scoping
test A-2/high heat
removal
Furnace Awith
catalyst A-7/ high
heat removal*
Furnace A/with
catalyst A-8/ low
heat removal*
Gravimetric Analysis
g/h
24.9
28.1
20.7
54.6
mg/MJ in
321
380
234
1170
Total Chromatographable
Organic s
ff/h
1.57
5.93
26.7
42.8
mg/MJ in
20.3
80.1
301
917
Polycyclic Aromatic
Hydrocarbons
g/h
0.543
0.435
2.58
2.68
mg/MJ in
7.00
5.88
29.1
57.4
N)
U>
a. Weigh scale data suspect; per hour data therefore suspect,
been affected.
Per heat unit data not as likely to have
-------
TABLE 4-3a. GAS CONCENTRATIONS - FURNACES A AND B COMPARATIVE DATA.
Furnace /Test /Condition
Furnace A/A-3/high heat removal
Furnace A/A-4/high heat removal
Furnace A/ A- 5 /low heat removal
Furnace A/A- 6 /low heat removal
Furnace B/B-1/high heat removal
Furnace B/B-2/high heat removal
Furnace B/B-3/low heat removal
Furnace B/B-4/low heat removal
02 %
9.70
9.55
11.01
9.92
15.76
16.09
15.40
15.38
CO2 %
10.42
10.30
8.82
9.61
4.01
3.71
4.68
4.63
CO %
2.44
1.79
1.46
1.75
0.93
0.78
1.27
1.10
THC ppm
Naa
Na
Na
Na
Na
Na
Na
Na
a.
Hydrocarbon analyzer not available for these tests.
TABLE 4-3b. GAS CONCENTRATIONS - FURNACE A SCOPING AND PROTOTYPE
CATALYST DATA.
Furnace /Test /Condition
Furnace A/scoping test A-
1/high heat removal
Furnace A/ scoping test A-
2 /high heat removal
Furnace A/with catalyst
A-7 /high -heat removal
Furnace A/with catalyst
A-8/low heat removal
03 %
14.27
15.59
11.08
13.52
CO2 %
6.38
5.16
9.39
7.32
GO %
1.15
0.62
1.37
0.95
THC ppm
1057
1640
2533
1358 •
TABLE 4-4.COMPARITIVE DATA AGGREGATED BY OPERATING MODE AND FURNACE
[RANGE IN { }].
Operating
Mode
High Heat
Low Heat
removal
Furnace
A
19.6 (14.8-24.5)
0.347(0.216-0.478)
45.6 (38.8-53.4)
16.6 (15.9-17.3)
0.236 (0.228-
0.245) 44.4 (42.4-
46.4)
B
12.0 (10.8-13.3)
0.319 (0.315-0.324)
53.8 (50.5-57.1)
9.35 (9.2-9.5)
0.283 (0.235-0.332)
55.2 (55.1-55.4)
Parameter
M5G Particulates, g/kg
PAH, g/kg
Delivered Efficiency, %
M5G Particulates, g/kg
PAH, g/kg
Delivered Efficiency, %
26
-------
TABLE 4-5. OVERALL COMPARISON OF RESIDENTIAL WOOD, OIL, AND GAS COMBUSTION EMISSIONS3
Combustion Device
Natural gas furnace
Conventional
High Efficiency
Oil Furnace
Retention head
Conventional
Conventional wood stove
Certified wood stove
Non- catalytic
Catalytic
Pellet (certified)
Pellet (exempt)
Fireplace
Wood furnace
Cor dwood- Swedish
lab tests
Intermittent
firing
Continuous
firing
Chips (dry)
U.S. EPA lab tests (Ais report)
Fttrnufi $
Furnace B
M5H Particulate, mg/Ka input
0.44.
0.43
3.2
15.1
786
383
425
110
176
907
1862
182
45.3
1048
681
PAHs, mg/MJ input
0.000124
0.000028
e
--
40
28
24
0.082
0.014
41
--
15.3
<0.02
15.6
16.1
Hutagenicity, krev/KJ input*
0.007°
NDc.d
6
20
600
100
--
--
--
--
148f
0.48f
--
to
a =
b
c
d
e
f
g
All data except that in italics taken from: McCrillis, R.C., "Review and Analysis of Emissions Data for
Residential Wood-Fired Central Furnaces," In Proceedings of the
Annual Meetingof the AMMA,
Air & Waste Management Association, San Antonio, TX, June 1995, Paper No. 95-RP137.04.
Microsuspension assay, TA98+S9 unless otherwise noted.
Ames plate incorporation assay, TA98+S9.
ND means not detected.
No data available for this parameter.
Ames plate incorporation assay, TA100+S9.
Only includes comparison data.
-------
to
oo
03
Particula
/MJ input
O p
in fc
5
1400
1300
1200
1100
1000
900
800
700
600
500
400
PARTICULATE vs BURNRATE
i
-
A
Tr |
i e |
•
&&
i , i , i , i , i
I 834567
Bumrale (kg/h)
SErv
smivolatile Organics
mg/MJ input
in
1IVC
900
800
700
600
500
400
300
200
100
0
>LATILE ORGANICS vs BURNRATE
h V
-
-
"ff
A
m ™ fi "A A
-.,.,. A ... A, .
1 234567
Bumrate (kg/h)
cc
Sensible Organics
mg/MJ input
§
o
)ND
1400
1200
1000
800
600
400
200
0
ENSIBLE ORGANICS vs BURNRATE
1 v
: i
- Ha fi I i
V
234567
Bumrate (kg/h)
70
60
50
PAH
mg/MJ Input
8 §
20
10
0
PAH vs BURNRATE
•vc
•vc
« • »
• * * m
1,1,1,1,
234567
Bumrate (kg/h)
Figure 4-1. Summary of particulate and organic emissions data for wood-fired furnnaces A and B.
-------
Run TDD-1 A, Low Bum R*e
111 •
6 I I • 10 1t 12 13 M )S W t7 18 IB »
T*fM CWnfWOiKl (mt T»bb 2-])
Run TTO-1B, Low Bum Rate
2 3 4 5 6 r 8 8 IS 1! 12 13 14 15 16 1? 10 18 26
Tirpx Compoond (MM Ttble 2-3}
Run TTDD-2A, Scoping T«l I, High Bum Rate
Run TTD-2B, Scoping Trai 2, High Bum Rate
It
•§
I ?00
II
I MO
1 2 14 56 ) 8 » 10 It 12 13 M IS W 17 18 18 20
Tat* Compound (m* T«bk ]. J)
I 2 3 4 S 6 ! f » 10 11 12 IJ 14 15 16 17 18 18 20
Tiqyt Compound (me Ttbk 2-}}
Run TDD-2C, High Bum Rjle
Run TDD-2D, ffigh Bum Rale
11,1
ll
»1lt213M1SW)7t8»20
(at TlUi 2-3)
t 2 > 4 S » 7 8 » 10 11 12 H M IS 18 17 18 IB 70
(in T«bfc 2-3)
Run TTCD-1, CaalyB T«t, Low Bum RMt
Rl» TTCD-2, CtHlyil Tat, High Biira Rale
iLld.
2 3 4 5 E 7 S 8 W t1 12 13 14 IS 1« 1? 18 18 20
Tvfd Conpcmd (M« Titic 2-})
t ? 3 4 5 6 7 8 9 W (1 12 13 M IS *6 1? *8 19 20
"tap! Qmtix«na (n Tiblt M)
Figure 4-2.
PAH Results for Furnace A.
Identified in Table 2-3.)
(Target Compounds are
29
-------
I *06
r-
$90
400
I JOO
if
f 200
X
too
0
400
If**
1 "*
190
400
g 300
It
too
0
Rim * 1, Low Bora Rale. SampfagTnm A
-
.1 ... ..
TvKt f'^'iinnnl (tec TiMc 2-3)
Run # 3, Low Bum Rale, S«mpLmg Train A
L .
Tan* Cgqm>l(tcc T*k 2-1)
Rim If 2, High Bum Rate. Sampling Train A
...LI
Tup! *"— T— ' toe T*fc }.])
Run X 4. High Bum Rate, San^bdgTram A
.1
T*ga Ceapanl (we T*k )-l)
400
1 *°
too
400
I »0
M
1 **
100
0
400
1 MO
t
I ™
100
1 300
It
| 300
100
0
Rn * 1. Low Bum Rate, Sampling TnmB
-
I.I
Tops Cmtmad (« T«fc4c }.})
RBD * 3, Low Bum Rale, Sampling Tnm B
ROD * 2, High Bora Rate, Sampling Tnio B
I —••-.•
T»»a Coqnnl (m TAIt M)
Run * 4, High Bora Rate. Sunplmg Tram B
•1 - .-•• _
Figure 4-3.
PAH Results for Furnace B.
Identified in Table 2-3.)
(Target Compounds are
30
-------
SECTION 5 - CONCLUSIONS
There were several data quality problems with tests of
Furnace A, all of which, although significant, are thought to be
small enough to not bias the results for Furnace A sufficiently
to cause an order of magnitude error. Tests of Furnace B had no
reported data quality problems. All tests of Furnace B
particulate matter emissions were in the range of 36.5 to 37.6
g/hr (high heat removal rate - tests B-l and B-2) and 14.3 to
15.5 g/hr (low heat removal rate - tests B-3 and B-4) as shown in
Table 4-la. Particulate matter emissions from Furnace A appear
consistently higher but, within the limits of these tests,
experimental error, and considering the testing problems
previously discussed that may have compromised the data quality
for Furnace A, a direct comparison of Furnace A and Furnace B
emissions is without adequate foundation and therefore is not
meaningful. However, from inspection of Table 4-5, it is evident
that all wood-burning home heating combustion equipment,
including wood stoves, boilers, and fireplaces, has much higher
particulate matter emissions than gas-fired or oil-fired home
heating furnaces.
31
-------
Appendix A - Thermocouple Calibration Data
Al
-------
FURNACE A THERMOCOUPLE CALIBRATIONS
DATE: July 10, 1995
NAME: Joseph Valenti and Russell Logan
TEST: Emissions from wood-fired residential heating furnace
DATA ACQUISITION
Fire Box
Stove Exit
Stack
Dilution
Ambient
Water In
Water Out
BOILING WATER
°F
211,4
212.6
212.8
211.7
212.6
210.7
210.7
ICE WATER AMBIENT % DIFFERENCE
Op
32.4
32.4
32.4
32.4
32.4
32.4
32.4
3
3
68
68
68.0
68.3
69.1
67.4
68.0
0.56
0.11
0.22
0.39
0.11
0.94
0.94
METER BOX
Dilution
Filter
Inlet
Condenser
Temp Out
213
213
211
213
212
31
32
32
31
32
67
68
68
68
67
1.11
0.56
0.56
1.11
0.00
A2
-------
FURNACE B THERMOCOUPLE CALIBRATIONS
DATE: April 13,1995
TEST: Emissions from wood-fired residential heating furnace
Thermocouple Number BOILING WATER ICE WATER % DIFFERENCE
°F °F
1-Flue Gas 211 32 0.56
2-Room Temperature 211 32 0.56
3-Dry Bulb-Tunnel 211 32 0.56
4-Wet Bulb-Tunnel 211 32 0.56
5-Unit Top 211 32 0.56
6-Unit Back 211 32 0.56
7-Unit Right Side 211 32 0.56
8-Unit Left Side 211 32 0.56
9-Unit Bottom 211 32 0.56
10-Catalyst Downstream 211 32 0.56
11-Catalyst Center 211 32 0.56
12-(not used) 211 32 0.56
13-(notused) 211 32 0.56
14-(not used) 211 32 0.56
15-(not used) 211 32 0.56
16-(not used) 211 32 0.56
17-DGM in 211 32 0.56
18-DGM out 211 32 0.56
19-Filter 211 32 0.56
20-DGM in 211 32 0.56
21-DGM out 211 32 0.56
22-Filter.(2) 211 32 0.56
A3
-------
Appendix B - CEM Calibration Data
Bl
-------
FURNACE A CEM CALIBRATIONS
DATE: July 10, 1995
NAME: Joseph Valenti and Russell Logan
TEST: Emissions from wood-fired residential heating furnace
CEM ANALYZER
CO high
CO low
CO dilution
02
C02
SYSTEM BIAS
CO high
CO low
CO dilution
02
C02
AMBIENT
CO high
CO low
CO dilution
02
C02
ZERO
0 ppm
0 ppm
0 ppm
0.06 %
0.02 %
ZERO
0 ppm
0 ppm
0 ppm
0.04 %
0.02 %
61 ppm
0 ppm
2 ppm
20.66 %
0.05 %
SPAN ACTUAL
39307 ppm 39400 ppm
3760 ppm 3760 ppm
2004 ppm 2060 ppm
9.61 % 9.7 %
6.4 % 6.0 %
CALIBRATION ERROR
0.186
0
2.8
0.36
1.48
SPAN ACTUAL % SYSTEM BIAS
10132 ppm 10060 ppm 0.144
2093 ppm 2060 ppm 0.66
467 ppm 465 ppm 0.1
15.01 % 15 % 0.04
15 % 15 % 0
B2
-------
FURNACE B CEM CALIBRATIONS
DATE: June 28,1995
TEST: Emissions from wood-fired residential heating furnace
CEM ANALYZER
CO
02
C02
ZERO
0 %
0 %
0 %
SPAN
9.99 %
24.5 %
20.93 %
ACTUAL
9.99 %
24.50 %
20.93 %
% CALIBRATION ERROR
0
0
0
CAL GAS #1
CO
02
C02
CAL GAS #2
CO
02
C02
CAL GAS #3
CO
02
C02
AVERAGE
CO
02
C02
ACTUAL SHOULD BE % SYSTEM BIAS
0.93 % 0.987 % 5.78
10.2 % 10.05 % 1.49
9.43 % 9.99 % 5.61
ACTUAL SHOULD BE % SYSTEM BIAS
2.27 % 2.36 % 3.81
5.69 % 5.55 % 2.52
5.58 % 5.88 % 5.10
ACTUAL SHOULD BE % SYSTEM BIAS
7.68 % 7.94 % 3.27
17.58 % 17.53 % 0.29
19.05 % 19.89 % 4.22
% SYSTEM BIAS
4.29
1.43
4.98
B3
-------
Appendix C - Water Meter Calibration Data
Furnace A water meter flow calibration.
DATE: July 10, 1995
NAME: Joseph Valenti and Russell Logan
TEST: Emissions from wood-fired residential heating
furnace
water density: at 68°F= 8.3317 Ib/gal, at 150°F = 8.1818 Ib/gal
water temp, during calibration = 150°F
TRIAL
1
2
3
4
5
6
7
ROTAMETER
reading, gpm
4.60
4.50
4.30
4.50
6.20
6.10
6.20
FLOW
Ib/min meas .
39.50
39.56
37.68
38.60
51.24
51.33
51.40
FLOW
gpm calc .
4.83
4.84
4.61
4.72
6.26
6.27
6.28
%
difference
4.72
6.93
6.63
4.62
1.00
2.77
1.31
Average
Calibration
factor
1.04951
1.07447
1.07101
1.04839
1.01010
1.02847
1.01326
1.04217
Furnace B water meter flow calibration.
Test laboratory water meter calibration.
Water temperature not recorded.
Calculated
Gallons
18.29
29.67
30.52
32.13
Observed
Weight
152.3
247.1
254.2
267.6
Assumed
Density
8.326955
8.328278
8.328965
8.328665
Observed
Gallons
20.31
32.59
33.54
35.46
Average
Calibratioi
Factor
0.90032
0.91032
0.90995
0.90606
0.90666
Cl
-------
Furnace A water flowmeter calibration.
gpm actual = 0.72202 + 0.89974*(gpm observed)
6.5
o
K)
-I— '
o
I 5.5
D)
4.5
linear curve fit
calibration data
4.5 5 5.5
gpm
Flowmeter reading
6.5
-------
60
Density of water as a function of temperature
Density (Ib/gal) = 8.3654 + [F * (1.26x1 OM)] + [FA2 * (-8.98x10A-6)]
Marks' Standard Handbook for Mechanical Engineers, 7th Edition
Quadratic regression
80
gal = 0.1337ftA3
j
100
120 140
Deg. F
Water Temperature
160
180
8.4
8.3
8.2 -I t
-Q
-------
Appendix D - CEM Run Data
Dl
-------
FURNACE A WITHOUT CATALYST, HIGH HEAT REMOVAL RATE
02-Apr-96
IS.Jun-95
Run TDD-2A Scoping test 1
tine stack exit dMion H2Oii H2Oout firebox ambienl Move exit
"c degF degF degF degF degF degF degF
328 137 81 114 126 195 68 151
388
448
508
568
626
688
748
806
866
926
988
1048
1108
1168
1228
1288
1348
1404
1464
1524
1584
1644
1704
1764
1824
1884
1944
2004
2064
2124
2184
2244
2304
| 2384
2424
2484
2544
2904
2664
2724
2780
2840
2900
2960
3020
3080
3140
3200
3260
3320
3380
3440
3500
3560
3820
3980
3740
3800
3860
3920
3980
4040
4100
4156
4216
4278
4339
4399
4459
4519
4579
4638
4699
4759
4816
T3O
126
124
122
121
121
121
121
120
120
120
120
120
120
121
121
121
121
122
122
121
122
122
122
122
123
123
123
123
123
123
123
123
124
124
124
124
125
125
126
126
129
140
151
157
159
162
165
167
169
172
173
173
174
174
176
177
179
181
182
184
186
188
190
191
191
192
194
195
197
198
199
201
202
202
ry
77
78
76
76
76
79
79
79
79
79
79
79
77
79
79
76
76
76
76
76
76
76
76
76
76
76
76
76
78
78
76
75
76
76
76
77
77
76
76
76
77
79
81
81
81
81
82
82
83
84
83
84
84
84
84
84
85
85
85
86
88
88
88
88
86
89
67
87
87
87
88
88
88
88
114
114
114
114
114
113
114
114
114
113
113
113
112
112
112
111
111
111
112
111
111
111
110
110
110
110
110
110
109
109
110
109
108
109
108
108
108
108
107
107
107
107
107
107
107
107
107
toe
107
108
106
107
107
108
109
109
109
109
109
109
109
109
107
108
106
107
107
107
107
107
108
108
108
108
108
126
126
129
129
129
125
125
125
125
125
125
124
124
124
123
123
123
122
122
122
121
122
121
121
121
121
120
120
120
120
119
119
119
119
119
119
118
118
118
117
118
117
117
117
117
117
117
117
117
117
117
117
117
117
117
117
117
117
117
117
117
117
118
118
118
118
118
118
118
118
118
119
119
119
119
183
180
180
180
181
161
183
184
184
185
185
185
185
184
184
184
184
185
185
188
189
191
191
190
190
190
190
191
191
192
193
193
194
194
195
195
196
197
198
198
199
220
264
322
372
364
334
324
321
329
336
340
339
338
338
340
341
346
351
357
362
366
375
399
400
392
391
393
396
403
411
417
419
419
419
68
68
68
68
88
88
88
88
88
88
88
68
88
88
88
68
68
88
88
88
88
88
68
68
88
68
68
67
68
68
68
68
68
68
68
68
68
68
68
88
68
88
68
88
68
88
88
68
68
68
68
88
88
88
68
88
68
68
67
67
88
88
67
67
67
67
67
68
67
67
67
68
67
68
68
143
138
135
133
131
130
130
129
129
129
128
129
129
129
129
129
129
129
129
129
129
129
130
130
130
130
130
130
130
130
130
130
130
131
131
131
131
131
131
131
131
134
145
157
165
168
174
177
179
182
184
188
186
187
187
189
192
194
196
199
202
203
204
205
204
206
207
209
211
213
215
217
219
220
220
CO high COdUton CO low O2 CO2
ppm pom pom percent percent
4488 6761 4241 1822 258
4484
8059
5998
5802
5782
5788
5741
5754
5802
5843
5880
5876
5884
5912
5953
6047
6124
9189
8287
8352
6364
6368
8470
6624
6685
6775
8873
6978
7056
7100
7182
7316
7438
7894
7890
8085
8321
8484
8500
8573
8828
8883
10335
18877
20422
18412
18180
18988
19255
19076
19837
20837
21358
21438
21484
21240
20976
20758
20830
20715
21012
21159
21407
21831
21895
21529
21016
20915
20882
20992
21159
21281
21403
21566
21655
4494
601 7
5565
533
532.7
527
5285
5254
5304
542.3
5485
5508
5539
5592
5645
5763
5881
5977
8087
621.1
627
6222
8480
8678
6802
8877
7067
7194
7332
7419
7495
7796
8032
8436
8724
9131
9551
9766
9883
9998
10088
1041
15579
19976
20073
19888
20072
20062
20063
20068
20059
20005
2003.4
19945
20041
20063
20095
20059
20031
19897
1989.7
19906
19894
19894
19969
20007
19894
1991
19896
19899
19893
19899
19899
19897
19914
4194
5011
5013
5013
5013
5012
5015
5015
5014
5013
5016
5013
5013
5015
5013
5014
5015
5013
5015
5013
5014
5016
5015
5011
5013
5013
5015
5013
5014
5013
5013
5015
5013
5014
5012
5014
5011
5013
5013
son
5013
5013
5013
5013
5014
5013
5015
5014
5012
5014
5011
5015
5013
5013
5015
5017
5012
5014
5014
5014
5014
5012
5014
5014
5013
5013
5014
5015
5013
5014
5014
5012
5015
5013
5013
1952
1877
1858
1858
1853
185
1847
1845
1842
184
1839
1837
18.36
18.35
183
183
1829
18.3
1827
1824
1821
1817
1816
1818
1816
1815
1813
1807
1808
1809
1808
1803
18.01
1798
1794
1791
1786
17.85
1763
17.8
1779
17.69
1667
1388
12.78
12.9
13.26
13.33
1335
13.31
1301
1258
12.51
1264
1272
1274
1271
1264
1254
1243
1224
1214
1201
1192
1181
11.66
11.69
1173
1175
1165
1149
11.33
1121
11 1
1104
1 62
237
248
2.45
248
252
256
257
255
257
259
2.6
263
264
269
288
2.7
2.7
277
28
279
285
281
283
286
291
294
297
298
3
299
304
308
312
319
317
328
326
331
328
331
338
457
7.25
824
803
762
741
737
739
772
814
819
807
799
8
798
804
809
82
835
847
863
867
886
894
887
677
874
889
9
9.14
925
933
938
THC b
ppm
603
418
656
707
807
589
523
508
482
457
444
437
393
380
488
488
503
479
369
426
441
552
553
601
589
533
511
534
522
581
680
882
888
888
741
700
658
634
682
704
838
905
900
854
831
1957
1985
1882
1371
1502
1528
1812
1887
2268
2027
2037
1776
1801
1691
2446
2180
1639
1947
2874
2765
2120
2681
2522
3046
2855
3392
3513
3034
2974
3570
3346
Water
Balance actual fiow rate heat out
t>s gpm Bill/Interval
825 67 6604
825
825
82
82
82
82
82
81.5
815
81 5
81 5
81.5
815
615
812
81
• 81
' 81
80S
80S
805
805
80.5
80
80
80
79.8
80
795
795
795
79
79
79
79
79
765
785
785
785
78
78
775
77
766
765
76
755
755
75
74.5
74
735
73
725
72
72
71.5
71
70.5
70
695
69
685
68
67.5
67
885
86
66
65.5
65
645
64
635
67
87
67
87
67
67
67
67
6.7
67
87
67
87
6.7
67
67
67
87
67
67
67
67
67
67
67
87
67
87
67
67
67
67
6.7
67
67
67
67
67
67
87
67
67
67
6.7
67
67
67
67
6.7
87
67
87
67
67
67
87
67
67
67
67
67
67
67
6.7
67
87
67
87
67
87
67
6.7
67
6.7
67
6494
6659
6495
6550
6495
6660
6054
6109
5999
6165
6551
6331
8331
8332
6332
6388
5859
8002
5837
6003
5763
5893
8004
5894
5950
5950
5454
5785
5730
5895
5344
5399
5786
5786
5621
595.2
5767
5897
5787
5247
5732
5843
5823
5786
5733
5457
5512
5623
551 2
5733
5623
5733
5071
5181
4483
4518
4463
4628
4828
4297
4463
4297
5196
5622
551 1
5732
567.7
6118
5953
5953
5842
5952
589.7
6118
8227
UUatw nwt*r
Draft Cool water reading
On/Off density, fo/gal gpm
Off 826 89
on
OB
on
on
OB
OB
OB
OB
OB
OB
OB
OB
OB
OB
OB
OB
Off
Off
Off
Off
on
on
Off
on
on
on
on
OB
OB
OB
OB
OB
Off
Off
Off
on
on
on
on
on
OB
OB
OB
OB
OB
OB
OB
OB
OB
OB
on
on
OB
on
OB
OB
Off
on
Off
Off
Off
OB
OB
OB
OB
OB
OB
Off
on
on
on
On
On
On
On
828
826
828
826
826
826
826
826
826
826
827
827
827
627
827
827
8.27
827
827
827
627
627
827
627
827
827
827
827
827
827
827
827
827
827
827
627
827
827
828
828
828
628
826
828
828
828
828
828
828
828
828
828
828
828
827
827
827
627
827
627
827
627
828
828
627
828
828
828
828
828
827
8 27
8 27
827
827
66
66
99
99
66
66
66
66
66
66
66
66
66
66
6.6
66
66
99
99
96
66
68
66
66
66
68
66
66
66
66
66
66
66
66
66
66
66
66
66
66
66
6.6
9.6
66
66
66
66
66
66
86
66
66
66
66
66
66
66
66
66
66
66
66
66
86
86
66
86
6.6
66
86
66
99
9.9
86
66
-------
FURNACE A WITHOUT CATALYST. HIGH HEAT REMOVAL RATE
02-Apr-98
IS-Jun-95
Run TDD-2A Scophg test f
time stack GX* dttjtion H2O In H2O out fire best ambit* stove eg£
sec d»0F (JeoF dtjF degF dejF degF deoF
4876 202 88 108 119 419 88 220
4936
4996
5056
5116
5176
5236
5299
5356
5416
5478
5512
5592
S8S2
5712
5772
5832
5892
5952
6012
6072
6132
6192
6252
6312
6372
6432
6492
8552
8812
8672
8712
8792
9852
d9908
9996
OJ 7028
7088
7148
7208
7288
7328
7388
7448
7508
7568
7628
7688
7748
7808
7868
7828
7988
8048
8108
8168
8228
8284
8344
8404
8464
8524
8584
8644
8704
8764
8824
8684
8944
9004
9094
9124
9184
1244
9304
9364
201
201
198
193
191
190
lit
111
190
111
19;
199
194
191
197
197
195
195
195
1M
197
1(6
195
1(4
194
193
193
194
195
1(5
196
19?
188
KB
199
203
206
202
19?
193
IBS
in
189
its
184
183
183
181
182
182
183
183
164
164
184
184
184
184
184
184
184
183
184
184
185
186
198
190
190
110
191
180
1H
1BO
190
86
87
87
66
66
85
85
86
88
86
86
86
87
86
67
89
86
86
86
96
8?
8?
M
86
86
86
88
86
86
88
88
8?
88
89
86
87
88
87
89
86
89
85
85
15
84
65
84
84
64
84
84
94
84
84
84
84
84
64
84
84
84
84
84
85
85
85
85
85
85
85
85
85
89
89
85
109
109
109
109
109
109
109
tot
100
109
108
108
109
109
108
109
109
108
109
109
109
IN
too
109
110
110
110
110
110
110
110
109
no
111
110
110
no
no
110
110
110
110
110
110
111
110
111
111
111
111
111
110
lit
110
110
111
111
111
111
110
111
110
110
111
111
111
111
111
111
111
111
111
111
111
111
119
120
120
120
120
120
120
120
120
120
120
120
120
120
120
120
121
121
121
120
121
121
121
121
121
121
121
122
122
121
122
121
122
122
122
122
122
122
122
123
123
123
123
123
123
123
123
123
123
124
123
124
124
124
124
124
124
123
124
124
124
124
124
124
124
124
124
124
124
124
124
124
125
125
125
421
4(9
430
434
436
416
415
419
443
445
44(
4S4
463
472
476
474
472
474
474
476
4M
504
489
477
479
480
488
491
497
502
SOI
505
511
520
$24
531
534
527
518
512
509
909
904
903
902
502
504
903
903
909
908
512
521
521
523
528
928
931
934
937
918
940
941
946
950
957
568
571
578
578
580
575
573
974
574
67
67
68
67
68
88
68
6?
68
ire
98
66
88
88
88
87
87
88
98
98
88
68
68
98
88
68
67
87
6?
87
87
87
67
67
67
67
67
67
6?
6?
8?
67
87
67
67
67
67
66
67
81
61
6?
67
67
67
67
67
67
67
87
87
87
97
87
67
67
88
6?
87
66
67
68
68
69
67
221
219
216
213
210
208
208
208
210
210
212
213
216
219
221
220
218
21?
21?
216
21?
21?
215
214
214
213
213
214
214
216
21?
216
219
220
221
225
22B
22S
220
21S
212
209
20?
208
205
204
201
203
203
204
201
205
209
208
206
205
205
205
209
209
205
204
205
208
20?
208
211
212
213
215
215
216
211
218
219
COMsh COdoHon COtew O2 CO2
Ptm pern fsm ferewt percent
21399 1(89.6 5015 1102 9,4
21000
20752
20634
20908
20060
19470
18(11
18205
17926
18888
19821
18320
11124
1(104
19(43
20085
20154
28475
20133
20723
21472
21733
22160
22408
22489
22803
22844
22705
22607
22319
21851
21472
21086
20915
20038
20190
1(795
1(290
18183
17778
17480
17362
17362
17486
17509
17181
17407
171S4
17171
1728S
17196
17236
17310
17200
17118
17021
16935
16886
16862
16805
18842
16854
16614
16606
16772
16(68
17236
17371
17074
8354
1281?
2003.4
2004.1
1990S
2006
2006.2
2008.5
2005.9
2005.5
20059
2001.7
2006.2
20005
2005,9
2006.5
2006
2006.5
2006.7
2008.7
2006.8
2006.7
2006
2009
2006.6
2008.3
2007.2
2004.7
1(941
1(90,9
1868 3
1(88.8
19997
19698
19894
19933
20029
20052
2005.2
2007.3
2008.2
2009.5
2009.3
2006.7
20059
2009
2009.7
2009.2
20093
2005.5
2006
2006.8
2006.8
2008
2005.7
2008-5
2006.7
20067
20062
20055
2005.5
2007.3
2006.2
20072
2005.5
2006
2005-9
2006
20041
2006.2
2005.9
20066
20063
20068
2006.5
2009.3
2005-7
5012
5012
5012
5013
5013
5012
9013
9012
5013
SOI 3
9013
9011
5011
5014
5013
5013
5015
9011
9011
9013
5014
5011
5011
5012
5012
5013
5013
5015
5014
5013
5011
5015
5011
5014
5011
5013
50M
5011
5014
5013
5015
SOU
5013
5015
5013
5014
5013
$013
$011
5014
5016
9012
5015
5014
5011
5012
9014
5014
5011
5015
5011
SOU
5011
5014
5014
5014
5013
5012
9011
3)91
4018
11.05
11.07
11.09
11.24
1159
1196
12.21
1225
12.18
1334
1241
12.67
13,08
11.47
11.28
11.11
11
1079
10.92
11 16
11.11
1104
1095
1081
10.7
10.68
10.71
10.62
106
10.43
1042
1026
to
1042
1102
11.44
11.74
11.97
12.04
12.11
1218
1216
12.11
12.07
1203
12.08
12.08
12.02
11.78
11.72
1181
1188
11.9
1187
11.79
11 74
11.69
11.87
11.81
11.55
1148
114
11 13
1076
1066
10.6
1046
10.39
10.58
1494
14.58
(.15
937
(.29
(.08
8.81
1.51
145
939
• 41
9.2
(.76
1.5
(.23
(.21
94
•J
8,68
(.95
(.77
(.44
946
(.51
(.59
(76
989
• 84
9.82
993
8.99
10.07
10
10.2
1047
10.02
9.47
9.17
«J2
8.7
8.62
8.99
847
849
8.55
8.99
198
195
894
8.99
8(1
8.8
8.74
874
868
889
8.76
8.78
8.81
8,89
8,89
8.67
6.96
8.96
(.31
(.98
(.61
(.71
9 S3
(.87
».?1
5.18
6.65
UUator UU*»
THC bitanee aetiial flow rat* ten a*
ppm t» gpm BtufcttfVl!
3281 81 97 «!!.?
3558
3136
2965
2955
2794
2914
3084
3008
2729
2730
2879
2465
2973
2966
2769
3125
2818
229?
2774
2816
2750
2577
2564
2970
3306
2469
2436
3005
2728
3282
3050
2624
2554
2415
2806
2603
2426
2695
288?
2082
2182
2908
2841
2311
2476
2436
2458
2213
2223
2718
2144
2028
1978
2018
2057
2183
2199
2319
2476
1898
1938
1980
2230
2240
2021
2138
2108
1861
180?
1823
1696
1807
1831
1812
2022
82.5
82
61 S
61
60.S
60
S8.7
593
S»
SS.S
58
57.5
S7
56.5
99
S9.9
59.S
S4.(
54.S
94
535
53
925
52
51.5
SI
50.5
90
495
41.9
4(
415
46
47.5
4?
48.S
48.5
46
45,5
45
4$
44.5
44
43.S
43.5
43
42.5
42
41 .t
41.5
41
40.5
40.5
40
40
39.5
39
39
38.5
38
M
17.5
17,2
37
38.5
365
36
15.5
3S.S
35
34.5
34.5
M
33.5
W.S
• 7
6.7
6.7
6.7
6.7
6.7
6.7
8.7
6?
6.7
8.7
a.?
6.7
67
67
9.7
6.7
8.7
67
6.7
6?
6.7
6?
67
67
67
67
67
6.7
8?
8?
8.7
6.7
9.7
6.7
67
67
6.7
6.7
6.7
8.7
6.7
6.7
6?
6?
6.7
6?
6.7
9.7
6.7
6.7
6.7
8.7
8.7
8.7
87
87
67
8.7
6.7
8.7
6.7
6.7
6.7
6.7
87
6.7
67
6.7
6.7
8.7
6.7
9.7
6.7
6.7
578.6
5896
599.1
5991
599.0
9840
6008
5850
817.1
586.1
913.7
911.6
944.7
639.2
65S.8
619.2
650,2
672.1
9867
6228
6501
691.2
655.7
690.1
617.0
805.9
890.1
055 «
621.0
•190
672.1
666.6
586.4
622.4
661.0
644.4
688.8
672.0
8610
883.0
710.8
710.8
983.0
914.0
988,5
719.1
6(4.0
>96.4
982.9
709,0
9*8.4
741.8
705.0
741.8
727.1
663.1
710.5
877.4
718,0
721 ,5
7270
738.1
738.1
731.0
727.0
732.5
727.0
704.9
749.0
732.5
743.5
754.5
MM
7600
749.0
Draft Cool witer reading
Onftxi dens*?, fe/glrt gpm
On 8.27 B6
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
8.2?
8.27
8.27
8.J7
•.27
•.27
1.27
• 2?
• 2?
82?
8.2?
8.27
8.27
8.27
8.27
8.27
8.27
8.27
8.27
8.27
8.27
8.2?
8.27
8.27
827
8.27
8.27
8,27
8.27
8.2?
8.27
8.2?
6.27
6.27
8.27
8.27
8.27
8.2?
8.2?
827
82?
• 27
•.27
8.2?
8.27
8.27
8.27
8,2?
8,2?
8,2?
8.2?
8.2?
8.2?
8.27
S.27
8.27
8.27
• 27
».27
8-27
8.27
8.27
8.2?
827
6.27
8.27
8.27
827
8.27
8.27
827
8.27
8.27
6.27
8-27
6-6
6.6
6.9
96
6.6
6.6
6.8
86
96
9.6
6.8
6.6
6.6
66
8.8
6.6
6.6
6.6
86
66
6.6
6.6
6.6
66
66
66
66
6.6
•.6
6.6
8.6
6.6
66
6.6
95
6.6
6.9
69
6.6
6.6
6.6
96
9.6
96
66
66
68
66
6.6
6.6
6.6
86
6.6
66
68
9.6
6.6
6.6
8.6
66
6.8
6.6
6.6
8.6
6.6
6.6
9.6
6.6
66
• 6
6.9
66
9-6
68
66
-------
FURNACE A WITHOUT CATALYST, HIGH HEAT REMOVAL RATE
02-Apr-M
2
15-Jurv95 Run TDD- 2A Scoping test 1
time stack ex* oUlon H2Oln H2Oout flreboi ambient stove ext CO high COdUton CO low
sec degF degF degF degF degF degF degF
9424 190 85 111 125 576 67 216
9484
9544
9604
9860
9720
9780
9840
9900
9090
10020
10080
10140
10200
10290
10320
10380
10440
10500
10590
10820
10980
10740
10800
10880
10920
10980
11030
11099
11159
11219
11279
11339
11399
] 11455
11516
• 11576
11936
11996
11756
11816
11876
11936
11999
12059
12119
12179
12239
12298
12359
12412
12472
12532
12592
12952
12712
12772
12832
12892
12952
13012
13072
13132
13192
13252
13312
13372
13432
13492
13552
13612
13672
13732
13798
13848
13908
190
190
190
190
190
169
188
188
167
168
168
168
190
192
191
189
187
186
185
164
183
183
183
184
184
184
184
188
186
187
188
187
186
188
189
188
188
167
187
167
167
188
182
179
176
175
174
173
173
172
172
171
171
170
170
171
173
174
175
175
175
175
176
176
175
173
172
171
170
199
169
198
167
197
196
85
85
85
65
85
85
85
85
85
85
85
84
65
85
85
84
84
84
84
83
83
83
83
63
83
83
84
83
84
84
84
83
83
84
83
84
83
63
83
83
83
83
82
82
81
81
81
81
81
61
81
81
80
81
81
81
81
81
81
61
61
81
82
61
81
81
81
81
60
60
60
60
80
80
60
112
112
112
112
112
112
112
112
113
112
112
112
112
112
112
113
113
113
113
113
113
113
113
114
113
114
114
114
113
113
114
113
113
114
114
114
115
114
114
115
114
115
115
115
115
115
116
116
115
115
116
116
115
115
115
116
115
115
115
115
116
115
116
116
116
115
116
115
116
115
117
115
116
116
116
125
125
125
125
126
126
126
126
126
126
126
126
129
127
127
127
127
127
127
127
127
127
127
127
127
127
127
127
128
128
128
128
128
128
128
128
128
128
128
129
129
129
129
130
129
129
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
576
580
581
582
579
577
576
574
575
576
575
577
599
949
938
611
593
588
581
578
578
579
581
581
583
585
585
589
595
800
904
904
805
908
808
909
908
908
939
962
674
968
844
618
901
589
560
578
578
560
583
585
566
584
581
563
593
594
594
593
590
598
600
593
567
582
577
573
569
569
569
566
566
564
562
88
06
67
67
88
86
88
99
98
98
66
88
99
69
69
69
86
66
66
66
66
86
96
66
66
99
66
96
66
66
96
66
88
66
66
69
66
66
66
66
88
67
66
67
99
97
69
69
67
67
67
66
86
67
67
67
67
67
67
67
67
67
67
67
67
67
67
67
67
67
67
67
67
67
67
216
216
216
216
216
215
215
215
214
214
215
215
216
219
216
216
214
213
212
211
210
210
210
210
211
212
212
213
214
215
216
216
216
216
216
217
217
216
217
217
216
215
211
208
205
202
201
200
199
199
198
196
197
197
196
197
200
202
203
203
203
204
205
205
204
202
200
199
198
197
196
195
195
194
193
ppm
14742
14746
14885
14832
14716
14600
14543
14526
14539
14543
14579
14726
14783
14824
14197
13944
13298
12867
12891
12590
12851
12879
12781
12919
13118
13212
13350
13550
13729
13827
13407
13257
13127
12878
12708
12528
12337
12081
11910
11747
11047
10758
10120
10421
10893
11389
11523
11637
11751
11812
11747
11572
11428
11430
11492
11590
11428
11011
10510
10592
10575
10742
10791
9855
0493
9721
9900
10148
10433
10832
10840
10571
10386
10335
10404
10506
ppm
2008.2
20083
2008
20055
20059
20065
20052
20049
2008
20039
2005.2
20088
20063
20046
1985
1964
18988
1871.4
1848
1642.1
1845.4
1851.1
18581
18776
1901.2
19053
19198
1938.5
1956.7
19446
19242
1911
1903.8
18747
1882.3
1837.2
18044
17756
17539
1754.7
1637
1619.5
14832
1553.2
1615.2
1888.3
16995
1897.9
1720.5
1717.4
1714.5
1885.4
1990.8
1964.2
1674.2
1882.5
16799
1622.9
1527.5
15654
15526
15776
18081
14281
1369.1
14168
14526
1463.4
1525.9
1596
15643
1545.1
15199
15055
15194
15342
02
CO2
ppm percent percent
5013 1207 656
5014
5013
5012
5013
5013
5013
5013
5013
5015
5013
5012
5014
5014
5013
5014
5014
5013
5012
5013
5013
5013
5015
5014
5015
5014
5013
5012
5011
5012
5013
5013
5013
5013
5012
5015
5015
5014
5015
5014
5014
5013
5015
5015
5012
5012
5013
5012
5012
5014
5011
5015
5014
5015
5013
5012
5014
5014
5013
5015
5014
5013
5016
5012
5014
5014
5013
5013
5015
5012
5013
5013
5015
5013
5013
5012
1206
1202
1199
1192
1195
1204
1205
1208
12.07
1203
1199
1195
11.98
1153
1143
119
12.25
1236
12.43
1246
12.47
12.43
1236
12.33
12.3
12.27
12.26
12.24
12.12
12
11.94
11 96
11.95
1199
12.02
1199
1206
1217
12.26
12.05
12.04
122
126
13.07
133
13.41
13.4
1337
13.31
133
1332
13.31
13.31
1339
1353
13.67
13.45
131
1318
13.18
1321
13.32
1323
13.29
1343
1391
1397
1374
1378
1389
1392
1395
1393
1393
1394
847
853
656
869
86
652
647
647
851
654
856
8.52
855
8.99
905
868
835
827
618
807
809
817
617
8.23
8.2
825
833
824
841
858
852
8.49
853
649
6.5
8.53
841
8.33
824
845
834
825
785
7.32
7.17
7.03
7.13
7.08
711
713
704
712
7.14
7.05
898
681
706
7.42
73
736
7.32
717
737
724
7.00
693
686
682
68
671
658
958
6.6
659
656
Water
THC balance actual flow rate heat out
ppm
1982
1402
1654
1778
1779
1745
1742
1992
1898
1658
1621
1532
1693
1626
1806
1515
1774
1568
1449
1525
1482
1435
1524
1504
1438
1475
1507
1731
1570
1462
1372
1329
1322
1580
1306
1092
1168
1113
1306
1239
1030
1108
1198
1069
1130
1086
1152
1092
1031
1018
1070
1101
1015
1044
1175
1226
1044
1222
771
789
767
782
772
763
783
785
796
600
615
833
625
793
750
744
793
785
In
33
325
32.5
32
315
31.5
31
309
30.5
30
30
295
29.1
29
265
28.5
28
28
27.5
27
27
285
285
26
26
255
25.5
25
25
245
24.4
24
24
235
235
23
225
225
225
22
22
21.5
21
21
21
205
205
20.5
20
20
19.5
19.5
195
19
19
19
19
185
185
184
18
18
16
17.5
175
17
17
17
17
165
165
165
16.5
16
16
16
67 7599
8.7
67
67
67
67
67
67
97
97
97
67
67
67
6.7
87
87
97
97
97
97
97
97
97
97
97
87
67
67
67
67
67
6.7
67
67
6.7
67
67
6.7
67
67
6.7
9.7
97
9.7
97
67
87
87
97
67
67
6.7
67
87
67
6.7
67
67
6.7
67
67
6.7
67
67
67
67
67
67
67
6.7
67
87
67
67
67
737.8
7544
6938
737.6
7599
7433
743.3
7543
732.2
7543
7598
7763
7598
7928
7818
7707
7597
7817
7596
765.1
765.1
7321
7927
754.1
7706
893.5
7540
746.5
781.6
7616
759.5
792.6
7981
7928
759.4
7949
753.9
775.9
781.5
759.3
803.5
7648
792.3
8086
7758
775.8
7647
753.6
7343
792.3
786.7
7647
797.6
8033
8198
792.2
819.8
803.3
8143
603.2
770.2
808.6
781.2
803.2
784.6
806.7
787.7
8143
7867
814.3
742.5
7548
7977
8067
8032
Dralt
Water meter
Cool water readwia
OVOfl density, b/jal
On 827
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
827
827
827
827
827
827
8.27
827
827
827
8.27
827
627
627
827
8.27
8.26
8.27
828
826
826
628
627
826
8.26
826
828
828
828
8.26
828
826
826
826
828
626
826
826
626
626
826
826
826
8.28
828
8.28
8.28
628
626
8.26
828
826
8.28
8.28
826
826
828
626
6.26
826
826
8.26
828
826
626
626
826
826
626
826
826
828
828
826
826
gpm
66
66
6.6
66
66
66
66
66
66
66
66
66
66
66
66
6.6
66
6.6
66
66
66
66
66
66
66
66
66
6.6
66
66
66
66
66
66
66
66
66
6.6
6.6
66
66
66
8.8
66
66
6.6
66
66
66
66
6.6
86
66
66
66
6.6
66
66
66
66
66
66
66
66
66
66
86
66
66
66
66
66
6.6
6 6
66
66
-------
FURNACE A WITHOUT CATALYST, HISH HEAT REMOVAL RATE
02-Afsr-M
juirw null i wfr* ssupmg lesi 1
« «x*l<» dMion H2Oil H2Ooul I
13988
14028
14088
14148
14208
14268
14328
14388
14446
14508
14568
14628
14688
14748
14608
14888
14928
14988
1504)
19108
15184
15224
152)4
15344
15404
15464
15524
15584
15644
15704
15794
15824
15884
15944
16004
18084
16124
16184
16244
16304
19364
19424
19494
18540
16)00
16660
16720
167BO
16840
16900
16960
17020
17080
17140
17200
17260
17320
17380
17440
17500
17560
17620
17680
17740
17800
17880
17916
17976
18036
18096
18158
18218
18278
1)338
18196
18456
166
166
166
167
167
166
168
167
168
18?
18?
165
163
163
163
162
162
162
181
180
160
160
181
161
160
160
160
190
160
160
160
1(0
190
160
180
160
169
158
198
159
198
159
199
199
159
158
158
158
198
158
158
157
158
157
157
158
157
156
157
157
19?
157
157
157
1*8
195
195
195
154
154
155
155
154
154
154
155
H=y <
80
N
80
80
80
80
80
80
BO
BO
80
80
79
79
79
79
79
79
n
78
79
79
79
78
79
79
79
78
78
79
79
79
78
7)
78
78
78
78
78
78
78
78
78
78
78
78
78
78
78
78
7»
7»
71
77
77
77
77
76
78
78
78
77
78
78
77
77
77
77
77
77
77
77
77
77
77
77
115
115
116
115
115
115
115
115
116
111
11S
115
115
115
115
115
115
115
115
115
115
IIS
119
115
115
115
lie
115
115
115
11)
118
115
11)
115
115
115
115
115
115
115
115
115
114
114
114
115
114
114
114
114
114
115
114
115
114
114
114
114
114
114
114
114
114
114
114
114
114
114
114
114
113
114
114
113
111
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
130
t30
129
130
129
129
129
129
129
129
129
129
128
128
129
128
129
129
129
129
129
129
128
129
128
129
12)
129
129
128
128
128
128
128
126
12)
128
128
128
128
128
128
128
128
128
128
121
128
r»bo> M**r* Movint CONati COoMion
3flg f dcg f
982 87
581 67
5)3 87
565 67
566
570
574
582
5W
579
571
563
595
551
549
948
542
519
537
535
534
513
533
531
530
528
528
525
924
924
S22
521
521
521
519
918
514
513
511
512
910
907
908
909
509
509
508
507
507
509
504
502
500
489
488
485
483
492
491
490
490
489
490
490
4)6
488
485
484
4(3
492
4)1
4)1
479
478
478
476
87
86
67
17
•7
87
87
67
67
67
66
67
87
87
97
97
97
(7
97
97
97
87
67
86
87
87
88
67
89
89
96
88
8)
6)
6)
66
89
M
68
66
68
66
66
68
88
68
68
M
M
88
6)
66
66
86
88
86
88
66
89
89
99
85
85
86
85
85
(5
(9
69
85
89
69
M0f
1)3
193
192
193
193
193
193
194
195
195
193
192
181
190
189
188
181
186
186
188
186
185
189
189
184
184
184
185
1)4
184
1(4
1(4
1(4
1(4
1)3
183
182
1)2
161
181
181
1N
1(0
1(0
1)1
1)1
1)1
1)1
181
1(1
181
181
«1
1(1
190
in
in
180
180
1)0
in
150
181
180
1?9
178
178
177
177
178
178
17)
176
176
176
»76
10624
10775
10693
10457
10902
10992
1054?
10124
94)3
9037
92)1
•798
10270
10595
10465
10307
10303
10343
10490
10596
1062)
1058)
109(3
10911
10457
10449
10376
10295
10229
1023)
10185
10095
99(9
10018
9977
9896
9949
9973
9888
8049
9682
9823
8717
9983
9440
•302
•139
9147
9224
•199
•111
•196
•233
•200
•159
•111
•025
8960
8900
9017
8980
•980
9005
MM2
•216
•241
•172
•208
•298
91)7
94)1
9589
9709
9542
•416
•408
1544.3
15793
1552)
1519
1534.7
15405
1537.4
1474.3
1358.3
1284.2
1137.7
14279
1901.8
1533
1513
1474.4
1478.7
14N.6
1517.9
1533.2
1530.4
1531.1
1524.7
1511 9
15099
1498.5
14875
1472-8
1488.1
1482.1
1494.)
1441.4
1431.3
1436.5
1422,4
1408.2
14142
1414.4
11993
1421-5
1)89.7
13893
1378-3
13807
1317.7
1314,3
1279.1
1292
11042
1298.7
1288.6
1296,5
1285-8
12)1-4
1278-5
1270-2
1257,5
1248.9
1242
125))
1247.9
1245
12513
1260-9
12«2
1287.4
1271-8
1288.2
1303.7
1312,2
1329.3
1151 .9
1366
11314
1J17.9
1318.7
CO low
O2
CO2
pprn rjfircei* e*re«*
5019 13.9 ) 61
9015 13.87 6.62
9015 138 872
9015 13.92 668
5013
5015
5015
5015
5012
5011
5015
5013
5013
5015
5013
5012
9013
9013
9011
9011
SOW
9016
5011
5013
5014
5014
5013
9015
9014
9013
9013
9015
9014
9013
9011
5013
5013
5015
5014
5015
5016
5014
5013
5015
9014
9014
9014
9011
5013
5013
9012
9019
5013
5014
5013
9014
5015
9013
9015
9013
9015
9013
9014
9013
9014
5012
9014
9015
9013
9011
9011
9014
90)3
9014
5012
5012
138
13.74
13.71
13.89
11.63
13.75
13.9
14.05
14.17
1423
1427
1426
1411
1415
1418
14.19
14.17
14.16
14,39
14.37
14.4
14.4
14.41
1437
14.36
1438
14.39
14,39
14.41
14.16
14.38
14.42
1446
1445
1446
14.52
14.57
1481
14.64
1458
1458
14.57
14.54
14.52
1453
1454
14.62
14.64
14-65
1469
14-65
1487
14.72
1476
1474
14.72
1473
14.73
14.73
14.77
1486
149
1491
1492
1494
14.93
14.93
1491
14.91
14.92
14.91
14.91
672
6,76
674
863
8(7
6,74
6,5)
845
6,33
62)
6.23
8.27
(.2
8.1)
9.14
9.15
9.17
8.17
6.19
6.18
6.17
)t)
6.16
6.18
6.2
(.1)
6.17
9.16
9.14
9.19
919
6.12
607
6.07
6,07
8.01
5.96
584
9.91
9,»7
598
5.M
8.05
60?
6,06
>08
5,98
9,0)
595
5.84
585
5.81
5.89
5.86
589
5,89
5.8)
588
588
584
9.78
9.71
586
9.88
9.65
5.67
5.67
5.97
5.68
568
5.7
5(1
WMw
THC batance tdyalfl9wimE« teats**
ppfn
750
757
756
756
732
715
711
675
642
640
690
729
749
740
728
710
694
701
713
719
729
711
795
793
761
764
785
749
724
718
723
704
680
672
677
680
684
889
700
689
9)5
894
875
643
616
610
607
592
570
564
595
531
513
511
503
4)7
470
474
4)0
469
459
48?
488
482
469
334
259
248
242
242
247
293
262
268
271
268
t»
1)
1S.S
15.5
15.5
15
15
15
15
14.9
145
14.5
145
14
14
14
14
11.5
11.6
11.5
115
11,1
13
11
13
12,5
12,5
12.5
12
12
12
12
12
11.5
11.5
11.5
11.5
11
11
11
11
10.5
105
109
10.9
10
10,4
10
10
10
10
10
97
95
95
9.5
9,5
9,3
8.6
8.5
8.5
85
85
85
85
6
8
(
7.9
7.7
7.5
7.5
jpm Bh^ntervit
6.7 712.2
6.7 717.7
6.7 803.2
6.7 803.2
67
8.7
8.7
6?
87
87
8.7
8.7
8-7
87
6.7
8.7
8.7
8.7
67
87
67
6.7
6.7
6.7
8.7
6.7
6.7
8.7
6.7
6.7
6.7
8.7
67
8.7
8.7
8.7
6.7
6.7
9.7
8.7
87
9.7
87
6.7
8.7
8,7
6.7
6.7
6.7
6.7
87
8.7
67
6.7
6.7
6.7
9.7
6,7
6,7
8.7
6,7
6,7
8.7
8.7
6.7
8.7
6.7
87
8.7
6.7
8.7
8.7
6.7
6.7
6.7
6.7
(383
(08.7
8308
825.3
BOS 7
•032
803.3
(30.8
797.8
808.8
8196
792.3
8308
808.8
)14.3
775.5
019.0
775.7
(08.8
803.3
(14.3
786.7
797.8
11 8.9
(03.3
731.6
770.J
792.3
731.6
786.6
764.7
797.9
7482
7482
711.1
770.1
759.1
7196
8031
8035
8090
775.9
7)14
809.0
8)9.0
781.5
825.8
7594
814.9
748,1
7)7.0
814,9
7)1,5
•14.9
803.5
798.0
798.1
794.8
801.6
781.5
795.1
770.5
787.0
787.1
781.5
781.5
798.1
781.5
7*9.0
820.1
809.2
Draft
V»«t«m«t»c
Coo) Witer reaoxig
OrJOlt dmly, fc'gal
Off 0.28
off >.ae
Off 826
Off 826
Off
Off
Off
Off
Off
Off
Off
Off
on
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
OB
OB
OB
OB
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
OH
Off
Off
Off
Off
Off
Off
Off
Off
on
Off
Off
Off
Off
Off
Off
Off
828
(.26
(.26
a.26
8,26
a 25
8.2)
a 28
8.26
8.28
8.26
826
826
8.21!
8.26
(.28
(.29
(.29
828
828
828
(28
(.28
(.28
(.28
(.26
(.26
8,26
8,28
8,26
826
826
8,28
826
8,28
(.26
826
0.28
828
828
828
828
8.29
8.26
820
8.29
(.26
(.26
(28
(.28
(.28
(.26
(26
8.26
826
8.2)
(.26
(.26
(.26
(.26
(.28
(.26
(.26
(26
8.26
6.2)
8,2)
(.2)
8.26
(47
(47
gpm
6.)
86
6.6
66
68
8.6
6.6
66
8.6
6,6
6,6
68
66
66
68
66
66
66
6,6
6,6
68
66
6.6
66
6.6
6.6
6.6
6.6
66
6,6
6.6
6,8
6.)
6)
6,6
68
8,6
66
6,6
6.6
8.6
6.6
6.8
6,9
6,6
6,6
66
6.6
6.6
6.6
9.6
96
66
86
66
69
6.9
6.6
66
6.8
6-6
6.6
6-8
6-6
9-6
9-6
9.9
6.6
6,6
66
6,6
6.6
86
6 6
6.8
56
-------
FURNACE A WITHOUT CATALYST. HIGH MEAT REMOVAL RATE
02-Apr-66
15-Jun-tS Run TDD-2A Scoping t«« 1
lime Onkeit tHution H2O«i H2QQUI «r«im« »
sec deg F
-------
FURNACE A WITHOUT CATAIYST, HIGH HEAT REMCVAl RATE "neo on
15-Jun-95 KunTDD-2* Scoping test 1 ,„,„,,
time stack exit dlutlon H2O in H2O out Are box amMera stove e*K
sec deg F deg F deg F deg F deg F deg F deg F
23064 142 73 108 122 386 84 1SB
23124
23184
23244
23304
23364
23420
23480
23540
23800
23660
23720
23780
21840
23900
23960
24020
24080
24140
24200
24260
24320
24380
24440
24500
24560
24620
24680
24740
24798
24856
24916
24976
25036
O 25086
, 25166
-J 25216
25276
25336
25396
25458
25516
25578
25836
average
25248
7.01333333
420.8000
142
142
142
142
142
142
143
143
143
144
143
143
142
141
140
139
138
118
139
142
142
141
133
138
137
137
137
137
137
137
136
135
13S
115
135
134
133
133
133
133
134
134
183
73
73
71
73
74
75
75
76
75
74
74
73
71
73
73
72
72
72
72
72
72
72
71
71
72
73
74
74
73
73
72
72
72
71
72
71
71
71
71
71
72
73
78
108
108
108
108
109
109
108
108
108
108
108
108
108
107
107
109
10?
10?
107
107
107
107
107
107
107
107
108
107
1117
106
109
108
108
108
109
105
105
105
105
108
109
109
lit
122
122
12J
122
122
122
121
122
12J
122
121
121
121
121
12t
121
120
120
120
120
120
120
120
120
120
120
119
120
119
119
119
KB
119
118
119
119
119
118
118
118
118
118
124
384
383
382
381
380
379
371
37?
378
374
372
370
398
387
387
160
390
147
384
400
411
194
170
15?
147
341
338
338
134
333
331
329
328
327
326
325
324
323
322
321
320
319
451
63
63
63
64
64
84
84
84
65
95
89
89
8t
84
84
64
84
64
84
94
63
83
63
63
63
63
M
84
84
84
84
84
85
84
84
63
6]
83
81
83
63
64
88
158
19*
158
157
156
15?
19*
197
157
156
199
196
156
155
155
154
tea
190
152
158
198
191
198
194
152
150
148
148
14?
147
147
146
148
145
144
144
144
143
143
142
142
142
183
CONgtt COdHutum CO low O2 CO2
ppm ppm ppm percent percent
6486 7797 5015 16.11 455
8488
8421
8358
6289
6208
81 f3
8470
84S8
6331
6218
6108
5889
5904
5M1
5782
5713
$873
5857
5840
5008
4484
4504
4822
$119
5184
5172
5155
5103
5050
4819
4868
4887
4891
4838
4622
4X8
4828
4777
4738
4 859
4808
4582
11486
7714
761.1
748,2
7346
714.8
708
7684
758$
736.2
721.5
700
871.2
888.1
6$4.1
637.7
818.3
880.1
8758
615.1
529.8
411.6
421,2
475.6
5308
827.2
532.2
528.2
S1J.8
5084
502.4
4868
480.8
4M.8
4782
475.6
476.1
475.8
489.2
457.6
440.8
411.5
410.2
9014
9011
9013
$014
$015
9015
901$
5015
$016
9016
$014
9014
5014
SOU
5015
9013
9014
5015
SOI 2
4986
4484
4470
4798
9013
SOU
$014
5011
5013
$011
4984
4943
490?
4880
4819
4806
4789
4809
4798
4712
4697
458$
4586
16.14
18.18
16.19
1621
16.23
16.24
16.19
16.16
1918
19.23
16.31
16.38
18.4
16.44
16.47
16,48
16.77
16.98
1681
16,51
19.18
18.32
18.85
16.87
16.9$
17.02
17.03
17.04
I7.M
17.1
17.14
17,17
17,17
17,18
17.21
17.24
17.24
17.28
17.24
17.28
17.28
17.3
U.27
4.53
448
4.47
446
444
4.43
4,48
4.4?
4.45
4.41
434
4.27
426
4.23
4.21
4.18
392
378
388
4.27
4.99
4.41
406
3.8$
3.76
1.71
1.99
38?
18$
381
3.98
1.98
196
354
1.54
3.51
1.51
1.$
351
3,48
3,4?
3.46
6.38
THC balance actual flow rate fieatout
ppm •» gpm Btuflntecval
112 2,5 8-7 7550
111
108
108
106
105
100
98
99
98
95
95
91
92
88
87
90
117
129
118
101
95
100
115
117
108
103
89
98
M
91
B8
89
79
T7
78
76
74
88
88
86
64
63
1057,06
2 8-7
2 6-7
2 6.7
2 6.7
2 6.7
2 6.7
1.5 8.7
1.5 5.7
1 .5 6.7
1.5 67
1.5 6.7
1.5 87
1.5 6.7
1.6 6.7
1.5 6.7
1.5 6.7
1.5 8.7
6.7
67
6.7
8.7
87
87
8.7
1 87
1 67
0.5 6.7
O.S 6.7
0.5 6.7
0.5 6.7
0.5 67
0,5 6.7
0.5 6.7
0.5 6.7
0.5 8.7
0.5 67
0.5 6.7
0.5 6.7
O.S 6.7
0.5 8.7
0.3 67
0 67
186
Total Btu out -
Total Btu « -
Efficiency -
Ave. water -
fjurwvte «
Wood moisture
768.0
760$
771 5
755.0
6685
6832
883.2
6832
6942
7329
7385
7330
7SB5
7386
7275
738.5
733.1
718.6
7166
7387
727.6
716.6
738.7
722.1
711.1
6945
6448
8278
872.5
7056
7112
7057
634.6
7188
700.2
722.3
727.8
722.4
694.8
688.2
661 6
8506
7185
301,944
516,041
98.80%
tiUafwr iralAr
Draft Cool waiter reading
On/Off density, Ib/gail gpm
Off 8.27 88
Off
Of!
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Of!
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
OB
OB
Off
OB
OB
Off
Off
Off
Off
Off
Off
Off
OB
on
on
on
Off
Off
Off
. Btumr out «
.Blumrii-
8.27
8.27
8.27
8.27
8.27
8.27
8-27
827
827
8.27
8.27
8.27
827
828
8.28
828
828
828
8.28
626
8.28
8.28
828
8.28
8.28
828
•.27
828
8.28
828
828
828
8.28
8.28
828
8.28
828
821
828
828
828
828
8.2?
43,338
73,580
98
6.8
6.6
6.6
86
t.a
«8
6.6
6.6
6.6
8.6
6.6
6-6
99
6.8
8.8
86
86
6.8
66
8.8
98
6.6
6.6
66
86
66
8.8
6.6
6.6
66
66
86
86
9.6
9.6
66
86
6.6
66
66
66
6.66 gpm
4.14
29.00%
drykgyhr
-------
FURNACE A WITHOUT CATALYST. HIGH HEAT REMOVAl RATE
02-Apr-M
19-.lun.95
Run TTD-2B Scoping test 2 .
time flick ext dilution H2O In H2O out fire box imblent stove ftxt CO Mgti CO dBution
tec ifejF d«gF dejF degF dejF dtjF
-------
FURNACE A WITHOUT CATALYST. HIGH HEAT REKKJVAl RATE
02-Apr-«
1»-Jun-95 R»TTD-2B Sc^mf l« 1
time Mack cut (Stfion H2OH H2Oout «r« bo» taunt a«««j« CONifi COiMtoi
SM eUgF deaf dejF degF 4tg f (hjF d^F pom ppm
10260 tM 80 144 158 73« 67 20? 55JO 19684
10320 IBB 81 144 158 737 87 20? 5582 1(722
10360 193 83 144 159 748 87 208 5623 1898.5
10440
10500
10560
10620
10680
10740
10600
10660
10920
10980
11036
11096
11156
11216
11276
11338
11398
11456
11516
11576
11636
11696
11756
11816
11876
11936
11996
12058
12116
12176
12238
O 12296
12358
\O 12412
12472
12532
12592
12852
12712
12772
12832
12892
12952
13012
13072
13132
13192
13252
13312
13372
13432
IMB;
13552
13612
13672
13732
13786
13S46
13908
13968
14026
14086
14148
14208
14266
14326
14368
14448
14508
14568
14628
14888
14748
lav
198
198
196
185
195
194
1S4
195
ifie
U7
195
195
195
196
1M
200
200
200
tS9
198
196
195
195
1B7
199
1(9
200
200
200
200
200
199
199
196
IBS
116
186
199
200
201
200
200
200
200
201
203
202
200
200
201
203
204
206
205
207
207
207
208
20t
201
209
209
207
206
207
207
208
208
208
20?
205
204
HJ
83
83
61
SO
79
78
78
78
79
80
80
90
80
80
M
M
79
80
80
•1
82
83
83
82
81
80
7»
78
79
78
80
81
82
83
63
•4
83
91
80
80
78
78
78
78
78
81
82
83
84
n
81
83
82
81
M
80
80
80
79
79
60
81
82
82
82
82
83
81
80
BO
78
78
144
144
145
145
144
144
144
144
144
144
145
144
145
145
14$
(45
145
145
145
144
145
145
146
149
146
145
145
145
145
14$
146
145
146
146
148
147
147
14?
147
148
148
14t
148
146
146
148
147
14?
147
148
148
148
141
141
147
147
14?
147
147
147
147
148
141
148
149
148
149
149
148
148
148
149
148
159
153
159
160
160
160
160
180
180
160
160
160
160
180
160
160
1(0
160
181
161
160
161
181
181
1(1
161
161
161
161
161
161
161
161
161
161
162
182
182
t82
182
182
162
162
162
162
162
163
163
163
163
183
163
183
183
163
164
163
164
1M
164
164
164
164
1«4
164
164
165
165
165
186
165
165
185
744
732
728
721
719
71«
715
714
717
718
7t»
715
715
718
?ie
711
897
666
611
878
873
673
871
870
•es
669
672
674
873
(73
871
870
668
665
880
65$
653
•50
«47
649
649
650
649
848
846
646
649
£50
85 1
8S3
850
849
849
846
650
651
652
652
854
•59
•52
«49
641
641
649
649
648
849
650
651
650
641
644
87
87
87
06
M
n
•7
•7
(7
67
67
67
67
87
87
88
M
8?
87
87
87
«7
07
67
87
68
87
87
(7
67
<7
67
67
87
m
67
61
M
M
68
86
88
68
66
86
67
§7
66
•7
68
n
66
69
66
88
68
86
66
M
66
87
67
67
66
86
66
66
m
68
68
m
66
m
206
206
208
205
204
20S
204
204
205
208
208
208
208
210
210
210
211
211
211
210
210
209
209
209
209
209
210
210
210
210
211
211
212
212
213
213
211
213
213
213
212
212
211
211
211
211
212
212
213
214
215
215
216
217
217
217
217
211
218
211
219
220
219
220
221
222
221
221
221
221
219
218
21?
5587
5314
5013
5042'
5090
5062
S241
5852
5823
5280
5840
5599
5505
5880
5461
5721
5442
5774
5754
5745
5941
6112
6148
6250
6014
5721
S786
5656
9728
5122
4748
4928
4891
4907
4781
464?
4569
4272
4167
4252
4244
4195
4118
3890
3772
3845
3931
4114
4313
4439
4N9
4130
4287
4533
4545
4500
4472
4194
4553
4679
4588
4565
4959
4529
4855
4740
4608
4978
4801
4258
4252
3886
3682
2005.9
1869.1
18258
1908.1
1893.6
1(15.9
1924.2
19434
1995.1
19688
19795
20031
2002.8
2005
2008.2
2006
2005.7
2005.2
2006.8
20063
2005.2
2005.4
2006.3
2006.3
2008.3
20055
2005
2005.7
2004.7
2003.6
1872.5
19565
1930.7
1918
1682
1(56.1
1651.7
1(42.3
1626-2
1786.7
1770.7
1741.5
18964
16904
18766
16876
1656.4
1684.3
1743.5
18174
1621.5
1626.6
1659
1881 7
18862
19108
19181
1915
1911.2
19051
1910
1906.2
1906.3
1921.8
19393
19479
1959.1
1999.3
1988.)
19838
1848.S
1724.4
1663.9
CO tow
ppm
5012
5012
5013
5012
son
4888
S008
5014
5009
9014
5011
5012
5014
5012
5014
5012
5014
5013
5013
5012
5012
5014
5013
5012
5012
5013
5013
5013
5014
5011
5013
5009
5012
4761
4960
4910
4835
4(14
4689
4603
4151
4152
4262
4281
4235
4164
3937
3780
3662
1949
4134
42M
4472
4436
4191
4315
4578
4568
4537
4520
4189
4593
4748
4614
4605
4690
4561
4696
4781
4823
4985
48*6
4269
4279
3889
3689
O2 CO2
ptfwrt perctnt
17.35 3.76
17.36 3.71
17.43 3.87
1749
1758
1772
1771
17.7
17.6
1789
17.51
1759
17.85
17.39
1744
1756
17.49
17.62
1745
1752
1755
17.56
17.7
1761
17.56
1761
1757
1761
1773
1768
1771
17.53
17.66
1792
17.89
1768
1762
17.59
17.65
17.71
17.84
17.85
17.77
17.66
1785
17.65
17.8
17.87
17.84
17.68
17.44
17 41
17.46
17.46
17.62
17,67
17.5
17.5
17.59
17.61
17.85
17.58
17.4
1?,4(
17.5
17.45
1758
17.55
1748
1757
17.55
17.45
17.7
17.7
17.8
17.93
361
349
3.34
3.31
3.31
3.24
33J
3.1
344
3.38
3.61
3.56
3.45
359
3.38
3.54
344
341
3.42
3,29
3.18
3.42
339
1.41
336
1.25
S.»
328
3.47
3.33
3,06
3.31
333
34
3.42
3.36
3.31
l.H
3.0S
3.2
33
1.32
3.32
3.17
3.04
3.17
3.34
3.54
3.S3
3.48
3.47
3.28
3.27
3.41
3.42
3.35
3.35
111
343
3.98
349
349
3.54
3.36
344
346
3.39
3.39
3.49
3.23
3.22
3.11
3
Witt!
THC Inline* actual flow rate heats*
ppm fe* gpm BTU
2428 599 6.7 8464
2486 505 67 929.9
2502 59 87 aoa.o
2452
2368
2365
2368
2446
2453
2514
2681
2658
2855
2726
2708
2712
2712
2641
2585
2594
2855
2729
2738
2762
2778
2781
2725
2591
2571
2477
2388
2268
2163
2089
2008
1934
1678
1(49
1(37
1(36
1644
1614
1774
1772
1742
1755
1741
1724
1671
1652
1661
1759
1746
1755
1796
1825
1656
1693
1908
1898
1938
1964
19(6
1937
1950
2010
2005
2021
2076
2265
2192
186?
1842
1737
1664
1570
565
564
56
57.5
57.5
5?
57
S6.S
56.5
56
55.5
55.3
55
54.5
54
54
I3.S
SM
§3
53
52.8
52
51.5
51
51
90.5
505
50
50
50
49.5
48
485
48.S
48
47.5
47.5
4?
4?
46.5
46.1
48
46
45.5
45.S
45
44.i
445
44
435
43
43
42.S
42.5
42
42
415
41.5
41
408
40-5
40
395
38.5
39
365
38.4
38
36.7
37J
37.4
37
3?
6.7
67
67
67
67
8?
6-7
6.7
6.7
67
67
6.7
6.7
6.7
6.7
6.7
6,7
67
6.7
67
87
67
8.7
6.7
67
6.7
67
87
8.7
8.7
67
67
67
6,7
6.7
67
67
6.7
6.7
6.7
8.7
6.6
66
66
66
66
66
66
6.8
6.6
6.8
6.6
6.6
66
68
68
66
6.6
66
6.6
6.6
86
66
66
66
66
6.6
66
6.0
6.6
6.6
6.7
6.7
608.0
607.8
791.5
6243
640.7
868.1
H4.5
851.7
(73.6
779.6
846.1
857.1
851,5
810,6
(35,1
051,8
857.0
6570
6789
•84.4
•35.1
651.4
829.5
8349
841.8
851.3
867.8
867,1
•733
876.7
851.3
656,8
779.2
840.3
823.8
623.8
•23.7
•23.7
140.2
•566
873.0
850.4
850.4
877,4
666.6
181.2
155,7
8386
839.4
•12.4
817.7
•12.3
844.7
8393
880.9
818.8
866.3
877.0
•82.4
•77.1
8878
866.1
871.4
666.0
8498
860.6
860.5
865.9
869.9
8875
•7«.6
•10.6
810,5
¥Val«fmet»r
Draft Cool water readnfl
On/Of density, bfgal gpm
On B.20 6.6
On 6.20 6.6
On fl 20 66
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
Cm
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
8.20
(.29
8.20
8.20
8.20
8 20
8.20
8.20
6.20
8 20
(.20
(.20
8.20
8.20
8.20
8 20
8.20
8,20
8.20
8,20
819
8.19
8.19
8.19
61*
6,19
6.19
6.20
6,19
(.19
(.19
8.19
8 19
619
6 19
618
8.19
(.19
(.19
(,19
( 19
(19
• 19
6.19
6 19
6.11
8 19
8,19
8 18
8.19
8.18
8.19
818
819
• 19
• 19
•,19
1,19
8.18
8.18
8.19
8.19
1,18
819
819
619
8,19
fl 19
8,19
8,19
• 19
8.19
6.18
6.6
6.6
68
8.6
6.6
8.6
6.6
6.6
6.8
6.6
6.6
68
8.6
86
6-6
6,6
6,6
6,6
6,8
6.6
6.6
6,6
6.6
66
66
6,6
6,6
98
6.6
6.6
6.6
8.6
6.6
6.6
66
6.6
6.6
6.6
6.6
6.6
6.6
6,5
6.5
6.5
6.5
6.5
6.5
65
8.5
65
8.5
6.5
8.5
6.5
6.5
6.5
65
65
6.5
8,5
65
85
6,5
6,5
65
65
6.5
65
69
6.5
65
66
• 6
-------
FURNACE A WITHOUT CATAIYST, HIGH HEAT KMOVAt RATE
02-Apr-M
o
jun-aa KMR f f U-/D scopng le* 2
* start** dtotion H2Oin H2OoU *»!>!» tmbiM «
-------
FURNACE A WITHOUT CATALYST. HIGH HEAT REMOVAL RATE
02-Apr-M
19-Jun-95
Run TTD-2B Scoping lest 2
ttne stack exit dilution H2Oki H2O out firebox ambient stove ex*
sec deg F deg F deg F deg F deg F deg F deg F
19352 179 75 149 165 614 87 191
19412 179 76 150 165 911 97 191
19472
19532
19592
19952
19712
19772
19832
19892
19952
20012
20072
20132
20192
20252
20312
20372
20432
20492
20552
20812
20868
20728
20788
20848
20908
20968
21028
21088
21148
21208
21268
. 21328
J 21388
j 21448
., 21508
21568
21628
21688
21748
21808
21868
21928
21988
22044
22104
22194
22224
22284
22344
22404
22484
22524
22584
22844
22704
22784
22824
22884
22944
23004
23064
23124
23164
23244
23304
23364
23420
23480
23540
23600
23690
23720
23780
23840
17B
177
176
175
175
175
174
175
174
173
172
172
171
171
171
172
173
173
175
176
177
176
174
173
172
172
172
172
172
172
172
172
173
174
174
175
176
176
178
179
179
175
175
175
175
175
173
172
172
172
172
173
173
173
173
173
172
171
171
171
171
170
171
171
171
171
171
171
171
171
171
199
197
195
77
78
79
79
80
80
79
78
77
78
79
75
74
74
75
77
76
78
76
79
79
78
78
78
77
77
75
75
74
74
75
78
79
79
77
77
77
77
77
77
79
75
74
75
79
79
77
78
79
79
77
76
75
75
74
74
75
75
76
76
77
76
77
77
77
77
76
75
75
75
75
76
77
76
150
150
150
150
150
150
150
150
150
150
150
149
149
149
149
149
149
149
149
149
149
149
149
149
149
149
149
151
152
151
152
152
152
152
152
152
152
152
152
152
152
152
152
152
152
152
152
152
153
153
153
153
153
152
153
153
153
153
153
153
153
153
153
153
154
153
153
153
153
153
153
153
154
154
165
165
165
165
165
165
165
165
195
195
195
165
195
195
164
164
164
164
164
164
164
164
164
164
164
164
194
194
194
194
194
194
194
194
193
193
194
164
164
164
164
164
164
164
164
164
164
164
194
194
195
195
195
195
165
165
165
165
165
165
165
165
165
165
165
165
166
165
165
196
165
196
196
195
906
905
904
904
904
904
904
905
605
906
607
608
609
611
614
617
618
918
920
920
924
823
917
914
912
612
613
613
614
616
616
617
621
621
623
625
625
629
633
638
638
638
637
637
637
639
638
632
628
627
627
626
624
623
622
621
618
616
616
615
614
613
612
610
608
909
905
904
905
603
598
588
581
577
87
67
68
68
68
88
68
69
69
69
68
98
68
67
67
87
87
87
67
67
88
88
68
68
68
68
88
88
68
68
88
88
88
88
88
88
88
88
88
89
88
89
88
68
88
88
88
88
88
98
98
68
88
88
88
68
88
88
87
87
88
98
88
88
68
88
88
68
68
68
68
68
67
68
191
189
188
167
188
166
186
186
186
IBS
185
184
183
183
182
183
184
184
184
185
187
166
185
184
184
184
184
183
183
184
184
183
184
184
185
185
186
188
188
187
187
187
187
187
187
188
185
184
184
184
184
184
184
184
184
184
184
183
183
183
183
183
182
183
183
183
183
183
183
182
183
182
180
178
CO high CO dUton CO low
2938 1214 2928
2824 11981 2826
3162
3743
3878
4004
4020
3947
4281
4378
4439
4753
4818
4582
4492
4415
4211
4159
4224
4032
4142
4020
4032
3882
3552
3528
3479
3422
3312
3215
3251
3381
3259
3141
2974
2856
2950
4049
10449
11243
11580
11963
11947
12038
12260
12333
12388
12467
12297
12280
12191
12199
11776
11401
11438
11414
11523
11560
11507
11552
11654
11890
11784
11873
12089
12272
12341
12463
12207
11967
11918
11694
11190
9603
9473
9757
13577
15736
1844
17205
1754.1
1749.5
17793
18385
1825
18861
1697
1683.5
1875
18599
18577
17426
17181
1654
18981
19548
1702
1871.5
15562
14963
14263
1407.7
13874
1388
13875
13534
13057
13226
12396
1165
11416
11424
11331
10985
1114.1
1187
11738
11823
12121
12285
12347
1250
12253
1220.1
1202
1215.8
1184.6
11123
11092
11087
1122.6
11269
11204
11177
11388
11343
11426
1153
1192.9
12023
1212.7
1229
1202.6
1167.5
11654
1146
1111.2
8678
8387
875
3201
3780
3915
4033
4029
3987
4328
4412
4482
4793
4880
4622
4541
4455
4250
4198
4269
4063
4177
4069
4060
3916
3588
3545
3508
3447
3324
3240
3283
3365
3261
3177
2979
2851
2934
3459
5011
5010
5012
5013
5011
5010
5012
5011
5011
5011
5013
5011
5013
5011
5010
5011
5011
5011
5013
5014
5013
5011
5013
5012
5010
5011
5012
5013
5012
5011
5013
5012
5011
5012
5013
5014
5013
5014
O2 CO2
percent percent
18.23 252
163 247
1837
1834
18.44
185
1854
18.54
185
1849
1845
1839
18.38
1842
1845
1846
1851
1847
184
1845
1851
18.47
18.59
18.7
18.8
1871
18.63
1884
18.71
18.79
1878
1865
1865
18.74
18.76
1898
1857
1787
1134
977
967
9.52
946
95
954
953
9.6
965
957
97
964
994
9.93
9.9
9.9
9.97
1005
10.15
1027
1034
1039
1038
10.38
1037
10.38
1033
1038
1052
1059
1098
1088
1071
1076
11 1
1148
11.75
239
238
2.3
224
221
219
223
225
228
234
233
226
222
22
221
238
2.47
25
246
2.54
246
235
225
2.3
238
237
232
227
232
244
248
239
237
245
2.54
324
919
10.45
1054
1061
1062
1058
1048
1049
10.4
1035
1045
1032
1022
1014
1016
1017
1018
1017
1013
1007
999
993
992
994
998
995
993
997
992
983
978
967
984
961
954
92
8.8
855
Ulfotu
THC balance actual flow rate heat out
ppm tot gpm BTU
1267 21.5 87 8503
1321 21 07 B3Q. 3
1542
1653
1778
1829
1804
1951
2016
1981
2123
2146
2047
1976
1901
1829
1733
1747
1622
1681
1624
1654
1633
1563
1524
1411
1373
1308
1251
1205
1165
1104
1095
1027
968
925
938
922
868
884
913
874
878
900
900
884
892
876
865
894
927
902
870
871
870
871
870
892
902
930
937
944
989
979
999
1011
1028
1037
1034
1005
988
942
762
768
793
766
21
205
20.5
20
20
20
195
195
195
195
19.5
19
19
19
19
18.5
185
18
18
178
175
175
175
17
17
17
17
17
17
165
16.5
165
16
16
159
224
155
155
15.1
15
15
15
15
15
15
145
14.5
14
14
14
137
135
135
135
135
13.5
13
13
13
12.5
125
125
12.5
12
12
12
12
12
12
12
115
115
114
11
8.7
67
87
97
97
9.7
97
9.7
97
97
97
97
97
97
97
9.7
97
97
97
9.7
97
97
97
97
97
97
97
97
9.7
97
97
97
97
97
97
97
97
97
97
9.7
97
97
97
97
9.7
97
97
97
97
97
97
97
97
97
9.7
6.7
67
67
67
67
6.7
6.7
67
67
6.7
6.7
6.7
67
6.7
6.7
67
67
8.7
87
8229
8174
828.4
8229
8174
7956
806.5
801 1
7956
8284
8394
850.3
8613
8450
855.9
812.2
8170
8013
7958
7632
7904
7795
7904
7904
7904
8123
7904
8974
8482
6700
6208
6154
6427
6263
6264
6154
6318
620.8
620.8
8426
631 8
8427
610.0
9481
8945
9481
6371
8429
9098
831 6
6425
9534
948.0
6753
8643
8843
6752
6370
9697
958.8
8479
6697
636.9
6424
6389
6148
675.1
6424
6842
6880
6697
9642
942.3
9314
UUaftBr m*»*r
Draft Cool water reading
On/Or7 density, b/gal gpm
On 818 66
On a 1fl 89
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
818
818
818
818
818
818
818
818
818
818
818
818
BIB
8.18
819
8.18
8.18
8.18
8.18
8 18
818
618
6.18
8.18
6.18
8.19
6.18
818
818
818
818
818
818
818
818
818
818
618
818
818
818
818
818
818
6.18
6.18
818
8 IB
817
818
818
818
81B
818
818
818
818
817
818
817
817
817
817
817
817
817
817
817
817
817
817
817
8.17
817
69
66
66
66
66
66
66
6.6
66
66
66
66
66
6.6
66
66
66
6.6
6 6
6.8
66
6.9
6.6
9.9
6.6
6.6
86
66
66
66
66
66
6.6
66
66
66
66
66
66
66
6.6
66
66
66
6.6
66
68
6.6
6.6
6.6
6.6
66
68
66
66
66
66
66
66
99
99
99
99
99
66
6.6
6.6
6.6
6.6
66
66
6.6
6.6
66
-------
FURNACE A WITHOUT CATALYST, HIGH HEAT REMOVAL RATE
02-Apr-96
1 9 JUT. M Run TTD-2B Scoping IM 2
limt MKkddt (Hulran H2Olti H2OOU flribia imbtofl xove ert
sts dejF itgf dejf itegF *jF dejf t*af
23900 155 78 154 166 574 M 178
23990 164 Tt 154 IM 569 68 175
to
i*u^u
24080
24140
24200
24260
24320
24380
24440
24500
24560
24620
24600
24740
24706
24656
24916
24976
2S036
25096
25156
2S216
2S276
25336
253B6
25458
25516
25576
25630
28698
25756
25816
25B76
25936
25996
26O56
2611«
26172
26232
212)2
2*352
26412
28472
28532
265(2
26852
26712
29772
26832
25892
25952
27012
27072
27132
27192
27252
27312
27372
27412
27492
27548
27001
27061
27728
27780
27046
27B08
27W
21028
21088
28146
28206
21288
28328
28300
1Q3
163
162
162
162
162
162
160
160
160
160
190
100
160
159
160
160
160
160
160
160
150
wo
1S7
157
IS?
ISO
157
15*
156
15»
150
157
157
157
196
157
157
1S7
157
157
157
157
157
158
157
157
157
157
156
155
158
156
196
1S7
167
157
156
187
157
157
1ST
1H
159
IM
160
160
161
161
in
163
163
163
163
n
77
75
75
74
73
73
73
74
75
76
76
76
78
78
76
75
74
73
73
73
74
74
75
77
77
76
76
7S
74
73
72
72
73
74
75
75
75
7S
75
76
75
75
75
73
73
73
73
74
75
76
77
77
76
75
74
73
72
7J
74
75
76
77
77
70
70
7?
77
77
76
75
73
73
73
154
154
1S4
154
153
153
153
154
154
154
154
154
154
154
153
154
153
153
183
183
153
183
153
153
153
153
183
153
153
1S3
153
153
192
153
153
153
153
153
183
153
153
153
182
182
152
1S2
152
152
152
182
152
152
152
152
1S2
152
152
152
151
152
152
152
182
182
1S2
152
152
152
152
152
151
151
151
151
165
166
166
in
166
166
168
166
165
166
165
168
165
166
165
165
166
168
168
165
168
165
165
165
165
165
165
165
165
165
105
165
185
185
165
165
165
165
164
184
164
165
164
164
164
164
164
164
164
164
164
164
164
164
164
164
163
164
164
164
163
163
163
163
163
163
163
164
163
163
163
183
163
163
565
562
562
562
559
558
557
S58
558
553
552
551
550
548
547
548
843
541
540
536
531
530
528
827
525
525
525
524
525
525
525
524
524
523
523
526
527
828
526
525
525
524
822
520
510
510
517
516
516
515
513
511
501
508
508
505
505
505
505
506
500
500
510
511
511
511
512
513
513
514
513
514
514
514
n
8*
88
8*
90
88
88
88
88
88
88
80
81
88
61
M
68
60
66
M
M
88
81
87
87
81
68
81
8*
06
68
67
87
67
87
87
87
67
67
88
8*
(0
88
88
88
88
87
6T
87
87
87
87
87
67
88
88
87
67
67
67
67
87
87
87
87
80
68
88
88
68
68
a*
67
07
175
174
174
174
174
173
173
172
172
171
170
170
170
170
171
171
171
171
171
170
170
170
170
in
168
188
188
188
188
188
169
188
190
187
187
167
197
167
187
167
167
167
187
167
187
187
187
167
167
166
166
186
186
168
186
167
167
16?
197
188
167
167
187
187
180
161
170
170
171
171
172
172
172
172
CO high COdkOcn CO k)W O2 CO2
ppro ppm pom percent partert
9880 091.8 5012 11.91 134
•Ml «01.5 5012 1202 8,26
10002
10814
10030
9823
9733'
9705
9864
9644
9976
9488
9314
9200
9127
9028
8988
8952
8968
•844
1844
9233
9932
10091
10184
10193
102M
10234
10205
10180
10138
10138
10075
10107
10002
9548
9448
9403
0383
•314
•241
1151
81 M
900*
•976
•931
•996
1021
BS93
8823
H27
•903
8818
9025
9257
9334
•285
•318
•383
9302
9509
•163
8963
8M3
mo
•980
1964
1919
•875
IW9
•919
8M4
8870
1813
•670
8686
905.*
910.1
111.3
891
8695
•701
884.6
•918
863
8407
•21.9
810.1
791
7814
7804
7703
772«
771.8
789
7136
698.9
933.9
9351
9377
9398
945.6
939.8
•403
•27.9
9287
9225
925.1
931
859.4
•411
634.3
626.7
1263
•125
N3.5
7t3.6
714.2
779
770.7
76*,1
786,3
782.4
774.3
77J.9
7686
7594
775.4
806.3
•281
621.5
819
823.6
821
8488
•21.6
774.1
779.8
778.9
780.4
783.5
771,8
7622
765.8
7744
775.7
7721
7606
7725
771.5
5013
5011
5013
5012
5012
5012
5011
5014
5011
5012
5013
5015
5011
5013
5014
5015
5013
5011
501 3
5013
5012
4012
5014
5013
$014
5014
5013
8013
5012
5011
5011
5015
5014
5013
5011
5012
5011
5012
5013
5013
5013
5012
5012
5412
5013
5011
5011
5014
5014
6013
6013
5011
5012
5012
5013
5010
5014
6013
SOI 2
5012
6012
5013
5013
5013
5011
5012
5012
5011
5012
5012
5013
5013
5012
5011
12.18
12.2
12.23
12.22
12.2
12,19
12.15
12.10
12.11
12.32
12.54
12.55
12.55
12-55
12.88
12.88
1253
12.82
12.65
12.73
12.77
1288
12,92
1298
1288
12.88
12,88
12.89
1296
12,94
1297
1302
13.07
1314
1317
13.11
13.13
13.09
13.12
13.19
13.17
13.18
13.14
13,1
13,08
U.1J
13.19
13J3
13,21
13.21
1J.21
11.28
13.34
13.39
13.38
13.38
13,37
1338
1124
13.13
not
1281
12.11
12.73
1289
1292
1257
1251
1248
12,36
1231
12,34
12,36
12,38
6,21
1,15
114
8.2
1.22
0.25
1-21
8.3
133
8.2
801
•
802
803
901
904
805
799
7.S8
7.87
7.71
7-»7
7.85
7.85
7.63
7.62
7.61
7.59
7.S3
7,55
753
7.5
7.47
747
7.45
7.45
7.48
7.51
7.46
7.44
7.47
7.45
7.40
7.49
7.46
7.43
7.4
7.38
7.43
7.48
7.47
7.4
7.32
728
7.28
7.29
7.27
7.27
7.38
7,49
7.61
7.76
7.13
7.11
704
7.07
•
802
7.98
8
799
7.96
7.81
7.81
Witer
THC bitonct Kfcal flow rite he* out
ppm In gprn STU
776 11 6.7 831.3
788 11 87 858.7
756
73?
725
704
880
858
634
921
911
616
816
805
801
596
597
593
588
57?
668
680
598
801
808
818
833
841
644
638
641
638
834
633
619
615
820
598
597
589
512
597
590
SN
577
577
575
564
554
549
551
548
552
595
557
564
562
560
569
570
562
548
583
582
573
683
590
596
619
643
685
671
671
668
858
646
11
106
10.5
10.5
105
10.5
10.5
10.5
10.5
10
10
10
10
95
9.5
9.5
95
9.5
9.5
85
9.5
9.5
9
g
1
8.5
8.5
8.5
6.5
8.5
65
86
85
85
8
8
6
g
1
7.8
7.5
75
7.5
7.5
7-8
7.5
7.S
7.5
7.1
7
7
7
65
66
62
7
7
7
66
6.5
6,5
6
6
6
8
8
6
5.5
8.5
8.5
5.6
6
55
6.7
6.7
6.7
6,7
8,7
8.7
6.7
6.7
8.7
67
8.7
9.7
6.7
8,7
8.7
8.7
«.?
• 7
6.7
6?
8.7
6.7
6.?
6.7
6-7
8.7
6.7
6.7
6.7
6.7
87
6.7
67
6.7
6.7
67
6.7
8.7
8.7
6.7
8.7
8.7
6.7
8.7
6.7
6.7
8.7
6.7
6.7
87
8.7
6,7
67
6.7
6.7
8.7
67
6.7
6-7
6.7
6.7
8-7
6-7
8.7
e.i
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
658.7
•53.1
•53.2
•47.7
869.6
875.0
8587
6812
6478
664.1
642.3
853.2
574.0
6423
8388
831.4
6587
858?
8588
875.2
675.2
647.9
858.8
642.4
831.5
631.5
826.1
9370
931.5
9534
664.3
6589
689.8
858.9
6534
8091
6460
647.9
631.6
820.7
831.7
6480
631.7
659.0
642.8
8535
8318
653.8
6426
6426
•15,4
620.8
637.2
620.8
8372
6481
8318
8536
620.3
M82
•20.9
604.5
593.6
•31 .B
513.6
810.0
6100
653.6
810.0
9210
848.3
9537
8538
681.1
Water meter
Drill Coot wtter reading
On/Off derrsly, ttfgal gpm
On 8J.17 8.6
On 817 46
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
8.17
8.17
8.17
8.17
8.17
8.17
0.1?
8.17
8.17
8.17
8.17
8.17
8.17
8.17
8.17
8.17
8.1?
8.17
8,17
8,18
8 18
81?
8.17
8,17
8.17
817
• 17
•.17
B.17
• 19
818
818
• 18
8.18
818
81B
BIB
8.17
811
818
811
B18
8 18
1.11
818
S.18
8.18
818
618
•.18
8.18
818
B.18
8.18
B.18
8.18
818
818
811
8.18
8.18
8.18
8 IB
8.10
0.18
8.18
6.18
811
B.1B
S.18
8 18
B 18
8 18
818
6.8
66
6.6
6.6
88
6.6
6.6
6.6
6.6
6.6
6.6
6.6
66
66
6.6
6.6
S.6
6.8
6.8
6.8
6,6
68
6,8
60
66
6,6
6-6
6.6
69
66
66
66
66
6.6
66
66
6.6
6,6
8,6
88
66
8.6
6.6
8,6
6.6
8.8
8,8
6,6
6,6
66
6,8
8.9
8,9
6.9
6,6
66
6.8
6.6
68
6.6
6.6
6-6
6.6
8.6
6.6
6.6
6.6
6.6
6.6
6.6
8.8
6.6
06
66
-------
FURNACE A WITHOUT CATALYST, HIGH HEAT REMOVAL RATE
02-Apr-96
IB-Jun-95
Run TTD-2B Scoping test 2
time stack end dilution H2Oin H2Oout fceixn ambient stovteidt COWoti GO (Union CO tow
«•= *>SF <*«SF *9f *Jf degF *jF degF pnm ppm pom
2»"» «J » 151 tai 514 67 172 W22 7897 5012
28508 181 76 151 183 511 37 171 ,w 75ee M11
26568
28828
2B888
2874B
28)08
29668
28924
28884
29044
29104
29164
29224
29284
29344
29404
29484
29524
29584
29844
29704
29784
29824
29884
29M4
30004
30084
30124
30184
30244
3D300
30360
30420
i 30480
i 30540
) 30600
30660
30720
30780
309X0
10900
10960
31020
31080
31140
31200
31280
31320
31380
31444)
31500
31560
31620
31678
31738
31796
31956
31916
31976
32036
32096
32156
32216
12276
12136
32390
32456
32518
32578
32636
326M
32758
32816
32878
32936
101
181
181
162
162
162
163
163
162
163
163
163
163
182
162
181
181
181
162
182
182
182
163
162
1(2
162
16!
161
181
161
162
162
163
164
164
164
164
164
163
163
163
162
183
163
163
163
183
163
183
162
162
162
163
163
163
164
164
164
164
165
164
164
163
162
162
161
161
161
181
161
162
163
183
183
it
11
11
78
77
77
77
78
74
73
73
73
75
76
77
78
78
78
77
77
76
75
74
73
73
73
75
76
77
77
77
77
77
75
74
74
73
74
75
75
75
76
76
76
76
78
75
74
73
73
74
75
78
77
77
78
77
76
74
74
73
73
73
73
75
76
77
77
78
77
77
77
76
74
IS!
152
151
152
152
151
152
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
150
15t
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
151
150
151
150
150
151
151
151
191
151
151
151
151
151
151
151
151
163
163
163
183
163
163
163
183
163
163
1«3
163
163
163
163
163
163
163
183
183
163
163
183
183
162
183
162
183
161
163
162
163
163
183
162
162
162
162
162
162
163
163
183
162
1(2
162
183
163
163
163
163
163
163
163
183
163
163
163
163
163
183
163
163
181
181
163
163
163
163
161
183
183
183
163
510
510
509
508
509
507
507
505
505
505
505
506
508
509
508
507
506
506
505
504
505
506
507
508
508
50)
MO
511
513
512
513
513
511
510
510
511
513
513
51]
514
514
512
509
50B
504
503
504
504
503
499
497
502
509
510
508
506
505
504
502
500
499
498
496
4)1
4)7
4)9
4)3
4)2
480
480
479
480
4)9
490
87
•7
87
88
68
68
88
88
68
67
87
67
67
86
67
67
67
68
68
66
88
68
68
68
68
•7
87
87
88
87
88
68
68
88
88
68
88
68
87
68
88
88
68
68
68
88
88
88
88
67
67
87
67
67
88
88
88
68
68
67
67
67
67
88
67
87
67
67
67
68
88
68
68
68
170
170
170
170
171
171
172
172
172
173
173
172
172
172
171
171
171
171
171
171
171
172
172
171
171
171
171
170
170
170
170
170
171
172
172
173
173
174
173
172
172
172
173
172
172
172
172
171
172
172
171
172
172
172
171
172
172
173
173
173
171
172
172
171
171
170
18)
189
189
189
170
17t
171
172
1891
B921
8900
8415
8370
8301
8346
8407
8423
8394
6297
8093
7902
7922
7813
7776
7833
7813
7772
7837
7857
7772
7842
7870
7981
7928
7385
7442
7422
7418
7422
7491
7463
7406
7483
7410
7406
723)
7129
7182
7182
7121
7227
7345
7503
7115
736)
7174
8B2S
8816
6954
8897
8405
5900
5819
5623
5859
8904
5877
6010
5981
•014
•124
5653
5904
5888
9949
8071
6075
8213
6294
6401
6787
6986
750
725,3
722
707
700.2
899.5
8)6.5
706.1
715.7
715.2
707.8
689
658
6484
6387
626-6
635.6
•37
624
6312
836.1
834.3
815.9
61)3
•12-3
8071
581-7
58S.1
588.3
980.2
584.3
991.6
585.4
5895
588.4
586.4
585.1
585.3
550.1
551.4
552-9
945-2
956.8
582.2
582.5
593,8
589
S54.4
S28.1
509
113.8
531.1
482.4
3983
301 1
3888
391
408.4
4116
410
4095
417.2
425
404.6
390.8
406.1
3994
41f.)
41)
433.1
437.1
4497
4M1
5348
5013
5013
5014
5013
5013
5012
5011
5010
5012
5014
5015
5011
5010
5011
5013
5012
5012
5013
5012
5011
5010
5011
5013
5013
5011
5012
5014
5013
5011
5012
5011
5013
5013
5011
5013
5013
5012
5012
5013
5012
5011
5012
5012
5012
5011
5011
5010
5013
5010
son
5011
5011
5012
5012
5011
5013
5010
5011
5014
5010
SOU
6014
5010
5010
5011
5011
9012
9014
9012
9013
9012
5013
5014
5013
O2 CO2
pereeri percent
12 37 7.82
12.41 7.92
12.43
12.48
12.BS
12.B8
12.89
12 82
1282
12)2
1284
1279
12.81
12.8
12.78
12.75
12.73
12.84
1289
12.9
1291
1291
1292
12)5
12)4
1293
12.94
12.93
12.83
1279
12.73
12.89
12.74
12.75
12.72
12.75
12.67
12.7
1264
12,84
12.67
12.7
12.71
1275
12.79
12.81
12.8
12.84
tuts
12)3
1288
12.87
1294
1283
1239
12.21
12.24
12.3
12.37
12.53
12.51
12.52
12.57
12.6
12.6
12.86
12.86
12.9)
12.98
12.97
12.98
12-97
12.96
1294
1265
1278
7.9
7.88
7)1
7)2
79
?«
7.)7
7.95
795
7.95
795
799
902
8.08
805
7.99
7.M
7.9
791
7.9
7.88
7.92
7.81
7.93
7.9
7.95
8.04
8.07
8.06
807
60B
6,09
608
8.06
8.12
8.12
BIS
B13
8.13
8,08
8,09
805
801
B
7)8
7 BS
7.97
7.95
7,9
7.88
7,8
7,89
8,12
8.29
828
8.25
8.2
8,08
812
B.08
8.05
8.02
B
795
7.71
7.8
7.84
7.12
758
7.57
757
7.61
772
7.77
tAj*»»r
THC balance actual flow rate Mat out
ppm bs gprn BTU
638 5.5 67 848.3
635 5.5 67 6265
629
621
618
808
612
618
618
•20
613
806
599
592
591
591
583
584
583
571
589
564
554
542
535
526
518
513
515
516
516
514
514
517
516
519
519
508
497
501
518
527
538
563
573
590
MM
812
572
538
492
484
440
382
319
315
310
308
305
304
288
278
289
285
262
280
259
257
251
250
249
294
283
302
367
287
5
5
5
5
48
45
45
45
45
45
48
45
45
45
4
4
4
38
3.5
3-5
3.5
35
3,4
3-5
35
35
35
3
3
3
3
3
35
3
3
3
3
2.5
25
25
2
2
2
2
2
1.5
15
1.5
1.5
1.5
1.5
1.5
1.5
1.5
0.5
05
0.5
O.S
O.S
0,5
0,4
0
0
0.2
• 7
87
8.7
• 7
8.7
6.7
8,7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
67
67
67
67
67
87
67
87
87
67
6.7
6.7
6.7
8.7
6.7
6.7
8.7
87
6.7
6.7
67
6.7
6.7
6.7
6.7
6.7
6.7
6.7
8.7
8.7
87
6.7
8-7
6-7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
5.7
8.7
6.7
8.7
67
6.7
6.7
6.7
6.7
6.7
6.7
67
821.0
820.9
837.3
815.5
604.6
5W.9
615.5
659.2
651.7
670.1
653.1
670.2
6592
6265
8265
610 1
631.9
0285
•31.9
•374
•269
6374
637,4
6483
8593
•421
•320
•156
589.8
837.4
828.5
621.0
6374
642.9
826.5
837.5
632.0
642.9
637.5
626.5
648.4
846.4
832.0
832.0
642.)
8156
832,0
8429
•64.7
8593
6484
6052
6320
6429
632.0
637.4
631.9
642.9
870.2
653,9
8648
884.8
651.)
653.9
659,3
628,5
6320
8285
•21.0
• 10-1
621.0
626.5
8320
659.3
Draft Cool water rearing
On/Off density, fc/gftl gpm
On 8,18 9,6
On 8 18 66
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
O»
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
818
8.18
8.18
818
818
8.18
8.18
818
BIB
918
8,18
818
818
818
8.18
6.18
819
818
6.18
8.18
8,18
8.18
8.18
8.1B
8.18
818
6.18
8.18
8.18
818
8.16
8.16
8.18
818
818
818
818
818
618
8 B
8 8
8 8
8. 8
a. •
8.18
8.18
9.18
818
818
818
819
819
818
8
8.
8
8.
a.
8.1)
B.1B
8.18
6.18
8.18
8.18
8 18
8.18
8.18
66
8,6
66
6,6
66
66
66
• 6
• 6
96
86
66
6,6
6.6
8.6
6.6
6.6
96
66
66
66
68
66
68
8.6
6.6
68
66
86
88
6.6
66
6,6
6.6
66
6.6
66
6.6
68
68
66
6.8
88
88
68
66
6.8
8.6
66
66
68
68
B.8
16
6.6
6.6
6.6
66
86
6.6
6.9
68
6.6
6.6
6.8
•.6
6.6
•-6
6-6
6-6
6-6
68
66
-------
FURNACE * WITHOUT CATALYST. HIGH HEAT REMOVAL RATE
02-Apr-98
K-jun-K
time
see
32998
33052
33112
33172
33232
33292
333S2
33412
Run TTD-28 Scoping lest 2
slack exit
deaP
163
183
162
181
160
160
180
cSMion
&S F
73
71
73
73
74
76
77
H2Otl
*gF
lit
150
150
ISO
1S1
151
151
H2Oout
dejF
162
183
182
162
183
163
182
Ike box
{leg p
483
419
49fl
495
494
464
483
ambient
In •
59.21%
6.6 gpm
3.95 drykg/hr
2i14%
40,922
70,125
-------
FURNACE A WITHOUT CATALYST-HIGH HEAT REMOVAL RATE
02-Apr-M
27-Jun-95 Run TTD-2C
time stack exit dilution water in water out fire-box ai
sec
3080
3140
3200
3260
3320
3380
3440
3500
3560
3620
3680
3740
3800
3860
3920
3980
4040
4100
4156
4216
4276
4336
4396
4456
4516
4576
4636
4696
4756
4616
4676
4936
4996
, , 5056
Q 5118
, . 5176
Lrt 52M
5296
5356
5416
5476
5532
5592
5652
5712
5772
5832
5892
5952
8012
6072
6132
6192
6252
6312
6372
8432
6492
6552
6612
6672
6732
6792
6852
6908
6968
7028
7088
7148
7208
7288
7328
7388
7448
7506
7566
F
129
123
116
112
110
108
108
107
107
107
108
107
108
108
108
109
109
110
110
110
111
111
112
113
113
113
115
114
115
115
116
116
117
117
116
118
119
119
120
120
121
121
121
123
135
134
134
137
139
142
144
145
147
148
149
150
151
152
154
155
156
157
156
156
159
161
163
164
165
169
174
177
160
162
184
186
F
93
69
67
67
67
87
87
87
87
87
88
67
87
67
87
86
86
86
86
88
88
85
88
88
87
87
87
87
86
88
88
88
88
86
88
89
89
89
89
69
89
89
89
89
91
92
93
93
93
93
93
93
93
94
94
93
94
94
95
95
95
95
95
95
95
96
96
97
97
98
99
100
100
101
101
tot
F
184
164
164
163
163
163
162
162
162
161
161
161
160
160
160
160
160
159
159
158
158
156
158
157
157
157
157
156
154
155
154
154
153
154
153
153
153
153
153
153
152
152
152
151
151
151
151
151
151
150
150
149
150
149
149
149
148
149
148
148
148
147
147
147
147
147
147
147
146
146
146
146
146
146
145
145
F
173
173
173
173
172
172
172
171
171
171
171
171
171
170
170
170
170
170
170
169
169
169
169
168
168
168
188
167
167
167
167
167
168
168
166
166
165
165
165
165
164
164
164
164
163
163
163
163
162
162
162
162
161
161
160
160
160
160
160
159
159
159
159
158
158
158
158
157
158
157
157
157
157
157
158
156
F
209
185
181
179
179
179
180
180
181
182
183
184
184
165
186
186
167
167
188
188
189
169
190
190
191
191
192
192
193
193
194
194
195
195
196
196
196
197
198
198
199
199
200
200
170
150
206
396
441
435
426
394
385
380
369
356
335
316
308
303
306
306
301
304
314
363
474
466
421
375
363
362
367
379
394
415
nbient stack
F
79
80
80
79
79
80
79
80
79
80
79
80
79
80
80
80
80
79
79
79
79
79
79
79
80
79
79
80
79
79
80
80
80
80
80
80
80
80
80
81
81
80
80
80
60
80
81
80
81
81
80
80
80
80
81
61
81
81
81
81
61
61
61
81
81
81
81
61
61
81
81
81
82
82
82
82
F
140
135
129 •
124
121
119
118
118
118
118
118
118
118
118
119
118
119
119
120
120
121
121
121
122
123
123
123
123
124
124
125
125
125
126
126
127
127
127
127
128
128
129
129
130
137
141
143
146
149
150
152
153
154
156
156
156
158
180
161
162
184
184
185
186
167
189
171
172
174
177
181
184
186
188
190
192
CO high
ppm
6103.5
3068
31778
69702
111328
140096
158936
17077.6
17806
182088
184977
188395
191325
19409.2
19604.5
198364
20039.9
201375
202799
204956
20674.6
209876
21301.3
21521
215739
21651.2
217163
217814
218471
21525.1
21679.7
217529
21712.2
21687.5
21781.4
21785.5
218872
22106.9
22166
225827
228878
232381
237712
24308.3
25533
217326
189149
174357
17614.7
17374.7
17578.1
18033.9
18538.4
19014.5
19458
20084.6
20731.6
214884
21765.1
22216.8
232259
23807.8
24153.6
24137.4
24393.7
24226.9
25012.2
281108
25752.8
253418
28377.3
32421.9
346598
384339
37040.2
37744.1
COdkl
ppm
495
1898
575
133
192.1
230
253.1
2892
2747
282.6
286
2869
2913
2998
301.6
3099
3219
327
3328
3397
343.9
353
3576
3836
3678
3765
3778
3804
384.8
3802
3849
388
392.1
394
402.3
4056
4108
4108
4106
4245
4357
4456
4591
471.4
9813
14429
11878
13776
13377
13197
13583
1392.1
14451
14832
15184
1589.4
18393
17223
1738.8
1795.4
1932.5
1941.8
1966
1963.4
1999.5
1968.1
20029
20034
20039
20042
20042
20033
20039
2003.7
20044
20042
CO tow
ppm
4845
3182
30776
49752
50069
50094
50077
50061
50077
5009
50077
50069
50069
5007.7
50081
5007.3
5009
50081
50081
5009
5007.3
50077
50094
5009
50069
50073
50081
50085
50069
50073
50073
50081
50069
5008.1
5009
50081
50098
50085
50085
50085
50077
50069
50053
50073
50073
50073
50081
50073
50077
50085
50061
50053
50094
50077
50069
50069
50077
50085
50077
5007.3
5007.7
50057
50057
50069
50053
50073
50073
50073
50069
50081
50085
5006.9
50069
50061
50073
5007.7
02
%
1518
183
1888
17.46
1575
14.58
139
1353
1331
1323
1318
13.12
1302
1297
1294
1294
12.93
12.97
13
1302
1306
1305
12.98
1294
1299
12.95
1294
12.89
12.91
1295
12.9
12.88
1289
12.92
1288
12.88
1286
1283
12.85
128
12.73
127
12.64
12.55
1241
13.16
15.39
15.75
1525
15.17
15.12
15.05
15
1493
14.83
1484
1471
1454
1436
1414
1389
1367
1355
1353
1346
1333
12.96
12.5
1251
12.34
11 1
992
939
9.21
901
886
C02
%
431
1.74
134
259
3.97
491
548
583
6.05
618
827
639
6.51
661
668
674
679
6.79
68
68
682
687
695
7
7
703
7.04
709
708
703
709
712
7.12
7.1
716
7.16
7.2
725
724
734
743
749
76
773
7.97
691
476
463
5.21
533
542
549
554
563
578
592
606
622
641
684
6.87
706
718
718
725
7.38
7.78
82
819
848
982
1094
1139
11.68
11.84
11 98
Water
balance actual flow rate
t»
87.0
87
875
881
67
67
67
87
88.2
87
87
869
665
665
885
865
865
'865
865
885
885
865
865
865
86.5
86.5
665
665
665
865
86.5
86
86
86
88
86
86
88
86
86
86
86
85.5
855
85.5
85.5
85
847
84.5
845
84
84
835
835
83
82.5
82.5
82
82
815
61
61
80.5
80
80
79.5
79
785
78
76
771
766
76
75.5
75
743
7.8
7.6
76
76
78
76
76
76
76
76
74
74
7.4
74
74
7.4
74
7.4
74
74
68
6.8
68
68
66
68
68
68
68
68
68
6.8
6.8
68
68
66
68
68
68
68
68
66
68
68
68
68
68
68
68
6.8
68
68
68
68
68
68
88
68
66
66
6.8
68
88
88
68
68
68
6.8
68
6.8
68
68
68
68
68
68
heat out
In/Interval
554.16
55416
554.16
61594
55435
55435
616.15
554.54
454.54
61636
80169
801.69
66209
60190
601 90
60190
60190
61815
66231
88253
614.07
614.07
61407
614.27
61427
61427
61427
61447
72667
67055
71711
717.11
717.34
66195
71734
71734
66216
66216
68216
88216
61621
66237
86237
71780
86256
66256
66258
662.58
607.37
66279
86279
71825
80756
663.00
607.75
607.75
663.20
60775
68320
60794
60794
66341
66341
56758
60812
60812
80812
55284
86361
60831
80831
80831
80831
80831
80849
60849
Water meter
Draft Cool water reading
On/Off
-------
FURNACE A WITHOUT CATALYST-HIGH HEAT REMOVAL RATE
02-Apr-W
27-Jun-95 Run TTD-2C
lime stack exit dHution water In water out nre-box ambient
see
7628
7698
7748
7808
7688
7828
78(8
(048
•108
•166
6228
•294
8344
8404
•464
6524
(9(4
8644
1704
•764
8824
(8(4
•844
9004
8064
9124
9184
9244
9304
8384
9424
9484
B944
. 9604
O *660
,_., 9720
OS 978°
9(40
8900
9960
10020
10080
10140
10200
10280
10320
10380
10440
10500
10560
10620
10680
10740
10800
10880
10920
10980
11036
11096
11156
11216
11276
11336
11388
11458
11516
11576
11919
11598
11756
11(16
11878
11936
11986
12056
12116
!•
187
168
188
188
193
202
208
213
215
217
219
219
220
219
219
219
218
220
220
222
222
222
223
223
223
223
223
223
222
221
220
220
220
220
220
219
219
218
218
218
218
217
217
217
217
217
216
217
217
216
216
215
215
215
214
213
213
212
211
212
211
210
210
209
210
210
210
209
208
206
208
208
207
206
205
204
t-
102
102
102
102
104
106
107
108
108
108
108
106
107
107
107
107
107
107
108
108
106
108
m
108
108
108
106
10*
108
108
108
108
109
108
108
108
108
107
107
107
108
108
107
107
107
107
107
107
107
107
107
107
108
108
106
106
106
108
108
106
105
105
105
105
105
105
105
105
104
104
104
104
103
104
104
104
f
149
145
145
145
146
146
145
148
146
148
146
147
147
147
147
149
149
148
148
148
149
141
149
150
149
190
150
150
150
190
191
151
151
151
191
192
192
152
15)
153
193
191
153
151
151
194
194
154
194
154
159
155
195
155
155
155
159
196
158
156
157
157
157
157
157
157
158
158
156
158
198
158
158
158
158
158
F
156
158
156
156
158
156
157
157
157
157
157
156
151
158
198
158
158
159
160
160
190
m
191
191
191
iet
162
182
192
162
162
161
191
16)
163
164
184
164
194
195
165
165
185
195
198
196
196
169
169
169
197
167
187
16*
168
168
168
188
1(8
16*
169
189
169
170
170
170
171
171
171
171
171
171
172
172
172
172
f
412
446
455
497
787
1128
1161
1160
1097
1096
1043
1021
1109
1162
1162
1162
1150
1110
1065
10)4
1029
1028
1027
1028
1017
1038
1027
1005
891
978
981
SI*
845
818
910
933
840
847
959
860
960
857
847
914
619
911
910
914
919
916
912
911
928
991
960
«56
844
815
•18
950
955
954
995
812
103?
1090
1115
1111
1105
1108
1113
1097
1115
1126
1095
1101
F
(2
82
82
62
82
(2
82
82
(2
82
(2
83
n
62
83
n
n
n
n
83
82
(s
n
82
83
n
n
93
83
63
•3
83
93
93
n
(3
91
m
m
63
93
S3
91
83
•3
94
M
94
M
94
83
81
M
•3
n
83
M
n
83
13
B3
83
n
n
93
83
83
84
14
94
93
(3
81
83
83
83
stack
F
1*3
194
1*5
195
1*9
207
215
221
229
229
231
232
234
233
211
231
21)
213
215
216
218
239
238
23*
238
239
2K '
237
218
239
2)9
2)5
239
219
216
219
239
23$
214
235
235
239
119
235
235
2)4
235
219
2)5
2)5
239
219
216
239
2)5
2)4
2)4
213
214
234
234
233
211
230
2)1
2)2
232
231
230
228
227
226
225
223
222
220
COWgh
pom
16)484
191673
381185
3*521.3
36181.1
41198.2
47721.4
499169
496617
49267.8
4977*.!
47984
489M4
476766
482969
490M.7
47810.1
47721.4
46464
45454 B
463)1.1
47*91.)
4*2(11
492*51
457(8.2
4453*4
44988.6
445384
43879.1
434652
4)084.8
421*5.6
41411.5
407104
39929.2
38(50.0
38240.6
182124
M277.S
386353
3*611.6
408)6.6
41391.5
406244
40512.8
41324.9
420025
43926.2
4414(8
44192.2
44498.7
44401
4 3803 B
41387.5
43200.7
42818.2
42545.6
42860.8
438493
43204.7
38237.5
35837.5
33219.7
!t7KU
31646.8
304321
298187
266276
2S916J
24810.5
245321
250081
248989
24056
218665
232058
CO 0*1
pucn
2004.7
2003)
20019
2001.9
20034
20041
2003.1
2001.4
20014
2003.7
2004.1
200J.7
20042
2001.7
2001.7
2003.1
20037
20039
2004.1
20034
2004.7
2004.1
2001.7
2004.1
20041
20042
2004.1
2002.*
20044
2001.7
20034
20044
2004.1
2003.1
20017
2003.1
2003.7
2004.1
20041
2004.1
20041
20034
2003.1
2003*
2004.6
20036
200)9
2004.2
200)6
2003.7
20011
20038
2004.1
20031
20041
20042
20037
2004.6
2001.1
2004.1
2001.7
2001.9
2004.1
2001.7
20011
2003)
20041
2001.9
2001.7
20031
2003.8
20037
19049
1*408
19439
1901.1
CO tow
pom
5006.1
5006.9
500(5
9005.1
900? .3
5006,1
90094
500*4
50069
5007-7
50081
50073
5007.7
9008.1
9008.5
50073
50061
50093
5008.1
5007.7
50061
900(4
5005.3
5006.1
9005.7
5007.1
50091
5009.7
50073
50094
5009.4
5O045
50099
5007.7
5007.1
5009,1
S009.7
8007.1
5008.*
90094
5005.1
5007.3
5006.1
90077
9004,1
5009,1
9008
5009.5
9009.9
5007,7
5006.8
5009.5
5007.3
50073
9007.1
5004-9
50071
5009.1
5009.5
5006,*
5009
50077
5006.5
5007.7
9007.3
9005J
50091
5009.7
50073
5007.1
90065
50057
5007.7
5009.9
50061
50091
O2
%
B.?6
8.7
8.71
884
(.76
7.27
473
398
393
4
4
398
401
4.08
4.11
4.4
439
412
419
1.87
1.91
1*8
1*7
1.1
192
383
383
383
184
1*4
3.9
193
387
384
387
389
382
3.76
1.76
3.95
3.77
399
1.96
1.91
3.7
1.7
1.68
398
3.69
395
3.97
1.99
1-96
1-97
1.65
3.66
3.95
1.69
1.61
1.96
361
179
3*9
4
3.87
3.71
368
3.72
383
4.04
419
4.44
4.75
494
507
524
CO2 JUM-THC
% pom
12 08
12.18
1218
1204
12.14
13.73
18.13
16.72
1672
1994
te.e?
18.72
16.74
1696
16,11
1(0*
18.15
1818
1643
16.72
16.78
16.69
18.55
16.85
1694
1681
1978
19.76
16.76
197
16.61
16.6
16.84
197
1689
1671
18,?6
19,?7
19,79
1611
18.85
1988
1888
1868
1691
16.78
1878
16.79
19.75
16.71
1697
16.61
16,57
18.51
1945
19.18
16.15
18.31
19.29
19.32
1938
16.23
16.05
15*5
1583
16.13
16.28
16.36
16.3
18.12
15-M
15.5
15.14
149?
1465
14.68
Water
balance actual flow rate
In
71.9
73
721
715
707
70
98
98
675
895
955
94.5
94
93
62
81 5
90.5
9C
58
58
57.5
56.5
555
55
54
91.5
92.5
52
51
50.5
49,5
48
49.5
47.5
47
49.3
45.5
45
44,1
43.5
43
425
41.5
41
40.5
40
39
385
19
17.5
39.7
39
15.5
35
345
34
31.5
13
12.5
32
11.5
11
90.5
10
295
295
29
28.5
29
28
27.8
27
265
26,5
28
25.8
gpm B
68
6.9
98
88
68
68
98
68
96
68
8.8
98
69
96
68
6.8
88
86
66
68
98
88
68
6.8
68
66
6.6
9.9
66
68
8.8
86
98
68
8.9
6.8
69
(.9
8.8
68
8.8
6.8
61
6.9
6.9
6.6
98
6.8
68
68
98
88
86
6-8
6.9
6.8
98
66
61
98
88
88
98
6.8
(.(
8.8
68
8B
68
8.8
9.8
98
98
96
8.8
6.8
neat out
tuMmal
808*9
808.49
80849
60849
591.01
59101
(6181
90831
60831
90831
567.76
(08.12
80812
608 12
68341
607.84
907.84
90794
66320
693,20
60775
907.75
96300
90756
68300
60756
662,7*
(62.7*
86279
69279
60737
682.56
69258
610.41
862.58
662-37
662,37
662.17
80696
962.16
882.18
6(2.16
692.16
0(2.16
717.34
961.85
961.85
(61.85
9(1.85
691.85
681 73
(61.73
(61.7)
718.66
716.88
71696
817.41
86152
716.94
716.64
661.30
96130
691.10
716.41
716.41
71(41
71817
71617
716.17
716.1?
716.1?
716.17
715.83
71581
71»d
715.83
Draft
OnftOff
OH
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
Water meter
ter
tygil
6 19
818
819
8.19
819
(.19
6.19
81*
819
(.19
8 19
(.19
1.19
919
918
819
8.11
8.18
8 19
• 19
1.18
918
818
• 16
818
8.18
816
818
818
6.16
8.1>
9,16
sie
818
818
818
9 18
(18
817
6.17
817
8.t7
(-1?
(.17
(17
817
6.17
8.17
(.17
817
817
817
117
8.17
817
817
817
8.17
6.17
8.17
816
816
816
8.19
(.18
(.16
816
6.16
(.19
(16
(.16
(16
• 19
819
• 18
8.1(
readng
gprn
9.7
9.7
8.7
97
(.7
87
67
6.7
6.7
87
8.7
6.7
(7
9.7
6.7
6.7
6.7
6.7
(.7
(7
(7
87
9.7
9.7
67
97
97
9.7
9.7
67
67
8.7
8.7
67
67
67
6.7
6.7
87
67
67
8.7
8,7
9.7
97
9.7
87
8.7
6.7
6.7
67
67
8.7
9.7
9.7
6.7
97
6.7
8.7
67
6.7
9.7
8.7
8.7
9.7
67
87
6.7
87
6.7
8.7
67
67
(7
6.7
6.7
-------
FURNACE A WITHOUT CATALYST-HIGH HEAT REMOVAL RATE
02-Apr-96
2?-,)Uf»-e5 Run TT&-2C
time stack eat dfejticn w»t*r in wattr out fire-box ambient
sec ** r "" "
12178
-~j
12296
12356
12412
12472
12532
12592
12852
12712
12772
12832
12892
12952
13012
13072
13132
13192
13252
13312
13372
13432
13482
13552
13612
13672
13732
13781
13848
13908
13968
14028
14088
14148
14208
14268
14328
14388
14446
14508
14581
14628
14688
14748
14(08
14888
14128
14988
15048
15108
15184
15224
15284
15344
15404
15464
15524
15984
15644
15704
15784
15824
15884
15944
16034
18064
16124
16184
18244
16304
16364
16424
16464
16540
16000
16660
r
201
200
200
200
200
201
201
201
197
162
167
157
151
148
145
143
142
140
136
137
136
135
134
132
132
130
130
128
128
128
127
126
125
125
124
123
123
122
121
120
119
119
tie
118
117
116
115
114
114
114
113
113
121
127
132
136
139
141
144
145
148
151
153
155
156
158
180
181
183
163
163
165
165
196
167
168
r
103
103
103
104
103
103
103
103
10!
98
97
98
98
98
96
95
98
95
95
95
95
95
95
95
95
95
95
95
93
92
91
90
90
90
89
89
89
88
M
88
87
87
87
86
88
86
85
(5
86
86
86
85
87
88
89
89
(9
89
89
89
89
89
89
10
90
90
90
90
90
90
90
90
90
90
90
90
r r
15S 172
159
159
159
159
159
159
160
160
180
180
160
160
160
180
180
180
160
160
160
(80
160 '
160
159
150
1S6
158
1ST
157
156
156
1(6
155
155
154
154
1S4
154
153
153
153
153
153
153
152
152
152
1S2
152
152
1S2
152
151
1S1
151
151
150
150
149
150
149
149
149
149
149
149
149
ISO
ISO
150
150
150
150
ISO
150
150
172
173
173
173
173
173
173
173
174
173
173
173
173
173
173
173
173
173
173
173
173
172
172
172
171
170
170
169
166
188
188
187
167
168
186
166
166
168
165
165
165
1(5
185
165
184
184
164
194
184
183
163
163
163
182
182
182
182
161
161
161
161
181
160
161
161
161
161
162
162
162
162
162
182
162
162
t-
1126
1146
1157
1163
1163
1128
1057
1038
1023
915
803
738
695
687
643
624
611
59?
588
574
581
552
544
538
531
526
519
515
511
507
503
498
493
488
4(4
481
478
474
470
466
462
458
455
453
450
450
447
445
442
442
440
438
458
488
511
559
801
848
707
740
770
792
816
843
875
899
913
925
932
937
928
924
827
926
935
947
F
83
83
84
83
83
(3
B3
83
83
83
83
83
83
(3
83
83
83
83
(3
(3
(3
83
(3
63
(3
83
(3
(3
84
84
M
84
84
84
84
M
84
(4
84
84
84
84
84
M
83
83
83
83
(3
(3
83
83
83
83
83
83
63
63
83
(3
82
(3
63
(3
63
63
(3
63
82
83
83
83
82
82
(2
82
stack
F
218
218
214
214
214
215
216
215
213
204
191
181
172
186
180
157
154
151
149
147
146
144
143
141
140
139
138
137
137
198
135
135
134
133
112
132
131
131
130
129
129
128
127
127
12(
126
125
125
124
124
124
123
129
134
139
142
146
148
1(1
154
157
160
162
164
186
186
189
171
171
172
174
174
US
176
177
178
CO high
opm
22257.5
22528
228516
22876
22819
22768.1
21582
20922.8
20312.5
18176.3
2324J.2
32181 8
32894.5
2961(3
28253.3
23453 B
211(7
19335.9
17716.S
16459.1
15346.3
14388
13809.8
12923.2
12430.8
12052.4
11(12.3
116699
11584.5
115(4.5
11(007
11495
11254.9
11047.4
10778.8
103(4.1
10087.1
9847
85744
KW13
9261.1
91105
8980.3
(117.5
(891.4
8703.8
8589.7
8512.4
(394.4
(4147
8349.6
8385.9
8797.2
7539.9
7983.1
10620.1
12923.2
13883.5
138916
13810.8
14209
19384.9
16300.5
18821.3
17810.7
16249.S
18261.7
18066.4
17867.6
17439.8
17745
18050.1
17642.6
17528.2
17504.9
17570
COrJIu
ppm
17402
17975
1841 8
16109
1618.4
1821.1
1826.3
t827.1
1520.5
938
728.5
888
785
874
5(2.2
513.5
455.7
411.5
370.4
337.2
308.6
284
284.8
246.4
235
228.7
217.6
220.7
217.3
2178
218
210
2004
195
1(88
176.7
172.2
1862
160.2
154.3
1514
145
142.7
1393
1344
134.4
131
1299
1ZT.3
126.8
1232
123.4
457.5
452
621.6
(337
9S2,(
990.2
979
983.(
1036.S
1130.5
1186
1218.6
1289.2
1328.6
1318 B
1299
1258.1
1268.8
1291 2
1321.1
12845
1274.9
12804
1287.8
CO low
ppm
5009
5005.7
5007.3
5004.9
5005.7
5009
5008.5
5009.8
5007.3
5008.5
5010.6
5007.3
5008.1
5007-3
5006.9
5009
5007.3
5006.9
son
5007.3
5006.5
5007.3
5007.7
5007.3
5007.3
5007.7
5007-7
5006.5
5008.1
5006.8
50053
5007.7
5006.9
5009
5009
5008.1
5008.1
5008.1
5008.1
50073
5006.5
50081
5007.7
50085
5006.9
5008.1
50073
50077
5009
5008.5
5007.7
5009.4
5005.7
5007.7
5007.7
50073
5008.$
50073
5008.$
50053
5007.3
5007.7
50001
5009.4
5008.5
5008.5
50069
5007.7
5008.1
5006.5
5006.9
5008.1
5007.7
5007,3
50004
5008.1
O2
S.5(
5.96
59
5.63
5.41
5.22
5.06
5.25
601
7.07
(.78
948
10.18
10.8
11.15
1133
11.51
11.66
11.8
1181
11.82
11 99
11.13
11.93
1195
11.96
12
12.02
1213
12.17
12.19
12,22
1229
12.26
12-25
12-33
12.35
12.38
12.41
12.4
12.38
1235
12.39
1247
(2.48
1238
1243
12.45
12.46
1247
12.5
12.45
1201
13.21
14.4
13.57
12.53
1149
11.21
10.85
1029
984
946
9.12
893
8.9
8.71
8.55
648
847
1.54
886
873
874
(.92
(.49
C02 JUM-THC
% ppm
14 J
13(8
1388
14.11
1432
1451
14.98
14.36
1366
12.71
11.29
11 14
1083
10.34
10
9.73
941
9.14
8.87
8.71
854
636
8.24
6.13
8.02
7.94
7.85
7.76
7.64
757
7,53
747
739
7,38
733
7.2J
7.19
7,14
7,09
7,08
7.07
7,05
7,02
8,94
6.92
7
694
8.92
6.89
6.92
8,89
6,93
7.33
6.21
5.49
6.44
7.5
618
853
8B7
936
9.79
10.15
10.92
10.71
10.79
11
11 18
11.32
1136
1129
11.17
11.15
11.17
11.33
11.49
Water
balance actual flow rate
255
25
25
245
24
24
24
235
235
235
23.5
23
23
23
23
225
22.9
22.5
22.S
22.5
22.5
225
22.5
22.5
22.5
22.5
22-5
22.5
22
22
22
22
22
22
22
22
22
22
22
215
21.5
215
21.5
21.5
21.5
21.5
21.5
21.5
21.5
215
21.5
21.5
21.5
21
21
21
21
21
20.5
20.5
20.5
20.5
20
20
20
20
195
19.5
19.5
19
19
19
19
18.5
1(5
1(5
heat out
gprn Btufaterval
6.1 T1S.93
88
86
8.B
6.B
6.8
6.8
8.8
6.8
66
66
86
6.8
6.8
6.8
6.8
6.8
6.6
6.8
68
6.8
(.6
68
6B
66
66
6.8
68
68
66
6.8
(.8
68
6.8
6.8
(.8
68
6.8
8.8
8.8
68
66
as
6.8
6.8
6.8
6.6
6(
86
88
(.8
6.8
68
6.8
6.8
6.8
6.8
68
6.8
8.1
8.8
9.8
68
6.8
6.8
6.8
68
8.8
68
68
68
88
68
68
68
715.93
771 00
71960
771 00
771.00
771.00
71569
71569
770.T4
719.89
715.69
715.69
71569
715.69
715.69
715.69
715.69
715.69
715.69
715.69
71S.69
(60.64
715.63
715.93
716.17
617.01
71641
661.30
681,52
681.52
661.52
861.73
681.73
661.95
661.95
961.95
661 .85
717.34
66216
662.16
66218
662.19
682.16
717.57
682.37
682.37
56237
66237
61821
80717
60717
88258
682.58
907.37
60737
68279
692.79
693.00
607.56
69] 00
663.00
663,00
807,75
663.00
663.00
683.00
607. M
66279
662.79
662.79
862.79
818.90
862.79
662.78
662.79
Water meter
Draft Cool water reading
OnlOTI density. b;»il
On 8 16
On
On
On
On
On
On
On
On
OB
Off
Ofl
Ofl
Ofl
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Ofl
Off
o»
Off
Off
OB
OB
OB
OB
on
Off
Ofl
Ofl
Off
Off
OB
OB
Off
OB
OB
OB
OB
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
8.16
8.16
B.16
8.16
6.18
1.16
8.16
6.16
(.16
8.16
8.16
8.18
8.16
8.16
819
8.16
8.16
(.16
(.16
8.16
8 16
1.16
1,16
8.16
8.16
8.16
816
8.16
8.17
8.17
8.17
8.17
8.17
8.1?
8.17
817
817
8.17
(.17
8.17
8.17
8.17
( 17
8.11
a 16
818
B.ie
818
8.18
8.18
818
818
818
8.18
818
818
818
818
(18
6.18
818
8.18
(18
818
6.18
8.18
8.18
(.18
(18
8.18
818
818
818
818
818
gpm
6?
8.7
6.7
8.7
67
67
6.7
6.7
6.7
6.7
6.7
9.7
8.7
6.7
67
8.7
8.7
8.7
8.7
67
6.7
8?
67
67
6.7
87
87
8?
8.7
8.7
8.7
87
6.7
87
67
6.7
9.7
6.7
8.7
8.7
87
8.7
87
6.7
6.7
8.7
8.7
8.7
87
97
67
87
67
6.7
6.7
8.7
07
0.7
6.?
8.?
87
67
6.7
8.7
6.7
6.7
6.7
8,7
6,7
87
• 7
9.7
8.7
6 7
6.7
-------
FURNACE A WITHOUT CATALYST-HIGH HEAT REMOVAL RATE
02-Apr-ee
27-JUV85
RunTTD-2C
(me fttck rut dMwi wltwln w
sec *" *~ "
11720
•"""*
oo
18780
16840
16900
16960
17020
17080
17140
17200
17260
17320
17110
17440
17500
17560
17620
17880
17740
17800
17880
17916
17978
18036
18096
16156
18216
18278
18339
18388
18456
18516
1(576
18(36
18696
18756
18816
18876
18936
18998
18056
18116
19176
19236
19292
19352
19412
19472
19532
18592
19652
19712
19772
19832
19892
19952
20012
20072
20132
20182
20252
20312
20372
20432
20492
20552
20612
20668
20728
20788
20848
20908
20968
21026
21088
21148
21208
119
174
179
181
179
175
172
170
189
189
170
!7fl
170
171
169
167
166
164
184
1(1
182
162
161
161
162
1(2
161
181
181
111
1(0
1(0
160
158
159
159
159
159
158
1$l
159
151
158
158
158
1S8
158
151
151
151
151
158
158
151
159
160
161
162
162
162
182
1(1
184
119
1«5
199
168
1(8
1(6
1M
119
169
1M
1H
165
166
91
91
91
91
91
91
90
90
80
91
91
81
91
91
90
90
90
90
80
M
90
90
90
90
90
90
90
90
90
80
80
88
88
88
87
87
88
88
85
85
84
14
84
83
83
83
83
83
82
82
82
82
82
82
12
82
82
82
82
82
82
81
82
83
84
84
84
85
89
85
89
85
15
95
85
15
150
150
ISO
151
151
191
151
152
1S2
152
1S2
152
152
152
152
152
152
152
152
192
1*2
152
192
152
152
192
192
192
152
152
191
192
151
151
151
151
150
ISO
ISO
ISO
150
150
ISO
ISO
190
148
150
149
148
141
141
148
148
148
149
149
149
149
149
148
148
149
149
149
149
149
148
148
149
148
149
148
141
149
148
148
Heron fte-lxn MMM
F
162
183
163
163
164
164
164
164
1(4
154
194
194
164
164
164
164
164
1(4
1(5
1(5
164
164
194
164
164
184
1(4
184
184
164
194
194
193
194
163
163
163
163
163
1(3
163
163
113
1(3
163
162
162
112
183
162
162
192
192
162
162
162
162
182
182
182
181
192
191
1(1
161
161
161
161
181
tet
tet
tet
181
191
161
181
C
984
977
9*2
848
924
905
1M
192
883
828
890
848
939
841
80S
867
839
121
121
127
123
122
830
822
111
797
785
711
771
793
757
759
758
7(1
757
754
790
750
757
75S
754
757
746
741
741
746
744
738
730
725
720
712
708
709
701
897
895
896
88$
887
889
709
712
704
697
690
689
689
989
689
(M
Ml
M7
888
889
707
F
12
•2
83
12
12
82
82
82
(2
12
(2
82
82
82
81
82
82
82
82
82
82
12
•1
11
11
12
12
(2
It
11
12
12
12
•1
11
81
80
80
m
78
78
78
78
78
71
77
77
71
71
71
71
75
78
75
75
75
74
75
74
74
74
74
74
74
74
74
74
74
74
74
74
74
74
74
74
74
Hick
F
180
119
180
182
191
tH
119
183
182
181
185
185
185
118
185
114
111
179
171
177
177
177
177
171
171
178
175
175
174
174
174
171
171
173
172
172
172
172
172
172
171
171
171
171
171
171
171
171
170
171
170
170
171
172
172
172
174
174
175
175
175
175
178
178
171
171
179
179
179
178
178
178
178
|78
178
178
CONgll
ppm
17801.1
16179,8
19848.3
17831
145(3
143555
14(24
14578.3
149007
151411
14(112
148(4.1
149577
14847.8
140055
14833.3
18040
173177
180664
180705
11107.1
184285
1*8239
18335
110257
167109
188OT6
17513
160094
184183
11700.3
188802
191(9.1
194S8
198382
20417.5
20723.5
207479
20871.1
20M7.I
21297.7
21847.1
22082.8
22355,1
22705.1
22991
22901.5
22712
232747
237134
242719
2481M
24507.7
247558
25101,7
25348.9
25288)9
248186
24914.9
25117.2
252*4.1
2S822.I
253499
23974.8
23238.1
232178
230581
230141
230857
23491,8
23661 3
23897.3
244141
246138
260836
25418.1
COdfc
ppra
1311.1
12288
12703
1295.7
973
1060,5
1068.7
1094.2
1093.9
1115.4
1074.4
10W.1
1079,4
1071.3
1014
1107,6
1185,1
1289.9
1329.7
1300
13172
13384
13S6.4
1314
1291 7
11794
12123
1280.1
11101
13333
13813
13875
1397.9
1414.7
1494.3
15044
19138
19111
1524.8
1533.2
1555.2
1598.2
1(29.1
1892
16848
1711.1
1(851
1(94.8
1744.8
1783.5
1131.1
19586
1889.1
1887 S
19178
1941.7
1932.3
1881.8
1899.3
19279
18349
1874.4
1945.3
1781
1749.1
1752.3
1741.5
1734.4
1746.1
17914
178*8
1118-1
1171-5
1188,7
1940.1
1984
CO tow
9001.9
90015
5007.3
5007.3
5001.9
50085
50071
5007,3
5007,3
50057
50085
5001,1
50085
5001.9
90081
9008.1
5009.4
5005.7
5008
9007.1
9007.1
9008.1
9007.1
9007.7
9008.4
9007.7
5008
5007.1
50073
90877
90091
50061
9001.5
9008,4
5006.1
90077
9009.3
9008.4
5010,8
50077
50065
8007.7
9009.5
9001.1
5009.5
90091
50073
50077
5006 S
5008.1
5007.7
5008.1
§008.5
50061
50069
9007,3
9009
5009,4
5008,9
5009.4
9001.1
5008,5
5009
5007.7
5007.7
5008.1
50096
50093
5007.1
5007.7
5008
5007,1
50081
5005.1
8008.5
8007.7
O2
8,32
7.63
593
531
612
813
9.4
1.7
977
9.84
88
152
185
8.91
902
9.59
10.19
10.57
1089
1053
1043
10.44
1037
1013
1049
1073
10.98
11.04
11.05
11.07
11.06
11
1088
11 04
11.16
11.14
11.1
11 03
1089
10-89
1098
10 S3
1099
10.8
1091
10.87
109
11 32
11.41
1142
1139
11.33
11.31
11.32
11.24
11 19
1108
10.88
10,84
10.81
10.8
10,77
10.71
10.8
1088
1083
10.88
10.88
1081
1062
1093
10.93
10.98
10.81
10.57
1043
CO2 JUIMHC
% Mm
11.88
1227
1449
1429
136
11.94
10.3
10.03
1S.03
10.27
11.07
11.41
1136
11,1
10.89
10.38
8.71
9.31
9,2
9.17
944
8.42
9.52
9.77
94
8.19
898
181
888
8.M
8.81
894
1.81
146
871
8.74
8.79
89
181
198
902
• 04
9.07
808
9.01
914
907
1.71
1(9
868
(71
• 71
8.1
1.85
1.85
8
91
9.32
8.31
8.35
936
8.41
8.45
91
965
893
994
96
959
958
8.9S
8.99
8.92
8.97
1.01
9.74
WM«r
:« ictua) 1tow rate
18
18
175
175
175
17.5
17.5
17
17
18.5
16,5
19.5
16
16
15,5
15.5
15,9
19
19
15
146
14.8
149
149
14.9
14
14
14
13.5
135
135
13.5
13.1
13
13
11
12.5
12.5
12.5
12.5
12
12
12
12
11. S
115
115
11.5
11
11
11
1B.5
10.5
105
10.3
10
10
13.5
9.5
8.5
83
9
9
1
8.5
6.S
8.4
65
6
6
8
8.5
5.5
53
5
5
8pm B
68
68
6.8
68
66
88
6.8
8.8
6.8
6.8
88
6.8
68
68
6.6
68
68
68
68
61
61
61
66
68
6.6
86
68
68
66
6.8
81
61
66
66
68
68
68
68
6.6
6.6
68
68
6.8
68
68
68
68
68
6.8
6.8
6.6
6.6
(.1
81
66
66
6.8
6.8
88
6.8
68
68
68
68
6.6
68
68
68
68
66
68
68
68
6.8
6.8
68
BMtoti
luMwvil
66278
718.02
71802
682.58
71780
717.80
717.80
682.17
881,17
882,17
8(2.37
6(2.37
882.37
882.37
66237
862.37
882.37
•82.37
71757
8(973
89237
892.37
882.17
8(2.37
8(2.37
6(2.37
6(2.17
66237
•93.17
•92.17
717.80
66237
882.58
717.80
(62.58
68258
718.02
711.02
71102
71802
7H.B2
71M2
•70.18
718.02
718.02
718.25
(62.79
71125
773,50
71125
71125
711,25
7H.25
7H.25
718.2S
718.25
718.25
718.29
711.25
711.25
71847
718 25
(13.00
66300
•1300
819.80
71847
718.47
•8300
711.47
8(3.00
718.47
71147
8(3.00
718.47
T1847
Water meler
Draft Coot Wfler readng
OnfOff *
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
oir
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
cut
Off
Off
Off
Off
Off
Off
wrty.il/jll
• 18
818
818
8.18
818
818
811
918
•.1*
8 18
118
818
• 18
818
818
818
B.It
9,11
8 18
911
1,11
118
811
811
8.11
8.18
6.18
8,18
1,18
(-18
818
811
811
8.11
816
818
111
116
816
818
118
111
1.18
111
818
818
818
818
8,18
8.18
811
818
1,18
1.1*
1.18
(.18
8.18
8.18
8.18
1.18
1.19
1.18
1.18
1.18
818
1.18
819
819
818
119
1.11
816
619
8.11
1.19
119
gpm
8.7
67
6.7
67
67
67
6.7
»,7
•7
1,7
87
1.7
6.7
6.7
67
(.7
8.7
17
(.7
(.7
8.7
8.7
87
8.7
8.7
67
67
8.7
87
17
(.7
«7
8.7
6.7
6.7
87
67
1.7
87
•.7
(.7
8.7
8.7
6.7
6.7
6.7
6.7
«.?
»,7
6.7
(.7
6.7
8.7
8.7
6.7
6.7
6.7
6.7
67
6.7
8-7
8.7
(.7
87
67
«,7
67
6.7
1.7
6.7
8.7
6.7
(.7
8 7
• 7
8.7
-------
FURNfcCE A WITHOUT C*TAIYST-HISH HEAT REMOVAL RATE
02~Af]r-99
27~Jun-B5 Run TTD-2C
time stack exit dilution
see F
212*8
21328
21388
21448
21508
21568
21628
21888
21748
21808
21888
21928
21 998
22044
22104
22184
22224
22284
22344
22404
22464
22524
22584
22644
22704
22764
AVERAGE
5,45111111 testlirj
327.068867 test mki
*-4
186
167
167
167
168
168
188
188
169
168
188
168
167
168
188
165
164
164
163
163
183
183
162
162
162
184
F
88
m
M
86
88
88
88
86
85
85
85
85
85
IS
B5
85
95
85
85
85
IS
It
85
64
IS
93
water In water out
F
148
148
146
148
148
148
148
148
148
148
148
148
148
148
141
148
148
148
149
148
148
148
148
146
146
152
F
HI
161
161
181
161
161
16
16
16
18
16
16
16
181
181
181
161
161
161
181
iei
181
161
161
161
184
fire-box
F
707
705
70S
705
704
704
701
898
690
890
8*0
684
678
878
676
672
871
868
664
662
660
656
655
855
858
676
ambient
f
74
74
74
74
74
74
74
74
74
74
74
74
74
74
74
74
73
74
73
73
73
73
73
73
73
81
Hack
F
179
179
179
180
180
181
181
181
181
181
181
181
180
179
178
177
177
178
176
176
175
174
174
t74
174
176
CONgh
ppm
25487.9
25141 6
255046
25459-8
2S1383
24865,7
247684
250244
24845.4
24532.1
24149.6
24141.4
24349
24910.5
25109.9
25238
25541 2
256063
25699.9
25895.2
2*703.9
25683.2
25883.6
2S724.3
2S834.8
24186.4
COolu
epm
1«87
1957.8
19874
1968.9
19429
18103
1912.8
18J7.8
19302
1888.8
1854.8
1853
1867
WJ7.2
19463
1956.4
1984.4
1988.4
1986.3
20031
1969.J
1(85
1997.6
1990.7
19759
CO tow
PPffl
50085
50102
5007.3
50069
5008.1
50069
5008.1
50065
5009.4
5008.5
5008.5
5007.7
5009.4
50065
50081
5006.1
5007.7
5009
5009.8
5006.5
5006.9
50081
5008.1
5008.5
5008.9
O2
%
103
10.25
10.21
10-15
10.15
10.09
10.11
10,15
10.09
1019
10.28
1036
1051
10.87
10.72
10.85
10.91
10,*!
1063
10.93
10.93
10-96
1097
10.96
1098
9.7
CO2 JUM-THC
% ppm
983
991
998
1002
10.05
10.12
10 11
10.01
10.14
1004
9.17
9.68
9,7
9.54
«.S1
938
934
832
9.31
9.33
9.9
9.27
9.27
9.28
9.25
10.4
balance
In
4,5
4.5
4
4
4
3.5
3.5
3.4
3
2.5
2.5
25
2
2
1.5
1.5
1.5
1
1
08
0.5
0.5
0
0
Water
actual flow rate
gpm
66
8.8
6,8
68
66
88
8.1
6.6
68
6.8
6.8
68
6.8
6,8
6.8
68
6.8
6,8
6.8
6.8
8.8
88
68
61
8.8
6,8
Total Stu out «
Total Btu M *
EFFICIENCY (i
Ave, water*
Bumrate «
Wood moisture
Water meter
heat out
Btu/Meml
718.47
71847
71847
716.47
711,47
716,47
718.47
718.47
718.47
716,47
718.47
71147
670.57
718.47
718.47
718.47
718.47
718.47
718.47
718.47
71t,47
718.47
718,47
718.47
718,47
888.5
219.936
566,588
31.82%
6.60
5-86
2390%
Draft
On/OfT
on
Off
Of
on
on
OB
Off
on
on
on
on
on
OB
Oft
on
on
OB
on
on
on
on
on
on
on
Olf
.Bluftirout*
,Btu/brin-
gpm
drykgftr
Coelwtter
demly. IKgil
819
8.19
619
6.19
8.19
8.19
8-19
619
818
8.18
8.19
8.19
819
819
119
819
B.19
8.19
619
619
8.19
818
819
8.19
8-19
8.18
40,347
103,940
reading
OJSB1
67
6.7
6.7
87
8.7
8-7
87
87
67
87
8,7
87
87
87
67
67
8,7
8,7
6,7
87
6.7
6.7
67
8-7
6.7
-------
FURNACE A WITHOUT CATALYST-HIGH HEAT REMOVAL RATE
02-Apr-98
30-Jtrv95RinTTD-2D
•me stuck e»t dUton wttertn water oil tire-bo* antnrt stack COH(f» COdflu
sec
1464
1524
1584
1844
1704
1764
1824
1884
1944
2004
2084
2124
2184
2244
2304
2364
2424
2484
2544
2604
2664
2724
2780
2840
2900
2960
3020
3080
3140
3200
Q 3260
H 3320
g 3360
'••' 3440
3500
3560
3820
3680
3740
3600
3860
3920
3980
4040
4100
4156
4216
4278
4336
4396
4456
4516
4578
4636
4696
4756
4816
4876
4938
4996
5058
5118
5178
5236
5296
5356
5416
5476
F
171
205
194
179
169
164
181
160
160
161
159
158
15?
156
155
155
154
154
155
156
15?
158
159
159
160
160
159
158
160
162
164
165
167
168
169
170
171
172
175
176
178
178
175
175
175
174
173
173
174
174
174
174
174
175
175
171
176
176
176
176
177
177
178
178
179
179
180
160
F
94
99
89
87
86
85
85
85
84
83
83
83
83
82
S3
82
82
82
82
83
as
83
63
84
85
86
86
84
83
82
82
82
81
82
83
84
84
85
86
87
88
aa
87
85
84
84
83
83
84
84
84
85
85
85
85
85
85
85
85
86
87
87
88
87
86
86
85
85
F
138
137
137
137
138
138
13?
140
141
141
141
141
141
141
140
141
140
139
139
139
138
138
138
138
138
138
138
138
138
137
138
13?
13?
137
137
13?
13«
137
138
138
138
138
139
138
138
138
138
138
138
138
138
138
138
138
138
138
138
138
138
138
139
139
139
139
139
139
138
138
F
153
153
153
153
153
153
152
152
152
152
152
152
152
152
152
152
151
150
150
150
149
149
149
149
148
148
148
148
148
148
148
148
148
148
148
148
148
149
148
148
149
149
149
148
149
149
149
149
149
149
149
149
149
149
149
149
149
149
149
149
149
149
149
149
149
149
149
149
F
227
213
308
350
353
349
349
382
409
416
394
369
361
358
358
358
358
357
361
369
369
376
391
409
419
517
516
467
483
464
462
465
473
481
466
488
488
491
507
513
510
509
511
513
514
514
519
524
52?
533
535
543
550
554
558
562
563
564
565
566
570
573
576
578
562
567
592
59?
F
73
73
73
73
73
73
73
73
73
73
72
72
72
72
72
72
72
72
72
72
71
72
71
71
72
72
72
73
73
73
73
73
73
73
73
72
72
72
72
72
73
73
73
73
73
73
73
73
73
73
73
73
73
73
72
72
73
73
72
72
73
72
73
73
73
73
73
73
F
183
223
223
206
195
185
179
176
175
174
172
170
168
167
186
165
184
184
164
185
166
167
167
168
169
168
167
166
168
169
171
173
174
175
178
178
178
180
181
183
183
183
183
182
182
182
181
181
181
181
161
181
182
162
183
183
183
184
184
184
184
184
185
186
167
188
189
119
ppm
9816
5684
12724
2118?
20278
19804
19621
19771
21021
20888
18860
17505
18870
17082
17696
16425
18685
18632
18347
19401
19198
18750
19338
18608
17590
17155
15210
14836
18113
17379
17411
18685
21285
20939
20752
20943
22233
23507
24239
23874
23157
22880
22900
23576
24251
24593
24744
25265
25777
25977
26111
26624
27210
27686
27901
27564
27153
26819
28880
27323
27861
28145
28215
28430
28898
29338
29692
29761
ppm
1008
939
1493
1478
1355
1354
1348
1430
1485
1366
1186
1159
1145
1181
1246
1270
1274
1259
1303
1375
1255
1353
1317
1224
1177
1100
971
1103
1201
1185
1241
1483
1477
1443
1452
1549
1686
1760
1708
1645
1646
1836
1877
1717
1737
1752
1816
1870
1884
1899
1946
1997
2006
2005
2004
1979
1943
1956
2003
2008
2005
2006
2006
2005
2006
2006
2006
2008
CO low
Ppm
5011
5012.6
5011
5009.4
5011.8
5010.2
5010.2
50102
5010.2
5013
5011
5010.2
5011
5009.4
5012.2
5010.6
5010.2
5010.2
5011.4
5006.9
5009
5007.3
5011
5009
5010-6
50122
5009.8
50126
5012.2
5009.8
5011.4
$009
5012.2
5011.4
5011.4
50098
5013
5011 4
5012.6
5009.8
50106
5012.6
5011.4
50118
50122
50118
5011.4
5011.8
5010.2
5011
5011.8
50102
5010-6
5012.2
5013-4
5010.6
5010.2
5011.4
5008.5
5010.6
5009.4
5012.8
5011
5011.4
5011.4
5011.4
5010.6
5010.2
O2
1427
15.12
12.18
11.1
1129
11.63
11.48
11.4
1095
10.82
10.79
11.51
11.52
11.44
11.88
11.61
11.83
11.72
11.56
10.93
10.17
10.32
1033
1004
974
971
10,45
1204
11.91
9,75
8,03
901
6.65
8.65
854
834
8,34
8,37
8,28
7.85
7,71
8.14
8.52
8,68
8,56
8.44
8.66
8.03
9.12
9.04
9
8.96
8.88
8.71
8.48
».3
8.27
8.26
831
833
8.27
8.17
81
8.01
785
77
7.5?
7.44
CO2
554
5.24
8.17
902
8.68
8.31
842
8.61
9.1?
9.25
921
8.44
8,43
8-48
822
6.08
808
8.19
6.39
925
9.79
9.57
974
10.07
10.33
1021
893
776
884
10.74
11.02
11.07
11.34
11.54
11.72
11.9
11.89
11.83
12.23
1274
12.35
11.88
1166
1171
11.9
11.7
11,26
11.12
11.25
11.3
11.36
11.42
11.58
11.76
11.99
11.99
1193
1187
11.89
11.92
12.03
12.11
1218
1233
12.49
12.63
127?
12.81
Water
balance actual flow rale heat oil
lt»
812
80
80
60
795
795
7S.S
79
79
765
785
785
78
78
78
775
77.5
77
77
78,5
78.5
7B
76
75.5
75
75
74.5
74.5
74
74
731
73.S
73.3
73
72,5
72.5
72
71.5
71
71
70.5
70
70.4
726
72,7
88.5
68
67.5
675
8T
685
66
66
65.5
65
64.5
84.8
84
63.5
63
62.5
82
615
61
605
60
60
59.5
gpm
6.8
68
6.6
6.8
6.6
68
6,8
68
68
6,6
68
6.8
68
6.8
6.8
6.8
88
68
6,8
88
6.8
6.8
8,8
8.6
6.8
8.8
88
6.8
6.6
68
6.8
6.8
6.8
8.6
6.8
6.8
6.8
6.8
6.8
6.8
68
6.8
8.8
68
6.8
6.8
6.8
6.8
68
6.8
68
6.8
6.8
6.6
68
68
6.8
6.8
6.8
6.8
6.8
6.8
68
6.8
6.8
66
68
6.8
Btu
831.5
»87.2
887.2
887.2
6315
831.5
831.7
6648
609.2
609.2
609.2
608.2
609.2
609.2
664.8
609.2
600.4
609.8
609.6
6096
809.7
569.1
609.7
6097
554,3
554.3
554.3
554.3
554.3
609.9
5543
609.9
609.9
609.9
6099
6099
554.3
6654
554.3
5543
609.7
809?
554.2
5543
5891
609.7
609.7
609?
609.7
609.7
609.7
6097
609.7
609.7
809.7
609.7
6097
609.7
609.7
6097
554.2
554.2
554.2
554.2
S54.2
554.2
609.7
569.1
Water meter
Draft Cod water read ng
Onon density, Ib/gal
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
8.21
8.21
8.21
8.21
8.21
8.21
8.21
8.21
820
8.20
820
8.20
820
8.20
8.21
820
8.21
8.21
8.21
8.21
8.21
8.21
8.21
8.21
821
8.21
8.21
8.21
8.21
8.21
8.21
8.21
821
8.21
621
8.21
8.21
621
8.21
8.21
821
8.21
821
8.21
8.21
821
821
8.21
8.21
8.21
8.21
8.21
821
8.21
821
8.21
8.21
8.21
8.21
821
8.21
8.21
821
8.21
8.21
821
8.21
8.21
gpm
6.7
6.7
8.7
6.7
6.7
67
6.7
6.7
6.7
6.7
6.7
6.7
6.7
8.7
8.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
8.7
87
8.7
6.7
6.7
6.7
6.7
6.7
6-7
6-7
87
6-7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
8.7
6.7
6.7
6.7
6.7
6.7
6.7
8.7
6.7
8.7
6.7
6.7
6.7
6.7
6.7
8.7
6.7
6.7
8.7
8.7
6.7
8,7
6.7
6.7
6.7
-------
FURNACE A WITHOUT CATALYST-HIGH HEAT REMOVAL RATE
02-AIX--88
ttme
see
5532
5592
5652
5712
5772
5832
5892
5952
6012
6072
6132
6192
6252
6312
6372
6432
6492
6552
8612
6872
6732
6782
6852
6908
6968
7028
7088
7148
7208
7268
j 7328
{ 7388
J 7448
7508
7568
7628
7688
7748
7808
7868
7928
7988
8048
8108
8188
8228
8284
8344
8404
8464
8524
8584
8644
8704
8764
8824
8884
8844
8004
9064
9124
9184
9244
9304
9364
9424
9484
9544
slack exit
F
180
181
181
181
181
180
179
178
178
178
179
179
179
178
178
177
176
178
175
174
175
178
179
179
178
177
177
177
178
178
179
179
180
181
180
179
177
177
178
178
175
175
175
175
175
178
177
177
177
178
178
179
179
178
177
181
185
188
187
187
187
186
186
186
185
185
184
183
i water In inter aA (re-box ambient
64
84
85
85
85
85
85
85
85
85
85
86
87
88
87
86
85
84
83
83
83
83
83
84
84
85
84
85
85
86
87
88
88
87
86
84
84
83
83
82
82
83
83
84
84
85
85
85
85
86
87
87
87
86
85
85
85
84
84
83
83
64
85
85
85
85
86
85
139
138
138
139
139
139
139
139
139
139
139
139
140
140
140
140
140
138
140
140
140
139
139
139
139
140
140
140
140
140
140
140
141
140
140
140
140
140
140
140
140
140
140
140
140
140
141
141
141
141
141
142
142
141
141
142
142
142
142
142
142
143
143
143
143
143
143
143
149
149
150
150
150
150
150
150
150
ISO
150
150
150
150
150
150
150
150
150
151
150
150
150
150
150
150
151
151
151
151
151
151
151
151
151
151
152
151
151
151
151
152
151
151
151
152
152
152
152
152
152
152
152
152
152
152
153
153
153
154
154
154
154
154
155
154
155
155
r
S03
810
616
619
619
619
616
818
623
629
828
830
834
826
819
621
819
844
682
651
686
718
721
705
680
851
838
639
646
648
653
665
678
705
699
685
67S
669
678
686
685
6S6
699
697
708
719
724
722
724
746
760
763
759
753
772
832
845
83T
831
824
821
817
818
816
814
812
812
811
r
73
73
73
73
73
73
72
73
72
72
72
72
72
73
73
73
73
73
74
74
73
73
73
73
73
73
73
73
73
72
73
73
73
74
74
74
74
74
74
74
73
73
73
73
73
73
73
73
73
73
73
73
73
74
74
74
74
74
74
73
73
74
73
73
73
73
73
73
stack
F
190
190
191
191
190
189
188
187
188
186
187
187
187
186
185
185
184
184
184
183
184
188
168
189
188
188
187
187
187
188
188
188
188
189
169
189
188
187
186
186
18S
189
185
184
185
185
186
188
187
187
188
188
187
187
188
191
195
197
199
200
202
201
202
201
199
199
198
198
COHtfl
ppm
29883
30208
30233
29740
28992
28300
2T885
27275
26884
270B7
27397
27502
27250
26921
26615
26701
26*47
27303
27i1»
27291
27026
27437
28290
24630
23787
24906
25881
26595
27189
27474
27637
27677
26966
25850
24642
24316
2S029
25863
267S2
27035
28721
26721
26733
26351
26432
25708
24882
24259
24097
23645
2261S
21928
21619
21672
220*5
24089
31690
31iSO
2»967
28912
28270
25964
25891
258S3
25700
25553
25407
24963
COdlu
PPm
2005
2005
2005
2005
2005
2005
1989
1966
1997
2005
2006
1991
1970
1959
1977
1975
1987
2006
1996
1945
1999
1945
1763
1670
1738
1892
1924
1987
1997
1997
2005
1983
1889
1775
1675
1781
1843
1938
19(4.
1693
1931
1939
1885
1928
1836
1779
1734
1712
1883
1584
1561
1511
1525
1531
1637
2003
2005
2005
1925
1883
1872
1846
1858
1845
1820
1818
1775
1754
CO low
5008.1
50102
50085
50081
5011
5011.8
5009.8
50114
5008.1
S010.2
5011
5011.8
50094
5010.6
5011.8
5010.6
5011.4
5010.2
5009.8
5011
5011.4
5010.2
5008.1
5009.8
5011
5010.6
5011*
5010.2
50102
5010.6
5011.4
5012.2
5010.2
5010.2
5011
5011.4
5010.6
5011
5012.6
5009.4
5009.4
5010.2
5011.8
5009
50114
5010.2
50108
5010.2
5013
5011.8
5012.8
50094
5009
50098
5011.4
5011
5010.2
5009.4
5007.7
5011.8
5012.6
5012.2
5010.6
5010.2
5010,8
50094
5009.4
5010.8
O2
739
7.39
736
714
7.02
7.14
745
7.76
8.13
8.19
7.96
7.5
7.3
7.5
7.71
8
8.23
885
884
9.18
8-97
8,28
7.6
782
8.17
8.5
8.58
8.31
8
7.85
7.86
7.7
7.66
7.68
7.S
7.76
8.24
8.38
8-41
8.37
8.48
8.69
8.56
8.37
8.32
8.15
?.96
7.84
7.83
7.87
782
7.74
7.74
8.01
8-29
7.89
S.5T
4.72
4.96
5.18
5.26
5.34
551
5.79
6.05
6.17
634
64
CO2 JUM-THC
% ppm
12.79
12.82
13.03
13.06
12,84
12.52
12.31
11.96
1189
12 OB
12.54
12.71
1253
1232
12.06
1184
11.79
11.82
11.68
11.29
1148
12.15
1279
1257
12.22
11.84
1175
1202
12.25
12.29
12.38
1254
12.56
12.57
1275
1243
1199
1182
1178
11.83
11.72
11.56
11.68
1186
11.89
12.07
12,24
12.33
12.28
12.37
1264
12.76
12.77
12,48
12.17
12.5
1468
15.42
15.2
14.93
1478
14.63
14.44
14.18
13.91
1378
1384
13.58
Water
balance sclual flow rale
Ibt
59
58.5
585
58
57.5
57.5
57
58.5
58
58
55.5
55
54.5
54
53,5
• 53
53
52,5
52
52
51,5
51
51
50.5
SO
50
495
49
48.5
48
48
47.5
47
46.5
46
45.5
45.5
45
45
44.5
44
44
43.5
43
43
42.5
42
42
41,5
41
40.5
40.5
40
39.5
39
38.5
36.5
38
37.9
37.5
37
37
38,5
36.5
36
35.5
35.5
35
Bpm
6.8
68
6.8
68
6.8
6.8
6.8
6.8
6.8
68
6.8
6.8
68
68
68
68
68
88
8.8
68
6.8
6.8
68
6.8
88
68
6.8
6.8
6.8
6.8
6.8
68
68
68
8.8
8.8
6.6
6,8
6.8
68
68
6.8
68
6.8
68
6.8
6.8
6.8
6.8
68
6,8
68
6.8
6.8
6.8
6.8
68
68
68
68
68
68
68
68
68
88
6.8
6.8
heal out
Btu
554.2
609.7
665.2
609.6
6096
609.6
809.6
6096
809.6
809.6
609.8
609.6
554.0
S54.0
561.4
561.4
561.4
817.7
561.4
817.5
581.4
8177
576.5
617,7
6177
561.4
8175
817.5
6175
817.5
617.5
617.5
5612
6175
8175
817.5
8737
817.5
817.5
617.5
617.5
673.7
617.5
617.5
817.S
628.7
617.3
817.3
817.3
617.3
617.3
561.1
581.1
617.3
617.3
581.1
6172
817.2
817.2
«73.3
673.3
6170
617.0
617.0
873.1
8170
873.1
8T3.1
Draft
OrVOff
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
Water meter
Cod wrtar retting
ctanrtty, Wfcet
8.21
8.21
821
8.21
821
821
821
8.21
821
821
8.21
8.21
6,21
8.21
8.21
821
821
821
821
8.21
8.21
8.21
8.21
8.21
8.21
821
8.21
821
821
821
8.21
821
820
8.21
821
8-21
8.21
8.21
8.21
8.21
8.21
8.21
8.21
821
8.21
8.21
8,20
8,20
8.20
8.20
8.20
820
8,20
8.20
8.20
8-20
8-20
8,20
8-20
8,20
8.20
8.20
6.20
8.20
8,20
820
8,20
8,20
6?
6-7
6.7
6.7
6,7
67
6.7
6.7
6.7
6.7
8.7
8.7
8.7
6.7
68
68
68
• 8
8.8
6.8
6.8
6.8
6.8
68
68
68
6.8
69
6.8
6.8
68
68
68
88
68
6.8
6.8
6,8
6.8
6.8
6.8
6.8
6.8
6.8
68
6.8
6.8
8.8
6.8
8.8
8.8
6.8
6.8
6.8
8.8
6.8
88
8.8
6.8
88
6.8
6.8
68
68
68
6.8
88
8.8
-------
FURNACE A WITHOUT CATALYST-HIGH MEAT REMOVAL RATE
30-Juv95 Rm TTD-20
$tm stacked! dluMon water In water out
sec ~
9604
9660
9720
9780
9840
9900
9960
10020
10080
10140
10200
10280
10320
10380
10440
10500
10560
10820
10680
10740
10800
10860
10920
10980
11036
11098
11156
11218
11276
11336
4 11396
J 11456
J 11516
' 11576
11636
11896
11756
11816
11876
11936
11996
12056
12116
12176
12236
12296
12356
12412
12472
12532
12592
12652
12712
12772
12832
12892
12952
13012
13072
13132
13192
13252
13312
13372
13432
13492
13552
13612
r
182
182
182
181
181
182
181
181
181
182
181
182
182
181
180
179
177
177
176
175
174
174
174
173
173
173
173
173
172
172
171
170
170
169
168
188
168
185
165
164
163
163
163
163
163
163
163
164
164
165
168
166
165
184
183
182
161
162
183
162
162
161
160
1S9
158
158
159
1SO
F
85
86
85
85
85
85
86
86
85
85
85
85
85
85
85
85
85
85
85
85
85
85
85
85
85
85
88
86
85
85
84
83
83
82
82
81
81
81
82
82
63
83
83
83
83
83
84
83
84
84
84
84
84
83
84
83
83
84
84
84
84
85
85
84
82
82
81
61
f-
144
144
144
144
144
144
144
145
145
145
145
145
145
145
145
145
145
145
146
146
146
146
145
148
148
146
146
146
148
146
146
146
148
146
146
146
148
148
146
146
147
146
147
147
147
147
147
146
147
148
146
147
147
147
147
147
147
147
147
148
148
148
148
148
14S
147
147
147
F
155
155
155
155
155
156
155
156
156
156
156
156
157
157
157
157
157
157
157
158
158
157
157
157
158
158
157
158
1S8
158
158
158
158
158
158
159
158
158
158
158
159
159
159
159
159
158
158
158
158
158
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
fire-box
F
60S
808
808
806
810
813
811
808
808
802
791
785
784
778
766
759
754
753
751
751
749
747
743
738
735
734
743
747
747
744
740
750
751
743
738
730
724
717
714
716
718
719
718
720
722
727
735
738
744
770
775
767
766
763
764
764
764
767
765
777
782
783
784
781
778
778
783
779
vrttKt
f
73
73
73
73
73
73
74
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
74
74
74
74
74
74
74
74
74
74
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
74
73
74
73
74
74
75
74
75
75
75
stack
t
197
197
196
196
195
195
196
196
197
197
198
198
199
198
196
195
1W
192
181
191
191
190
189
189
188
188
188
187
186
186
186
186
187
186
186
184
183
182
181
180
179
178
177
176
178
176
176
176
176
177
179
179
178
177
175
174
174
175
178
176
174
173
172
172
172
172
173
173
CONoJi CQrtlu
ppm
24723
24658
24715
24756
24780
24125
24032
24398
24648
24471
24219
2410S
23161
22078
21057
20337
19938
19885
19474
19401
18954
18489
18054
17782
17603
17588
17712
17147
18301
15796
15654
15649
15361
14897
14844
14933
15218
15568
15772
15969
15894
16024
1*130
18252
16298
16487
1871S
16638
16203
15613
12626
12231
13831
15230
15910
16239
18524
16596
18435
16451
16663
16109
15690
15708
15983
15853
15784
15772
1751
1749
1754
1767
1690
1685
1716
1745
1725
1683
1S87
1616
1510
1437
1384
1353
1370
1328
1323
1294
1251
1236
1207
1198
1191
1211
1181
1108
1079
4085
1061
1046
1001
999
1010
1029
1050
1064
1074
1087
1076
1084
1089
1097
1100
1128
1125
1094
1095
844
796
913
1029
1072
1093
1113
1124
1114
1074
1123
1079
1049
1050
1085
1060
1047
1048
1040
CO low
ppm
50106
5010.2
5011.8
5010.2
5010.2
5010.6
501 1.S
5011.8
5010.8
5010.2
5012.2
50106
5011.4
5010.2
5008.4
5010.2
5011.4
5011
5011
5010.8
50108
5009
50118
5011.8
5009.8
50114
5009.8
5012.2
5013.8
5011
50118
50122
50118
5009.8
5011.8
5011.8
5011.8
5011
SOOS.S
5009.6
50126
50106
5012.8
5008.5
5011
5012.2
5019.8
5011
5008.5
5013
5011
5012.6
5009.8
5011.4
5013
50118
5011
5011
5013
5009.4
5011
5012.2
5011
50114
50122
5011
501 1.8
5011.8
O2
8.42
642
6.48
8.56
6.56
6,41
643
6.34
8-2
8.22
83
8.18
6.1
6.25
663
7.04
727
7.49
7.57
7.81
7.6
7.58
7.59
7.81
7.58
755
7.54
7,58
7,78
7.94
806
809
8.11
8.18
8.44
8.78
9
9.12
9.24
9.33
934
932
9.24
9.19
9.11
9.05
8.99
8.91
8.72
8.54
7.55
736
8.16
9.36
9.96
10.02
9,91
9.71
9.2
882
9.4
956
9.59
954
9.45
933
837
935
CO2 JUM-THC
% ppm
1354
13.51
1344
1337
13.36
1S.48
13.47
13,55
1365
13.59
1347
1346
13.45
133
13
12:67
12.45
12.27
12.21
12.15
12.2
12.19
12.2
12.2
12.23
12.25
12.27
1224
12.07
11.8
1181
11.75
11.73
11.62
11.43
11,11
10.8
10.78
10.7
1061
10.61
10.61
10.85
10.68
10.78
10.81
10.85
10.93
11.08
11.23
12.19
12.22
11.42
10,37
9.9
9.68
10.01
10.22
1074
109
10.27
10.07
10.03
10 OS
1013
10.21
1015
1017
balance ac&Ml Sow rale
IM
34.5
34.5
34
34
33.5
33
33
32.5
325
32
32
315
31.5
31
31
30.5
30.5
30
30
295
29.5
29.5
29
29
285
28.5
28
28
27.5
27.5
27
27
27
27
26.5
28.5
28.5
28.4
26
28
26
25.5
25.5
25.5
25
25
25
24.5
24.5
24.5
24
24
24
23.5
23,5
23.5
23
23
23
22.5
22.5
22.5
22
22
22
21.5
21.5
21,5
Spm
68
66
6.8
68
63
6.8
6.8
6.8
68
6.8
68
68
6.8
68
6.8
66
6.8
6.8
68
68
6.8
68
68
68
6.8
6.6
6.8
6.8
68
68
6.8
6.8
68
68
68
68
68
68
68
68
68
68
68
6.8
68
6.8
6.8
6.8
6.8
6.6
68
68
68
68
6.8
88
6.8
6.8
68
68
68
6.8
6.8
68
6.8
68
66
68
heat 01*
Btu
575.7
6188
616.8
816.8
618.8
872.9
618.1
•18.6
6164
618.8
616.6
6166
672.7
872.7
872.7
672.7
8727
8727
6164
672.5
672.5
6164
672.7
575.3
872.5
6725
6164
672.5
672.5
672.5
672.5
6725
672-5
672,5
672.5
728.5
672.5
872.5
672.5
672.5
672.2
728.5
672.2
672.2
672.2
672.2
827.4
872.5
872.2
672.5
728.5
672.2
872.2
6722
8722
672.2
672.2
872.2
672.2
816.0
616.0
616.0
616.0
618.0
616.0
672.2
872.2
672.2
Draft
OnOft
on
on
on
on
on
on
on
on
on
on
on
on
On
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
Coolvwler
density, to/gal
8.20
8.20
8.20
8.20
8.20
820
8.20
8.18
6,19
819
8.19
8.19
8.19
8.19
819
8.19
8.19
8.19
8.19
8.19
8.19
819
8.18
8.18
8.19
819
8.19
8.19
819
819
8.19
8.19
819
6.18
8.18
8.18
8.18
8.19
8.19
819
819
8.19
819
8.19
8.19
8.19
8.18
819
819
819
819
8.19
8.19
819
8.19
8.19
618
a 19
8.19
819
8.18
8.19
819
819
819
619
8.19
readno.
gpm
6.8
6.8
8.8
6.8
6.8
8.8
6.8
6.8
S8
6.8
6.8
6.8
68
6.8
6.8
88
6.8
8.6
8.8
6.8
68
68
68
66
6.8
68
68
6.8
6.8
6.8
68
6.8
6.8
6.8
68
6.8
68
6.8
8.8
6.8
68
88
68
68
68
68
6.6
68
6.8
88
68
88
86
6.8
8.8
88
6.8
6.8
6.8
6.6
68
68
6.6
68
6.8
66
68
68
-------
FURNACE A WITHOUT CATALYST-HIGH HEAT REMOVAL RATE
02-Apr-96
30-JUT-95 Rin TTD-2D
time stack exit dUion water in water out fire-box ambient stack CO Ugh COdlu
sec
13672
13732
13788
13848
13908
13968
14028
14088
14148
14208
14268
14328
14388
14448
14508
14568
14628
14688
14748
14808
14868
14928
14968
15048
15108
15164
15224
15284
15344
15404
Q 15464
KJ 1552<
FT 15584
15644
15704
15764
15824
15884
15944
16004
16064
16124
16164
16244
16304
16364
16424
16464
16540
16600
16660
16720
16780
16840
16900
16960
17020
17080
17140
17200
17260
17320
17380
17440
17500
17560
17620
17680
F
160
160
160
161
161
161
161
161
162
161
160
160
160
160
160
161
161
161
161
161
161
161
160
160
160
160
161
161
161
161
159
159
158
157
157
156
155
155
155
155
155
155
155
155
155
155
156
156
155
155
154
153
153
153
153
153
153
153
153
153
153
154
153
154
154
154
154
155
F
81
80
80
80
80
80
81
82
82
83
82
83
83
83
83
63
82
62
61
80
80
60
61
82
82
62
82
82
63
63
83
83
62
61
61
80
60
79
79
80
61
62
82
83
84
64
65
84
84
82
82
81
81
80
79
79
79
79
79
80
81
81
82
82
82
83
83
83
F
147
147
147
147
147
147
147
147
147
147
147
147
147
147
148
148
147
147
147
147
147
147
147
148
148
148
148
147
148
148
148
146
148
148
148
148
146
146
148
146
146
146
148
148
146
146
146
146
148
146
148
146
147
147
147
147
147
147
147
147
147
147
147
147
147
147
147
147
F
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
160
160
159
160
160
159
159
160
160
160
160
159
160
160
160
160
160
160
160
160
160
160
160
160
160
160
160
160
160
159
160
160
160
160
160
160
160
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
F
775
772
767
766
765
762
753
748
743
738
740
739
738
739
739
740
740
742
744
745
745
749
748
748
753
755
749
756
767
763
749
744
737
732
724
718
714
714
720
721
722
722
724
724
728
728
727
727
725
716
692
667
666
669
693
696
695
697
697
696
695
694
694
694
696
700
702
704
F
74
74
74
74
74
74
74
74
74
74
74
73
73
73
74
73
74
73
74
74
73
73
74
73
73
73
73
73
73
73
74
74
73
74
74
74
74
74
74
73
73
73
73
73
74
74
74
74
75
75
75
75
75
75
75
74
74
74
74
74
73
74
73
74
73
73
74
73
F
174
174
175
175
176
176
177
177
176
177
176
176
176
176
176
176
176
177
177
178
177
177
178
178
178
178
178
177
178
177
176
175
174
173
172
171
171
170
170
170
170
170
170
170
170
170
170
170
169
169
169
169
168
166
166
166
168
168
168
166
168
168
168
166
168
169
168
169
ppm
15698
15776
15938
15759
15373
15190
15106
15064
15141
15125
15137
15129
15165
15271
15295
15173
15055
15064
15198
15287
15474
16056
15995
15666
15426
15230
15002
14860
14657
14526
14303
13945
13745
13766
13692
14236
14543
14722
14925
14856
15035
15194
15230
15328
15487
15503
15361
15340
15466
15613
15568
15434
15597
15751
15930
15951
15820
15767
15768
15861
1 5845
15544
15633
15833
16024
16223
16435
16650
ppm
1051
1064
1055
1021
1012
1008
1006
1008
1007
1011
1007
1013
1020
1019
1016
999
1002
1012
1021
1024
1070
1072
1039
1027
1010
1009
965
966
964
954
926
913
908
917
934
961
967
990
978
991
1006
1010
1013
1028
1033
1026
1017
1026
1025
1028
1011
1025
1039
1052
1054
1041
1037
1046
1047
1049
1030
1029
1049
1063
1069
1086
1100
1110
CO low
ppm
5011
5011.8
5010.6
5011
5013
50122
5011
5011.4
5011
5011
50126
50114
50098
5011
5013
50118
50118
50106
50094
5012.2
5013
5009
50106
5012.6
50102
50102
50114
50118
50114
50102
50106
5011
5011 4
50102
50118
50102
50122
5006.5
50114
5009.8
50106
5010.2
50116
50116
50126
5011
5011
5009.4
5011.6
5013
50102
50122
50138
50116
50106
50102
50102
50102
50085
50102
50106
5011.8
50102
5011.4
50106
5011.4
50114
5009.6
O2
937
937
93
9.11
895
897
901
8.96
897
897
901
915
927
939
931
9.18
904
693
662
677
871
892
892
887
885
894
896
899
9.1
939
967
993
10.14
10.22
10.31
1046
10.5
1042
10.35
10.33
10.31
10.25
10.26
10.24
10.2
1018
1017
1016
1014
10.18
10.26
10.34
1035
10.29
1024
1024
1025
1026
1021
1017
1012
1016
1017
1016
1016
1009
1005
997
Water
CO2 JUM-THC balance actual flow rale heal out
% ppm
1016
1021
1031
1052
10.7
1071
1068
1072
10.71
1071
1066
1059
1061
10.51
106
1067
1075
1083
1093
1096
1103
1081
1082
1087
1087
106
1076
1074
10.64
103
997
978
964
956
949
936
933
939
945
948
947
95
95
951
952
952
951
951
947
941
931
923
921
919
92
923
926
928
9.31
936
943
939
936
943
944
951
956
961
Ibs gpm
21.5 68
21
21
21
21
205
205
20.5
205
20.5
20
20
20
195
195
195
19
19
19
19
185
185
185
185
18
16
16
18
17.5
17.5
17.5
17.5
17
17
17
17
17
165
165
165
165
165
16
16
16
15.5
15.5
15.5
15
15
15
15
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.1
14
14
14
135
135
135
13.5
13
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
66
68
66
68
68
68
68
68
68
68
68
68
68
68
68
68
68
66
68
68
88
66
68
66
68
68
66
68
68
68
68
68
66
68
68
68
68
68
68
68
68
68
68
68
68
68
Blu
6722
627.4
672.2
6722
672.2
6722
6722
6722
672.2
672.2
672.2
672.2
6722
6722
6160
6160
7263
7283
6722
7283
7283
6722
6722
6720
627.2
672.0
6720
6722
6720
6720
6720
6720
6720
6720
6720
6720
6720
672.0
6720
6720
672.0
6720
6720
6720
672.0
6160
672.0
6272
672.0
672.0
6720
672.0
7283
6722
6722
6722
6722
6722
6722
6722
672.2
6722
6722
6722
6722
6722
6722
6722
Water meter
Draft Cool water readng
OrVOff density. Ib/gal gpm
on 819 68
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
oft
off
off
off
off
off
off
oft
oft
oft
off
off
oft
oft
oft
oft
oft
oft
oft
off
off
off
off
off
off
oft
oft
oft
off
off
oft
oft
off
oft
oft
oft
oft
oft
oft
off
oft
oft
oft
oft
off
oft
off
8.19
819
819
819
819
819
819
819
8.19
819
819
819
819
8.19
8.19
819
8.19
819
619
819
8.19
819
819
819
8.19
619
6.19
819
8.19
819
819
8.19
6.19
619
619
819
819
819
819
819
819
819
819
8.19
819
619
6.19
819
619
819
819
819
619
619
619
819
819
819
819
819
819
819
819
8.19
819
819
819
68
68
68
68
6.8
68
68
68
6.8
66
68
66
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
66
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
68
66
66
68
68
68
68
68
68
68
68
68
68
68
68
68
-------
FURNACE A WITHOUT CATAIYST-HK3H H6AT REMOVAL RATE
02-Apr-98
ju-A-n-33 mji i i u~£u
time stacks* dUion watwln urateroU flre-bojr wnfcfert stw* COMffi COoHu
sec
17740
17800
17860
17916
17976
18036
18096
18156
18216
18276
18336
18396
18456
18516
18576
18838
18698
18756
18816
18876
18936
18996
19056
19116
19178
19236
19292
19352
19412
19472
Q 19532
X 19592
•fT 19652
"^ 19712
19772
19832
19892
19952
20012
20072
20132
20192
20252
20312
20372
20432
20492
20552
20612
20668
20728
20788
20848
20908
20868
21028
21088
21148
21208
21268
21328
21386
21448
21508
21588
21628
21S88
21748
F
155
155
155
155
158
156
158
157
157
158
156
155
155
155
1S4
154
154
154
154
154
155
154
154
155
155
155
155
155
154
155
155
155
155
155
155
155
154
155
154
154
154
154
153
1S3
154
153
153
153
153
153
153
153
153
154
153
«53
1S3
153
154
154
153
153
153
153
153
153
153
153
F
83
83
83
83
83
83
83
82
81
81
81
80
81
80
80
80
80
80
80
80
80
80
80
80
80
80
SO
80
80
79
80
79
79
79
79
81
81
82
82
82
82
82
82
81
80
80
79
79
79
81
81
82
82
82
82
82
82
82
82
81
80
79
79
79
79
79
81
81
F
147
147
147
147
147
147
148
147
148
14?
147
147
147
147
148
148
147
14S
148
147
146
147
148
147
147
147
147
147
147
147
147
147
147
147
147
147
14?
147
147
147
147
147
147
147
147
147
147
147
147
147
147
147
147
147
147
147
147
147
147
147
147
147
147
14?
147
147
147
147
F
159
159
159
159
159
169
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
160
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
158
159
159
f
708
711
714
715
717
721
718
716
708
692
676
666
666
865
868
865
885
888
868
684
664
667
666
866
668
885
683
660
858
857
654
654
653
651
648
851
858
660
882
662
661
660
659
896
658
858
857
658
658
859
658
657
859
681
660
851
648
84$
640
638
638
838
635
833
832
631
828
624
F
73
73
73
74
73
73
73
74
74
74
74
74
74
74
74
74
74
74
74
74
75
74
74
74
74
75
74
75
74
74
74
74
74
74
74
74
74
74
74
74
74
74
74
74
73
74
74
74
73
73
73
73
73
73
73
73
73
73
74
74
74
73
74
74
74
73
73
74
f
189
189 .
169
169
170
170
170
171
172
172
171
171
171
170
170
170
171
171
170
171
171
171
171
172
172
171
171
171
172
172
172
172
172
172
171
171
171
171
170
170
170
170
169
169
169
189
169
169
169
169
169
169
189
169
189
169
189
168
169
188
168
168
169
189
180
189
169
169 .
ppm
18748
16825
17009
18874
16675
16687
16834
16382
15824
15841
16419
18968
17432
17660
17700
17734
17741
17806
18030
17835
17782
18294
18266
18262
18543
1«758
1879S
18713
18S81
18840
19185
19002
18986
19165
19194
1S734
18278
17888
17200
17009
16952
16911
16870
16854
18773
18675
16260
16248
16138
15885
15873
15930
15987
15898
15540
15413
15711
15558
15389
15206
14941
14616
1451«
14380
14266
14282
14018
13788
pprfi
1111
1127
1130
1096
1121
1106
1098
1056
1029
1009
1094
1159
1153
1165
1163
1185
1187
1184
1178
1164
1183
1202
1199
1207
1226
1233
1227
1229
1222
1259
1249
1242
1251
1262
1245
1191
1196
1126
1118
1114
1112
1110
1105
1103
1093
1072
1983
1065
1044
1043
1043
1047
1046
1030
1008
1030
1028
1013
1000
882
963
954
943
936
938
930
905
905
CO tow
opm
50102
50106
50085
5011
5010.2
5010.2
5011.8
5010.2
5012.2
5011.4
50098
50106
50102
5012.2
50103
50114
5011.4
5010.8
50098
5011
5009.8
50114
5011.4
5011.8
5011
50122
5010.2
50114
5011
5010.8
5013
50096
50098
5013
5011.4
5011
5009.4
5010.2
5010.8
5013.4
50098
50118
5011.4
5011.8
5011.8
5011.4
5011.4
5011.8
5011.4
5011
5010.2
5009
50134
5011
5009.8
501 1.»
5011
5911
5009.8
5011.4
5013
5009
5009.8
3013
5011.8
5012.S
5010.8
50118
02
9.9
985
982
977
972
8.83
9.5
8.3t
8.35
9.48
978
885
10.03
10.08
10XJ4
10
8.99
10.04
989
898
993
982
882
8.84
9.84
9.77
9.79
9.81
9.95
9.88
988
9.9
992
999
9.98
9.98
10.04
10.01
10.03
1004
1003
1004
10.02
998
998
9.98
8.34
9.93
993
9.81
9.88
988
982
961
9.83
986
10.02
10.14
10.12
10.08
10.08
1013
10.14
10.13
10.16
10.1
10.16
10.26
Wain
CO2 JUM-THC Mmce idual How rale heMoU
% ppm
968
9.75
98
9.85
9.93
10.01
10.12
10.19
10.24
10.08
9.8
962
9.55
9.52
9.53
8.81
9*1
9.59
9.81
9.63
9.65
972
9.74
9.71
9.71
9, 76
9.73
972
9.73
9.8
9,77
9.72
9,7
9,81
9.82
9.59
9.54
9.58
9.56
9.53
9.51
9.5
9.48
9.51
9.5
9.47
9.5
95
9.51
853
9.55
9.58
963
962
9.62
9.8
9.44
8.34
9.37
942
9.43
9.4
9.39
9.41
9.4
9.44
9.38
9.28
Ibs
13
13
13
12.5
12.5
12.5
12
12
12
12
12
11.5
11.5
11.5
11.2
• 11
11
11
11
11
105
105
105
105
10.4
10
10
10
10
10
8.5
95
95
f.S
8.5
9.5
9
9
9
9
9
85
8.S
8,5
8.5
8.5
85
8
8
8
8
8
t
7.5
7.5
7.5
7.5
7.5
7.2
7
7
7
7
7
7
7
85
8.5
gpm
68
66
66
68
6.8
6.8
6.8
8.8
6.8
68
68
68
6.8
68
6.8
6.8
6.8
8,8
68
68
68
6.8
6.8
6.8
6.8
8.8
68
6.8
6.8
6.8
68
6.8
68
68
8.8
6.8
6.8
68
68
68
68
68
68
68
6.8
6.8
6.8
6.8
68
68
6.8
68
68
6.8
6.8
6-8
8-8
68
6.8
68
68
6.8
68
6.8
6.8
68
8.8
68
BkJ
872.2
672.2
627.4
672.2
172.2
•72.2
818.0
872.2
618.0
872.2
672.2
672.2
672.2
872.2
•16,0
818.0
872.2
816.0
•18,0
872.2
616.0
672.2
8160
672.2
872.2
•27.4
728.3
872.2
672.2
8722
672.2
6722
672.2
B72.2
672.2
872,2
872.2
872.2
8722
672.2
672.2
6722
872.2
672.2
872.2
872.2
872.2
872.2
627.4
672.2
672.2
672.2
672.2
8722
•72.2
872.2
872.2
872.2
872.2
672.2
672.2
672.2
672.2
8722
§722
•72.2
872.2
6722
Water meter
Draft CooJ vmter resdng
OnOff density. Ib/gol gpm
off 8.19 88
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
oft
off
off
off
off
818
8.18
8 19
8.18
819
8.19
8.19
8.18
8.19
8.19
819
819
818
8.18
8.19
819
8.19
8.19
8.19
8.19
8.19
8,19
8.19
8.19
8.19
8.19
8.19
8.18
818
819
819
819
8.19
8.19
8.18
8.19
8.19
8.19
8.19
819
819
8.19
8,19
8.19
8.19
8.18
8.19
8.19
8.19
8,19
8,19
8,19
8.19
8.19
8.19
8.18
8.19
8,19
8,19
8,19
8,19
8.19
8.19
819
819
819
8.19
68
68
3,8
8.8
88
88
6.8
68
6,8
6.8
68
6.8
8.8
8.8
8.8
8.8
8,8
88
8.8
68
68
6.8
E.8
6.8
68
6.8
68
68
8.9
6.8
68
8,8
68
8.8
68
6,8
8.8
6.8
s.a
6.8
68
8.8
6.8
6.8
8-8
6.8
8.8
8.8
68
68
86
6.8
8,8
8.8
8.8
8.8
6.8
68
68
68
8.8
8.8
6.8
68
88
8.8
88
-------
FURNACE A WITHOUT CATALYST-HIGH HEAT REMOVAL RATE
02-Apr-96
30-Ju>95RuiTTD-2D „,„,, u
Sme stach e*t
sec
21608
21868
21928
21988
22044
22104
22164
22224
22284
22344
22404
22464
22524
22584
22644
22704
22764
22824
22884
22944
23004
23064
23124
23184
23244
23304
23364
23420
23480
23540
O 23600
K, 23680
Pr 23720
23780
23840
23900
23960
24020
24080
24140
24200
24260
24320
24380
24440
24500
24560
24620
24680
24740
24796
24858
24916
24976
25038
25096
25158
25216
25276
25336
25398
25456
25516
25576
25636
25696
25756
25816
F
153
154
153
153
153
153
153
153
153
153
153
152
152
153
152
152
153
152
152
152
152
152
151
151
151
151
151
151
151
151
151
151
151
150
150
150
150
150
150
150
150
150
150
150
150
150
ISO
150
150
150
150
150
150
150
150
150
150
150
150
151
150
150
149
150
149
149
149
149
dUtcn
f
82
82
82
82
82
82
81
80
80
79
79
79
80
81
82
82
82
82
82
82
82
81
80
80
79
79
80
81
81
81
82
82
82
82
82
82
82
82
81
80
79
79
79
79
80
81
81
81
81
81
82
62
62
82
82
82
81
80
79
79
79
79
80
81
81
81
82
82
water in water oU
F
147
147
147
147
147
147
147
147
147
14?
147
147
14?
147
147
14?
147
147
147
147
147
147
146
147
146
146
146
146
148
146
148
148
146
146
146
146
146
146
146
146
146
146
146
146
146
146
146
146
146
146
146
146
146
146
146
146
145
146
146
145
145
145
146
146
146
145
145
146
F
159
159
158
159
159
159
159
159
159
159
159
159
159
159
158
158
159
158
159
159
158
158
159
158
158
158
158
156
158
158
158
156
158
156
158
156
158
158
156
158
156
158
156
158
158
156
157
158
158
158
158
158
157
15?
15?
158
157
15?
157
157
157
157
15?
157
157
157
157
15?
flre-box
F
622
620
619
620
618
616
617
616
618
815
613
612
611
611
609
608
604
601
602
600
599
599
596
598
598
598
599
598
597
594
592
591
590
590
589
587
584
583
581
580
580
577
576
57S
572
572
574
574
574
573
573
574
575
578
560
581
593
604
606
600
598
593
589
588
586
586
580
578
an* in
F
74
73
73
73
74
74
74
73
74
73
74
74
73
73
73
73
73
74
73
74
74
73
74
74
74
74
73
73
73
73
73
73
73
73
73
73
73
73
74
73
74
73
73
73
74
73
73
73
73
73
73
73
73
73
73
74
73
74
74
73
73
73
73
73
73
73
73
73
•tack COtltfi COdlu
f
169
189
169
169
169
168
168
168
188
168
168
188
188
168
167
187
167
187
18?
167
167
167
186
166
168
168
166
168
188
186
165
185
165
185
185
184
184
164
164
184
164
164
164
164
184
164
184
184
164
184
164
163
164
184
184
164
164
184
163
164
183
163
163
163
163
183
163
163
ppm
13770
13709
13550
13591
13562
13635
13806
13847
14022
14176
14193
13953
13810
13798
13684
13745
13749
13908
13997
13940
14022
14002
14067
14132
13875
13753
13578
13473
13477
13391
13261
1307$
12842
12842
12498
12333
12223
1220?
12231
12154
12052
11951
11906
11930
11943
11873
11612
11849
12130
12329
12370
12333
12069
11S47
11894
11890
11882
12028
11983
11865
11845
11731
11890
11605
11585
11503
11487
11731
ppm
907
893
899
892
898
911
906
919
928
933
923
904
909
902
905
908
909
924
015
922
922
917
930
912
90S
892
885
885
S84
872
861
847
832
824
81S
802
802
801
797
788
781
775
780
781
783
775
773
791
811
812
814
795
782
780
779
779
785
786
778
772
785
786
758
782
756
750
757
779
CO low
PPm
5013
50118
5013.8
5011.4
5010.6
5010.2
5011 4
S0128
5011.4
5012,8
5011,4
5011,8
5011.8
5011.8
5011.4
5011
5009
5012.6
5011 4
5011.4
5011
5011
5010.2
5011.4
§012,2
5010.6
5010.2
5009.4
5010.8
5011 4
5012.6
5011.4
5011
5011.4
5011.4
5010.8
5012.6
5011-8
§011.4
5011
5010.2
5012.8
5010.2
5011.8
5009
50096
5011.4
5009.8
§008.5
§011.8
§013
5011.4
5011.4
5011.4
5012.6
50106
5008,1
5013
5011.4
§011.4
§009.8
5013
§011.8
5010.8
5011.8
5011.8
5010.8
5011,4
O2
%
10.26
10.28
1033
10.34
10.34
1038
10.37
1036
10.36
10.4
10.48
10.81
10.86
10.69
10.72
10.73
10.73
10.73
1069
10.69
10.66
1088
11.08
11.23
11.31
11.33
11.31
11,3
112S
11.26
11.33
11.4
11.43
114
11.44
1146
11.44
11.39
11.34
11.29
1128
11.27
11.29
11.38
11.44
11.41
11.32
11.28
11.25
11.2
11.17
11.16
11.12
11.3
11.41
11.4
11.33
113
11.35
11.41
11.42
1152
11.54
1153
11.51
1154
11.51
11. S4
CO2 JUM-THC
% ppm
9.3
9.27
924
9,23
9.23
917
9.18
9.19
8.1?
913
8.06
894
8.9
8.86
883
882
881
6.62
885
883
888
891
881
867
858
8.57
659
8.57
8.54
6.53
846
8.39
8.35
8.35
8.38
8.39
8.42
8.44
6.46
8.49
8.5
8.47
8.44
834
6.29
8.31
8.38
8.44
8.45
6.46
847
8.49
8.52
8.54
6.58
8.61
8.68
8.68
858
8.47
8.44
836
8.33
8.32
8.32
8.3
8.33
8.3
balance adual Sow rate
Ibs
6.5
8.5
8.5
6.5
6
6
6
8
8
6
6
5.7
55
5.5
5.5
. 5.5
5.5
5.5
5
5
5
5
5
49
4.5
45
4.5
4.5
4.5
4,5
4.5
4.5
4
4
4
4
4
4
4
3,5
35
3.5
3.5
3.5
35
3.5
33
3,2
3
3
3
3
3
3
2.9
2.5
25
2.5
2.5
2.5
2.5
2.5
2.5
2.5
2
2
2
2
opm
6.8
6.8
68
68
68
88
68
68
6.8
6.8
6.8
68
E.8
6.8
68
68
6.8
6.8
68
68
88
6.8
68
88
88
88
6.8
6.8
6.8
6.8
68
6.8
6.8
68
6.8
8.8
68
8.8
6.8
68
6.8
6.8
68
6.8
68
6.6
68
88
6.8
6.8
68
6.6
6.6
68
6.8
6.8
68
6.8
68
6.8
8.8
6.6
6.8
6.8
6.8
6.8
6.8
6.8
heatou
Blu
672.2
8722
672.2
627.4
872.2
672.2
672.2
6722
672.2
672.2
672.2
672.2
872.2
672.2
672-2
872.2
872.2
672.2
672.2
672.2
672.2
863.4
718.9
863.4
8636
718.9
6194
663.6
663.8
663.6
663.6
683.6
883.6
883.6
883.6
663.6
663.6
663-6
6636
663.6
883.6
863.6
6636
6636
663.6
663.6
608.3
663.6
6636
6194
863-6
663.6
608.3
808.3
608.3
863.6
6638
808-3
6083
883.8
683.8
663.8
608.3
6083
608.3
683.8
8638
608.3
Draft
OrtOff
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
oft
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
Cool water
density, IWW
8.19
8.19
819
8.19
8,19
8.19
8.19
8 19
8.19
8.19
8.19
8.19
819
8.19
8.19
8.19
8 19
819
819
6.19
8.18
8.19
8.19
8.19
8.19
8.18
819
8.19
8.19
8.18
8.19
8.19
8.19
8.19
8.19
8.19
8.19
8.19
8.19
819
819
819
8.19
8.19
819
8.19
8.19
8.19
819
8.19
8.19
8.19
8.19
8.19
819
8.19
«-19
819
819
8.19
8.19
819
8.19
819
8.19
8.19
8.19
tator motor
rearing
opm
6.8
6.8
6-8
68
6.8
6.8
68
68
8.6
68
6.8
88
68
6.8
8.8
88
68
66
68
68
6.8
6.7
6.7
6.7
8.7
8.7
67
8.7
8.7
6.7
6.7
6.7
67
6.7
8.7
6.7
6.7
6.7
87
87
8.7
6.7
67
6.7
6.7
6.7
8.7
87
6.7
8-7
8,7
6.7
6.7
8.7
6.7
6.7
67
8.7
6.7
6?
6.7
6.7
6.7
8.7
6.7
6.7
6.7
6.7
-------
FURNACE A WITHOUT CATALYST-HIGH HEAT REMOVAL HATE
02-AJT-96
30-JurvS5Ru"iTTD-2D
(me stacked dlution witerin witerotl fire-box ambiert stack CONgh COdlu
sec F
25876
25938
25998
2605S
26116
26172
26232
26292
26352
28412
26472
26532
26592
28652
26712
26772
26832
26892
26952
27012
27872
27132
27192
27252
27312
27372
27432
27492
27548
27608
[- 1 27668
KJ 27728
~f 27788
w 27848
27908
27988
AVERAGE
26444
7 3455556 les< dm
440.73333
149
149
149
149
149
149
149
149
149
149
149
149
148
148
148
148
149
149
149
149
149
149
149
148
148
147
147
147
147
146
148
146
146
146
146
162
e.hrs
F
82
82
82
82
62
82
82
82
82
82
82
82
82
82
82
82
82
82
62
81
80
79
79
79
80
80
81
81
81
82
81
81
81
81
81
83
F
146
146
145
145
145
145
145
146
145
145
145
145
145
145
145
14S
145
145
145
145
145
144
145
145
144
145
145
145
145
144
144
145
144
144
144
144
F
157
157
157
157
157
157
157
157
157
157
157
157
156
157
157
157
158
158
156
157
156
156
158
156
158
156
156
158
156
156
156
156
156
156
158
158
F
575
574
572
572
571
571
572
573
572
573
572
571
589
570
570
592
628
629
620
609
597
587
579
573
568
585
562
562
560
5S8
557
556
554
553
552
646
F
73
73
73
73
73
73
73
73
73
n
74
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
72
73
73
73
73
73
73
73
F
162
183
162
163
162
162
162
162
162
181
162
162
162
161
161
161
162
162
162
162
182
161
181
160
160
160
160
160
160
159
159
159
159
159
159
178
Ppm
11898
11796
11682
11580
11467
11405
11243
11104
10962
10885
10828
10852
10817
10954
11003
11096
10494
9025
8529
8537
3696
9013
9371
9644
9745
9831
9851
9880
9886
982?
9802
9778
974S
9860
9672
17907
ppm
775
764
759
753
746
739
727
719
712
705
70S
713
713
717
721
725
60S
545
545
548
570
596
621
821
635
638
642
842
639
639
634
632
630
626
634
CO low
Ppm
5013
5011.4
5013.4
5010.2
5011
5011.8
5010.2
5011.8
S012.2
5009.8
5012.6
5011.4
5010.6
5012.8
5013
5012.8
50114
5009.8
5010.2
5012.2
5012.2
5011.8
50095
50118
5013.4
50114
5011.8
5012.2
5011
5011
50114
50106
5011.4
5010,2
50085
O2
1159
11.57
1158
11,58
11.6
11.57
11.57
11.58
11.58
11.57
11.57
1157
1157
11.6
11.58
11.58
11,6
1155
1162
11.82
12
1213
1226
1234
1238
12,43
12.46
12.46
1249
1252
12.8
1282
1262
12.64
12.6$
955
CO2 JUM-THC balance
% ppm
825
826
822
8.21
818
821
8.2
8.21
8.19
819
821
82
822
8.19
8.2
8.22
8.24
831
818
6
7.88
776
769
7.65
764
763
7.63
7.65
7.65
7.63
7.6
758
7,59
7.58
7.56
1030
ItM
2
1.8
1.5
1.5
1.5
1.5
1.5
1.S
1.S
15
1
1
1
1
1
1
1
1
06
0.5
0.5
OS
0.5
0.5
0.5
0.5
05
0.5
05
0.5
0.5
0.5
0.3
0
0
Water Water meter
actual flow rate neat oil Draft Cool water rearing
gpm
6.8
8.8
6.8
6.8
8.8
68
6.8
6.8
8.8
6.8
68
6.8
8.8
6.8
68
8.8
88
6.8
68
66
68
68
6.8
66
6.8
6.8
6.8
6.8
6.6
6.8
6.8
6.8
68
8.8
6.8
681
Total Btu out =
Total Btu in *
Efficiency*
WMerflownte
Burrate =
Btu OrVOff detnMy,lb/gal gpm
608.3 off 8.19 8.7
608.3 off
663-8 off
663.8 off
619.6 off
6638 off
6838 off
606.3 off
663.8 off
683.8 off
6636 off
6636 off
608.5 off
683.8 off
683,8 off
663.8 off
608.5 off
608.5 off
608.5 off
663.6 off
6085 off
864.0 off
608.5 off
6085 off
6640 off
6085 off
6065 off
567.9 off
608.5 off
6640 off
6640 off
608.5 off
664.0 off
664.0 off
664.0 off
646.4
286,354 BtUhr
536.436 BtutT
53.38%
6,81 gpm
4.11 dry((fl*r
819
8.19
8.19
819
819
819
819
8.18
819
8.19
819
619
8.19
8.19
8.19
619
6.19
819
8.19
819
8.20
8.19
8.19
820
8,18
8.19
8.19
8.19
6.20
820
8.19
8.20
8.20
8.20
820
38.983
73.029
6.7
8.7
6.7
8.7
87
8.7
8,7
8,7
8.7
6.7
8.7
6.7
8.7
8.7
6.7
6.7
6.7
8.7
8.7
87
8.7
8.7
8.7
6.7
8.7
6.7
6.7
67
87
8.7
8.7
8.7
8.7
8.7
Wood moisture
-------
FURNftCE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE
02-Aur-M
28-JW-8S Run TTD-1A
time slack exit <*M!on water in water out fire-box ambient ttacti
sec
2780
2840
2800
2980
3020
3080
3140
3200
3260
3320
3380
3440
3800
3560
3620
3680
3740
3800
3860
3820
3980
4040
4100
4158
4218
4278
4338
4396
4486
4816
4576
4838
rt 4686
KJ 4758
-0 <«"»
4876
4838
4896
5056
5118
5178
5236
5288
5358
5418
5476
5532
5592
5852
5712
5772
5832
5882
5952
6012
8072
8132
6182
8252
6312
6372
6432
6492
8552
8812
8872
8732
6782
6852
6908
6888
7028
F
161
151
144
141
138
136
136
135
135
134
134
134
134
136
137
136
138
139
141
141
142
144
144
144
144
144
146
148
151
154
155
157
158
159
161
182
162
163
163
163
164
164
185
16«
166
166
166
166
188
167
168
168
188
170
175
180
182
183
184
185
187
188
188
180
183
196
199
199
200
200
198
187
F
89
83
81
60
80
79
78
76
78
77
77
77
78
78
79
80
80
81
81
81
81
60
79
79
79
79
81
82
83
83
83
84
84
84
83
83
83
82
82
83
83
84
85
85
85
84
83
83
83
83
83
84
85
86
88
89
89
89
89
88
88
88
88
88
88
88
80
91
91
81
90
90
F
144
144
144
144
144
144
143
143
143
143
143
143
143
142
143
143
142
143
143
143
143
143
142
143
142
142
142
142
142
142
143
142
143
143
142
142
142
142
142
142
143
143
143
143
143
143
142
143
143
143
143
143
143
143
143
144
144
144
145
144
145
145
145
148
148
146
146
147
147
148
148
148
F
150
150
150
150
150
150
150
150
150
150
148
149
149
148
149
148
149
148
148
149
149
148
148
148
148
14»
148
148
148
148
148
148
148
148
148
148
148
14f
148
148
148
149
149
148
148
148
149
149
148
149
149
149
150
149
150
150
150
150
151
151
151
151
152
152
152
152
153
154
154
154
144
155
f
323
302
305
307
321
327
333
337
342
342
338
348
348
348
363
358
356
360
362
368
364
390
384
368
388
388
402
431
448
455
456
460
467
476
494
496
498
505
510
515
517
520
522
524
529
532
534
538
536
534
536
541
546
54?
567
583
590
594
584
802
614
622
628
655
887
70S
720
727
741
742
737
738
F
78
78
78
76
76
76
75
75
75
75
74
74
74
74
74
75
74
74
75
75
75
75
75
74
74
74
74
74
75
75
75
75
76
76
76
76
75
75
75
75
75
75
75
75
78
76
75
75
75
75
75
74
74
75
74
75
75
75
75
75
75
76
75
75
75
75
74
75
75
75
75
78
F
186
174
187
182
159
157
156
155
154
154
153
153
154
154
155
156
158
157
157
158
159
160
160
180
160
160
182
165
188
170
171
173
174
176
177
178
178
179
179
180
181
181
161
182
182
183
183
183
184
184
184
184
185
186
192
197
200
202
203
205
206
208
209
211
214
218
220
223
223
223
2M
220
COMtfi
ppm
9308
8482
10980
11633
11608
11587
11332
11251
11222
11188
1M42
10817
11003
11580
11446
10618
10895
11397
11593
11536
11235
11589
11523
11332
11332
11385
12529
17049
17704
18083
18886
19460
18682
19786
19818
19421
18092
18771
20402
20544
20573
20488
20284
20097
1996?
18190
18840
19157
20056
20308
20333
20SS3
20927
21041
23645
25773
25627
25061
24872
26384
27718
28345
28846
28718
29108
33581
33689
32007
31112
30082
29224
28898
COdtl
ppm
1175.8
681.3
840,5
8218
8363
818.7
790,0
7863
7878
7808
7635
7706
766,!
822.8
824.8
7461
778.5
815.3
821.5
822.8
8102
8312
831.5
811.4
8115
813.8
868.3
1281 9
13278
13384
14088
1444.9
1473.5
1480.3
15094
14632
14290
14883
1544.8
15583
1557.5
15630
15417
15248
1528.0
1471.4
1412.8
1433.8
15202
1551.8
1558.9
1578.3
1601.8
16165
1828.5
2005.0
2005.4
2005.0
2001.1
2005.2
2009.0
20054
2005.0
2004.6
2004.9
2004.4
2004.6
2006.0
20062
20041
2005.7
2005.0
CO low
ppm
5008.8
5011.4
5011.4
5011.4
5012.2
5013
5010.2
5013
5011.4
5008.5
5009.8
5012.2
5011.8
5011.4
5011
5010.6
5012.6
5013
5011.8
5013.4
5009.8
5008
5011
5011
5008.5
5011.6
5011
5011.8
5012.2
50098
5011.8
5011
50096
5009.4
5011
5010.6
5011
5009,8
5007.7
5010.6
5011.4
5010.6
50098
5010,8
5012.8
5011
5011.6
5010.2
5009.4
5011
5011,4
5008.1
5008.8
5010.6
5011.4
5010.2
50102
5010.8
5010.2
5011
5013
50122
50128
5010.2
50085
50108
5011.8
50094
5010,6
5008.5
50094
S012.8
O2
%
14.81
1776
1811
15.83
15.34
15.24
15.22
152
1511
15.06
1508
15.04
14.97
14.71
1454
14.49
14.39
14.28
14.22
1424
1402
13.45
1368
13.81
14.08
14.1
13.79
12.74
12,68
12.51
12.45
12.38
12.27
12.22
12.12
12.03
12.16
12.09
11.17
11.84
11.81
11.8
11.8
11.77
11.77
11.92
11,81
11.75
11.58
11.57
11.56
11.8
11.41
11.38
10.08
8.44
833
8.46
8.5
831
8,03
7.88
7.89
7.83
758
805
5.58
5.56
5,59
548
6
8.46
OO2 JUM-THC
% ppm
4.9
2.87
4.34
4.77
4.83
5.02
5.04
5.09
5.17
5.22
521
522
5.S3
559
576
5.83
5.82
6.08
8.1
6.06
8.39
6.91
8.58
6.37
9.22
6,2
6.64
7.84
80?
8.28
8.31
6,38
8.47
654
8.67
8.74
8.38
865
8.87
8.82
8.84
8.84
884
885
8.85
8.88
8.82
8.85
808
909
8.1
8.17
8.25
8.28
10.77
12.18
12.18
1188
11.88
12.15
12.41
12.5
1282
12.87
1306
14.46
15.1
15.09
15,08
15.14
14.57
14.13
Water
balance actual flow rate
be
80.8
80.5
80.5
80.3
80
80
80
80
79.8
78.5
79.5
795
79.5
79
79
79
78.5
78.5
78
78
78
77.5
77.8
77,5
77.4
77
77
765
78
78
75.5
75
74.5
74.5
74
74
735
73.4
73
725
72
72
71.5
71
70.5
70.5
70
697
69.5
69
89
88.5
68
87.5
87
865
86
85.5
65
64.5
64
635
63
82.5
82
81.5
61
60.5
80
584
58.5
58
8.3
6,3
83
6,3
6,3
8.3
6.3
8,3
6.3
6,3
8.3
8.3
8.3
6.3
8,3
8.3
6,3
8.3
8.3
6.3
83
6,3
8,3
6.3
6,3
8.3
8.3
63
6.3
8.3
6.3
8,3
8,3
6.3
63
8.3
63
63
63
63
63
63
83
8.3
8.3
6.3
8.3
63
6.3
83
6.3
63
6,3
9.3
6.3
6.3
6.3
83
8.3
6,3
6.3
6.3
63
8.3
6.3
6.3
83
6,3
63
8,3
8,3
8,3
heat out
hi/Interval
30968
30988
308.38
309.88
308.89
309.88
361.83
361.63
361.63
361.83
309.97
309.87
309.97
381.74
309.87
30997
381.74
309.97
309.97
308.97
30997
30997
33783
308,97
381.74
381 74
381.74
361.74
361-74
361-74
309.87
361.74
30997
30997
361.74
361.74
361.74
361.74
361 74
361.74
308.87
30997
30897
309.87
308.97
289.31
36174
30897
30997
308.97
308.8?
309.97
381.83
309,97
361 63
309.68
308.88
309.88
308.79
381.53
30979
308.79
381.42
381.42
308.69
309.89
381,31
381.20
337.12
309.50
309.50
361.08
Draft
On/Off
-------
FURNACE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE
02-Af».96
28- Jur»-95 RunTTD-1A
time stack extt dlutlon water In wj
see " "~ "
7088
o
to
oo
7148
7208
7208
7328
7368
7448
750B
7568
7628
7MB
7748
7808
7868
7928
7088
8048
8108
8168
8228
8284
8344
8404
8464
8824
SS84
a«44
8704
8764
8B24
8884
8844
9004
8084
0124
8184
8244
8304
8384
8424
8484
8544
MD4
9660
8720
97SO
8840
9900
0960
10020
10080
10140
10200
10280
10320
10380
1044O
10500
10560
10820
10880
10740
10(00
10880
10820
10B80
11036
11098
11158
11218
11278
1133«
r
198
198
186
196
195
195
196
198
197
197
198
198
200
200
201
200
200
200
199
199
198
199
199
199
199
198
198
191
187
197
198
195
194
194
183
192
191
191
1*2
199
193
194
195
1«8
197
197
197
198
198
194
193
192
192
192
193
184
194
194
195
184
194
193
190
190
190
190
189
189
189
191
192
192
r
90
89
88
88
as
87
87
as
88
89
89
89
89
89
88
88
87
87
87
8«
88
89
90
90
90
89
89
88
87
as
88
86
85
85
86
86
87
87
88
•7
88
87
87
86
86
86
85
86
86
87
87
87
87
86
86
85
85
M
84
85
as
86
86
86
87
87
87
86
85
85
84
84
r
148
148
149
149
149
148
149
149
150
150
150
151
151
152
152
152
152
152
152
153
153
153
154
154
154
153
1S7
1S8
157
157
157
157
158
158
158
158
156
158
159
'58
160
160
160
100
161
161
161
161
162
162
162
182
163
163
163
163
164
163
164
164
164
165
165
166
166
166
166
167
167
167
167
168
llerout tit-bat ambient stick CQtt#i
P
155
155
1S8
158
158
158
158
157
1S7
1i7
158
158
158
158
158
158
159
180
180
181
1(1
181
181
181
182
182
182
163
183
133
163
183
164
164
184
184
185
165
185
18S
186
188
168
187
167
187
187
187
168
188
188
186
189
188
189
170
170
170
171
171
171
171
172
172
172
173
171
173
173
174
174
174
F-
737
742
7SO
7S8
781
788
774
784
786
793
801
812
819
820
821
818
819
819
114
808
SOS
»11
813
819
825
828
828
831
835
835
839
830
805
791
787
783
783
784
785
788
788
788
781
814
828
832
835
830
822
818
812
806
802
805
813
823
829
834
837
838
834
832
833
838
833
825
819
822
829
835
841
845
t-
76
78
76
76
75
75
78
74
74
75
75
75
75
75
75
75
75
7S
74
74
7S
7»
7S
76
70
7»
76
78
76
75
75
75
75
74
74
74
74
75
75
75
78
79
75
75
75
78
75
74
7S
75
75
75
76
75
75
75
75
75
75
74
74
74
7«
74
75
75
75
78
76
75
7S
75
F
219
219
219
218
218
218
211
218
218
220
221
222
224
225
225
225
225
224
224
224
225
22$
226
226
226
228
225
225
223
222
221
221
220
219
219
219
218
220
221
222
223
224
224
226
226
226
226
226
228
22S
224
223
223
223
223
224
224
224
225
225
225
224
223
222
222
221
221
221
222
223
223
226
ppm
28764
28880
21888
2M74
28S88
28341
28373
28556
28008
28888
29411
29346
28557
29915
29875
28490
29130
29069
29297
29952
31112
32039
32442
32320
3H27
31282
30900
30477
30892
30225
29736
29358
28298
27319
27928
29134
30017
30290
30782
31417
31565
32178
32528
33289
38731
369T5
35832
34080
32951
32157
31490
31079
30268
29574
26577
28556
28642
28048
27344
26151
26530
26160
2S509
24918
24093
23181
22660
23413
25842
27372
28235
28361
CO dig
d»
2005.4
20057
20054
2005.7
2004.9
2004.4
2008.2
2005.7
20055
20054
2004.7
2006.0
2005.0
20054
2005.4
2004.6
2004.7
2005.0
2005.0
2004.7
2005.4
2005.2
2005.2
2005.7
70052
2005.2
2005.4
2004.7
2005.4
2005.0
2005.9
20054
2005.7
20055
2005.2
2005.0
2005.4
2004.6
2005.4
20D5.7
20054
2005.7
2004.8
2004.7
2004.6
2004.7
2006.0
2005.0
2004.8
2004.9
2005.0
20050
2005.0
2004.7
20052
20080
2004.7
2005.2
2008.2
2004.2
2005.4
2004.8
2005.2
1886.7
1909.5
1812.0
1756J
1769.4
1886,8
2005.7
20054
2004.8
CO tow
ppm
80122
5009.8
5010.2
5010.2
son
50073
5011.4
5012.2
5010.0
5011
50114
5010.2
50094
5011
5012.2
50102
5011.4
5011.4
5010.6
5011
5010.2
5011
5010-6
5010.2
5010.6
5008.4
5013
50098
5008.4
5009.8
5011
5007.7
5010.2
50102
5011
50106
5010,2
5008 S
5010.6
50098
50094
5010.8
5010.2
5010.2
5009*
9009
5011
5010.2
5010.2
5011.4
5011.8
5011.8
5008
5011
5010.2
50081
5011.4
5011.8
5011. 6
5009.4
5008.6
5011.4
8011
5011.4
5010.2
son. a
5011. a
5010.2
50098
5011.4
5013
5010.6
O2
%
8.82
7.05
7.05
7
7.15
723
7.07
681
664
848
612
5.77
536
5.11
523
549
5.8
5.78
5.77
5.79
5.76
5.58
541
5.37
553
5.58
5.59
566
802
634
846
657
686
688
8.88
8.55
841
8.17
5.82
5.84
545
538
528
5.18
4.99
494
5
508
533
5.57
5.72
582
5.78
5.72
5.54
526
5.2
523
522
52
5.29
5.44
5.54
5.64
5.75
5.6
5.77
571
5.48
5.18
4.99
4.75
CO2 JUM-THC
% ppm
13.78
1356
13.56
13.S5
1342
13.32
13.41
13.7
1385
13.98
1435
14.89
1509
15.27
1508
1479
1451
14.52
14.48
14.45
1445
14.63
14.75
14.77
14.84
14.59
1451
14.37
13.92
13.8
13.46
13.33
13.1
1312
13.31
13.41
1354
13.75
14.08
14.2
14.38
14.45
1482
14.81
14.89
14.67
14.62
14.5S
14.32
14.11
1398
13.83
1389
13.97
14,19
14,4
14.43
1442
14.45
14.51
14.55
14.4
14.29
14.18
14.05
14,02
1403
1408
14.18
1432
14.47
147
Wlter
balance acftya! flow rate
fee
57.5
57
56.5
56
56
55.5
55
545
54
53.5
53
525
51.9
51,5
51
50.5
50
485
49
48.5
48
47.5
47
465
46
465
45
45
44.5
44
43.5
435
43
43
42.5
42
41,5
41
40.5
40
38.5
39.5
39
38.5
38
37.5
37.S
37
36.5
36.5
38
J5.5
35
345
345
34
34
33.5
335
33
32.5
325
32
31.5
31.3
31
30.5
30.5
30
30
28.5
29
heat out
ym Bluflntervai
8.3 30841
6.3
8.3
M
6.3
0.3
6.3
6.3
6.3
63
6.3
6.3
63
63
6,3
6.3
8.3
8,3
8.3
8.3
8.3
83
8.3
63
63
63
8.3
83
8.3
6.3
6.3
63
83
83
63
63
83
63
8.3
8.3
8,3
6.3
83
8.3
83
8.3
8,3
8,3
6.3
8.3
03
63
8.3
63
83
63
6.3
0.3
6.3
8.3
6.3
8.3
6.3
83
63
6.3
63
6.3
63
83
83
63
309.41
36097
36097
36097
360.97
38097
41254
360.86
380.88
412.41
360.75
38075
30811
360.83
380.83
38083
412.15
412.15
34455
412,02
412.02
360.40
360.40
411.89
48352
287.18
257.09
308.81
30861
308.81
308.81
309.51
308,81
308.51
308.51
30841
308.41
30841
30841
308.30
308.30
287.75
359,88
308.20
308,20
30820
30820
308.10
308,10
30810
308.10
30789
30799
307.89
358,32
307.88
359,32
358.20
35920
359.20
307.78
359.07
307.87
307.87
33502
358.95
30758
30758
35882
35862
307.45
Draft
Water meter
Cod water readng
On/Off dually, Ugi\
On 818
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
8.18
8.18
8.18
8.18
8.18
81«
818
818
818
8.18
818
818
818
818
818
818
8.18
8.16
817
8.17
8.17
8.17
817
817
8.17
8.16
a 16
8.16
6.16
816
8.16
816
8.16
816
816
816
816
616
8.16
8.16
816
8.10
8.18
8.15
8.15
8.15
815
8.15
815
8.15
8.15
8.15
8.15
8.15
815
814
8.15
814
814
8.14
8.14
8.14
8.14
8.14
8.14
8.14
8.14
8.14
8.14
814
8.13
flpffi
6.2
8.2
8.2
62
8.2
8.2
«.Z
6.2
6.2
6.2
6.2
8.2
62
6.2
6.2
8.2
6.2
8,2
6.2
62
6.2
6.2
6,2
8.2
82
8.2
8.2
62
82
62
8.2
62
62
6.2
32
62
8.2
62
6.2
6.2
8.2
6,2
6.2
8.2
6,2
8.2
8.2
8.2
8.2
6.2
8,2
6.2
82
8.2
8.2
8.2
62
82
8.2
6.2
6.2
8.2
62
6,2
8.2
82
8.2
6.2
6.2
82
6.2
62
-------
FURNACE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE
02-A«r-96
28-Jun-es
time sti
sec
11396
11458
11516
11578
11638
11888
11756
11816
11878
11838
11888
12058
12118
12176
12236
12298
12358
12412
12472
12532
12592
12652
12712
12772
12832
12802
12852
13012
13072
13132
13182
13252
Q 13312
Kj 13372
tX 13432
13482
13652
13812
13672
13732
13788
13848
13908
13868
14028
14088
14148
14208
14288
1432B
14388
14448
14508
14588
14828
14886
14748
14808
14688
14928
14888
15048
15108
15184
15224
15284
16344
15404
15464
15524
15584
15844
Run TTD-1A
ickexll Ellueion water In water oul fire-box ambient
f
193
183
180
174
158
151
148
142
138
137
135
133
131
130
128
127
125
124
123
122
122
121
119
118
117
118
116
115
115
113
113
112
111
111
110
110
110
108
108
108
108
toe
107
106
105
105
104
103
104
103
102
102
102
102
102
102
101
101
101
100
100
99
88
80
89
89
88
98
88
98
98
88
F
84
85
84
80
79
79
78
78
77
76
75
75
75
75
75
76
76
77
77
78
78
78
77
76
75
75
74
74
73
74
75
78
76
77
77
77
78
77
77
78
77
78
75
75
74
74
73
74
74
75
78
76
77
77
78
78
77
78
76
75
75
74
75
75
78
78
76
78
76
77
77
77
F
168
168
188
169
169
189
169
169
169
169
188
168
188
188
169
189
189
189
168
189
188
168
168
188
188
168
167
187
187
186
187
188
188
188
166
188
186
166
188
166
168
188
186
165
188
186
185
16S
165
185
185
185
16S
165
165
185
185
18S
164
164
164
164
184
184
184
164
183
183
164
183
183
183
F
175
175
175
178
175
175
176
176
175
178
175
178
175
176
175
175
176
175
176
175
175
175
174
174
174
174
174
173
174
173
173
173
173
173
173
173
172
173
173
172
172
172
172
172
172
172
172
172
172
171
171
171
171
171
171
171
171
171
171
170
170
170
170
170
170
170
170
170
188
170
189
170
f
S46
845
827
751
892
654
824
600
581
SOB
552
540
528
518
508
488
492
4S6
478
472
488
460
455
450
446
442
438
434
431
428
428
422
419
418
413
410
407
405
402
388
387
395
383
392
380
388
388
385
384
382
380
378
377
378
373
372
370
388
387
386
365
364
384
382
381
360
358
358
358
354
353
352
F
75
74
75
74
75
75
75
75
75
75
75
75
75
74
74
74
74
74
74
75
75
75
75
75
75
75
75
75
74
74
74
74
74
74
75
75
71
75
75
78
78
78
76
76
76
75
75
74
74
74
74
74
74
75
75
75
75
75
76
75
75
75
75
74
74
74
75
75
75
75
75
78
slack
F
227
227
226
211
184
181
172
165
160
156
152
148
147
144
141
140
138
136
135
134
132
132
131
130
128
128
127
126
125
125
124
123
122
122
121
120
120
118
119
118
118
118
117
117
118
118
116
115
114
114
113
113
113
113
112
112
112
112
112
111
111
111
110
110
110
110
109
110
110
109
too
109
CONjfi
ppirt
28060
27230
25387
22335
37272
45150
41732
38487
32483
28764
25675
23572
21838
20113
18880
17753
18728
15772
15084
14618
14022
13717
13348
13159
13082
12854
12602
12388
12179
12038
11841
11825
11828
11719
11540
11361
11178
11007
10771
10818
10437
10266
10180
10124
10009
8888
9745
8554
9526
9607
9803
9644
9676
9758
9705
9741
9737
8713
•878
8581
8570
9534
8530
8652
8810
8806
8884
9866
8904
10002
9981
9865
COcHu
ppra
2005.2
20049
18841
1178.8
8188
11252
1003.9
8382
7007
597.5
511.1
460.1
4118
377.8
342.0
309.7
282.8
280.1
2389
228.4
217.8
207.5
200.2
1932
192.2
W1.4
185.4
184.4
180.0
1771
172.7
180.5
155.4
156.1
1520
145.5
143.7
137.2
135.7
132*
130.7
127.1
122.8
121.3
1188
121.1
120.B
118,0
118.5
111.8
111.2
1107
107.1
108,1
1066
1053
1078
106.8
108.0
110.2
1112
108.2
108.1
100.8
101.7
104.7
103.0
104.5
998
1008
693
103.7
CO tow
ffiM
50102
5008.4
5010.2
50081
5011
5010.8
5011.8
5013
50118
5011.4
5012.2
5011
50114
50106
5012.2
50088
5011.8
5010.2
5012.2
5011.4
5012.2
5011.4
5011.4
5011
50114
5008.5
5011 8
5011.8
5012.2
5013
5012.2
S012.2
5011 8
5010.2
5011 4
5012.2
5011
5013
5011.4
50098
5011
50106
50098
5011
5008
5010.8
5013
5011.4
5012.6
5011
80108
5011.4
5010.2
5011.8
5010.6
5011.4
5011.4
5011
50134
5012.2
5012.2
50098
50122
5010,2
5011.8
5008.1
5010.2
50122
5011.4
5012.2
5010,2
5011,4
O2
4.62
46
4.78
588
807
8.88
9.51
969
893
1003
10.09
10.12
10.2
1029
10.38
10.43
10,38
10-42
10-37
10,32
10.37
10.35
10.44
10.48
10.44
10.48
10.57
10.82
10.83
10.88
10.72
10.85
10,51
10.48
10.52
10.54
10.55
10.55
10.88
10-57
10.58
10.59
10.55
10.91
10,48
10.54
10.6
10.75
10.77
10.87
10.65
10.83
10.56
10.48
1051
10.43
10.4
10.34
10,38
10.5
10.58
10.61
10.88
10.81
10.48
10.39
1044
10.43
1041
10.29
10.35
10.34
CO2
14.83
14,86
1478
13.58
11 96
11.85
11.28
10.97
1088
1088
10.51
10.34
1013
9.92
873
8,59
9.51
8.37
9.33
8.28
9,2
8.18
9.04
888
9.01
893
8.85
8.79
8.74
8.7
6.85
8.88
8.79
8.8
874
8.71
8.86
885
8.81
8.81
8.57
8.54
8.5«
882
8.82
858
8.S3
8.42
8.42
8.49
8.53
855
8.81
868
8.65
8.7
8.7
8.88
888
8.87
8,54
8.5
8.49
8.58
8.87
8.78
8.72
8.74
877
8.88
8.82
8.85
balance
t»
28
285
28.5
282
28
28
28
28
28
27.7
27.5
27.5
27.5
26
28
27,5
27.5
27.5
27.5
275
27.5
27
27
27
27
27
27
27.5
275
272
27.2
27
27
27
27
27
27
27
27
27
265
27
26.8
27
27
27
27
27
27
27
27
27
27
26.5
26.5
265
26.5
285
26.5
26.5
285
265
27
268
285
28.5
26.5
28.5
285
285
28.5
265
Water
actual flow rate
gpm
8.3
6.3
6.3
8.3
8.3
8.3
6.3
6.3
8.3
6.3
83
83
8.3
63
63
8.3
8.3
83
83
6.3
63
8.3
8.3
8.3
8.3
6.3
8.3
63
63
63
6.3
8.3
6.3
6.3
6.3
6.3
63
6.3
8.3
63
83
6.3
6.3
8.3
83
8.3
8.3
6.3
83
8.3
8.3
6.3
6.3
83
6.3
6.3
63
6.3
8.2
6.2
82
62
62
62
82
82
8.2
62
62
6.2
82
8.2
Water meter
Herat out
BtuMerval
35869
358.69
358.88
358.57
307.34
30734
35857
358.57
30734
358.57
30734
358.57
35869
40994
307.34
30734
33466
307.34
307.34
307.34
358.69
35869
30745
307.45
30745
307.45
358,82
30756
358,82
358.95
307.58
358.95
358.95
358.95
358.95
358.95
307.67
35885
35895
287.18
307.87
30767
307.87
35807
307.87
359.07
35807
359.07
359.07
307.78
30778
307.78
307.78
307.78
307.78
30778
30778
30778
35407
30349
303.48
303.49
283.25
303.49
303.48
303.48
354.19
354.19
25281
354 18
303.59
35418
Draft
On/Off
On
On
Off
Of!
Off
Off
Off
Off
Off
Off
Off
OB
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
on
Off
Off
OB
Off
OR
OB
OB
Off
OB
Off
Off
OB
OB
OB
OB
Off
OB
Off
Off
Off
OB
Off
OB
Off
Off
Off
OB
Off
OB
Off
Off
Off
OR
Off
Off
Off
Off
Off
Off
Off
Off
Codwiter
density, fgal
813
a 13
813
8.13
8.13
8.13
8,13
813
813
813
8.13
8.13
8.13
8.13
8.13
813
8.13
8.13
8.13
813
8.13
8.13
8.13
8.13
8.13
8.13
814
8.14
814
6.14
8.14
8.14
8.14
8.14
814
8.14
8.14
8.14
814
8.14
814
814
8.14
8.14
8.14
814
8.14
614
8.14
814
8.14
814
8.14
8.14
8.14
8.14
814
814
8.14
8.14
8.14
8.14
814
814
8.14
8.14
8.15
815
814
8.15
8.15
8.15
reacfrtg
Opm
6,2
8.2
8.2
8.2
82
8.2
8.2
8.2
6.2
8.2
82
8.2
8.2
8.2
6,2
6.2
8.2
8,2
8.2
8.2
82
8.2
62
82
82
82
8.2
6.2
8.2
82
82
8.2
8.2
6.2
6.2
62
8.2
82
82
8.2
8.2
82
62
82
82
8.2
8.2
6.2
8.2
8,2
8.2
82
8.2
6.2
8.2
6.2
8.2
82
6.1
6.1
8.1
61
81
8.1
6.1
81
8.1
6.1
61
8.1
6.1
8.1
-------
FURNACE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE
02-Apr-M
2S-Jun-95 RunTTD-1A
lime stick exit dkllon water in water out fire-box ambient stick COhidl
sec
15704
15784
15824
158S4
15944
16004
16064
16124
16184
16244
16304
16364
16424
16484
16540
16600
16660
16720
16780
16840
16900
16960
17020
17080
17140
17200
17260
17320
17380
17440
17500
I— I 1756°
O 17620
L>J 17680
O 1774°
17800
17860
17916
17976
18038
18096
18156
18216
18276
18336
18396
18456
16516
18576
18636
18696
18756
18816
18876
18936
18996
19056
19116
19176
19236
19292
19352
19412
19472
19532
19592
19652
19712
19772
19832
19892
19952
r
98
97
97
97
96
96
96
96
96
96
96
96
96
96
96
95
95
95
94
94
94
94
94
94
94
94
94
94
94
94
94
94
93
93
93
93
93
93
95
102
107
113
117
120
123
125
126
129
131
132
134
135
137
139
141
142
145
147
148
149
151
151
152
153
153
153
153
155
157
160
161
162
r
76
75
74
74
75
75
75
75
76
77
76
77
77
76
75
74
73
74
75
75
76
77
76
77
77
76
77
77
77
75
74
74
74
74
75
76
76
76
77
79
78
78
77
77
77
78
79
80
79
80
81
81
81
81
82
82
82
81
80
80
79
80
80
81
81
82
83
83
82
82
82
81
h
163
163
162
162
163
162
162
162
162
162
162
162
162
162
162
161
162
161
161
161
161
161
161
161
161
161
161
161
160
160
160
160
160
160
160
160
160
159
159
160
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
159
100
160
160
160
160
160
160
161
161
161
161
161
162
162
162
162
F
169
169
169
169
169
169
169
168
168
168
168
168
168
168
168
168
168
168
168
167
167
167
167
167
167
167
166
166
167
166
166
166
166
166
166
166
166
166
165
185
165
185
165
165
165
165
165
165
165
165
165
165
165
165
165
165
166
165
166
166
166
167
167
167
167
168
167
168
168
168
168
168
F
353
355
355
354
353
350
348
347
346
344
342
341
339
337
337
336
336
335
333
332
331
329
327
325
324
322
320
320
320
320
319
320
319
317
317
316
315
314
313
317
337
371
406
437
464
484
500
516
535
552
566
580
593
605
617
635
648
655
661
666
671
676
678
681
679
677
678
879
680
679
880
684
F
76
75
75
75
75
75
75
75
75
75
75
75
75
76
75
75
75
74
74
74
74
74
74
75
75
75
75
75
75
75
75
75
74
74
74
75
75
75
75
75
75
75
75
74
74
74
74
74
74
74
75
75
75
75
75
76
76
76
75
75
75
74
74
74
74
74
75
75
75
75
75
75
F
109
109
109
108
108
107
107
107
107
107
107
107
107
107
107
107
106
106
108
106
106
106
106
106
106
106
106
106
106
105
105
105
105
104
105
105
105
105
106
115
124
131
136
141
145
148
151
153
155
157
160
162
164
167
169
171
173
174
175
176
177
177
179
180
181
181
182
183
185
186
187
186
ppm
9957
9880
9717
9790
9847
10030
10152
10254
10319
10494
10571
10641
10845
10628
10478
10449
10555
10470
10S55
10759
10921
11007
11084
11214
11243
11340
11405
11414
11316
11247
11320
11344
11324
11483
11658
11804
11829
11959
12032
11491
8004
9296
11153
12390
13359
13782
12850
12862
13261
13814
14225
14966
15304
15731
16069
16272
1S092
14628
14990
15226
15393
15332
15511
15686
15877
16069
16309
16459
16419
15780
15361
15230
COdkl
DOT)
107.9
1100
1051
1071
101 1
102.2
1021
1051
985
101.4
977
1038
1030
1068
1081
103.4
1099
111.3
1012
1004
1040
1043
101 9
1024
1029
103.2
1053
1090
1095
1089
1076
116.2
1144
1063
106.4
1130
1086
1102
131.5
705.1
516.0
6712
8006
883.0
950.2
9806
898.0
899.7
9235
964.8
9904
1048.2
1076.8
1108.9
11336
1153.0
1122.2
10340
1062.7
10926
1104.5
1100.7
1114.4
11304
11390
1151.7
1167.6
11803
11969
1161 1
1117.5
1116.5
CO low
ppm
5011
5011 4
5011
50126
50114
50114
5011
50134
50094
5013
50122
50114
5011 4
50102
50094
50122
50122
5011
50106
50134
50094
50126
50102
5012.2
5013
5009
5013
5011
50106
50106
50114
50126
50106
5010.2
50114
5009.4
5011.4
5013.8
5011.4
5010.6
5011
5011.8
50106
5010.2
50106
5011.4
5013
5011
5010.2
5009.8
5012.2
5011.4
5011.8
5011
50106
5011
5011.4
50122
5009.8
50094
5010.2
5011
5011
5010.2
5010.2
50114
5011
5011
50118
5011
50098
50102
O2
%
1036
10.43
1057
1058
10.65
1057
10.52
10.45
1048
1038
1033
103
1034
1038
1049
1064
1059
108
10.83
10.7
1064
1065
1066
1058
1058
1054
1054
1056
10.68
1079
10.76
108
1091
1067
1078
10.73
1075
1069
1069
10.95
1462
15.32
14.81
1428
1381
1336
13.23
1303
1276
1246
122
1188
11.55
11.23
1092
10.76
10.48
1037
10.42
10.41
1043
1039
10.26
1017
1008
1019
1012
999
995
971
971
965
C02
%
6.84
8.79
8.67
8.66
8.61
8.68
8.72
8.76
674
682
8 86
8.89
885
681
8.68
66
867
854
654
863
868
867
888
874
873
876
876
876
865
856
8.6
857
649
856
863
668
867
8.72
873
8.47
555
523
574
625
667
709
721
7.4
7.64
79
813
644
872
8.99
9.28
941
969
976
969
9.71
971
9.79
99
999
1008
995
1001
1009
1013
10.34
1033
10.41
balance
to
265
265
265
265
265
265
265
265
265
265
265
265
265
265
265
265
265
265
265
265
265
265
26
26
26
26
26
26
26
26
26
26
265
265
26
26
26
26
26
26
26
26
26
26
26
255
255
255
25
25
25
25
25
245
24.5
24.5
24
24
24
24
24
24
235
23.5
23.5
23
23
229
225
225
225
222
Wlter
actual flow rate
flpm
62
62
62
62
62
62
6.2
62
62
62
62
62
62
62
62
82
62
62
62
62
82
62
62
62
62
62
62
62
62
62
62
62
62
62
82
62
6.2
62
62
62
62
62
82
62
62
62
62
82
82
62
62
82
82
62
6.2
62
82
62
62
62
62
62
62
62
62
82
62
62
62
62
62
82
Water meter
heat out
Btu/interval
30359
30359
35431
35431
30359
354.31
354.31
30370
303.70
30370
30370
30370
30370
28345
30370
35443
30370
35443
35443
30380
30380
30380
30380
30380
30380
30380
25317
25317
35455
30390
30390
30390
303.90
30390
30390
30390
28364
35467
30400
25325
30400
30400
30400
30400
30400
30400
30400
30400
30400
30400
30400
30400
30400
304.00
30400
30400
303.90
25325
30390
28364
30390
35455
35455
30380
30380
35443
30380
35443
30370
30370
30370
30370
Dralt
Onion
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
on
on
on
on
on
on
on
on
on
on
on
on
Off
Off
Off
on
on
on
on
on
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
Cool water
density, tvgal
815
815
815
815
815
815
815
815
815
815
815
815
815
815
815
815
815
815
815
8.15
815
815
815
815
815
815
815
815
616
818
618
816
818
8.16
816
816
8.18
816
816
8.16
818
816
816
816
816
616
816
816
8.16
816
816
816
818
816
816
816
816
816
8.16
818
818
818
818
815
815
815
615
815
815
815
815
815
readng
opm
8.1
61
61
81
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
6.1
61
61
61
6.1
81
61
61
61
61
61
61
61
61
61
81
61
81
6.1
61
61
61
61
61
61
61
81
61
6.1
61
61
61
6.1
61
81
61
61
81
61
61
-------
FURNACE A WITHOUT CATAIYST-IOW HEAT REMOVAL RATE
28-Jun-9S Hun TTD-1A
time stack exit dtutton water In water out fire-box ambient stack CO hitfi
sec
20012
20072
20132
20192
20252
20312
20372
20432
20492
20552
20812
20868
20728
20788
20848
20908
20968
21028
21088
21148
21208
21268
21328
21388
21448
21508
21568
21628
21688
21748
21808
_^ 21888
3 21928
*J 21988
_i 22044
22104
22164
22224
22284
22344
22404
22464
22524
22884
22644
22704
22764
22824
22884
22944
23004
23064
23124
23184
23244
23304
23364
23420
23480
23540
23600
23660
23720
23780
23840
23900
23960
24020
24080
24140
24200
24260
F
163
183
163
162
182
162
161
161
160
161
161
181
161
161
158
158
188
157
155
155
154
154
153
154
154
154
154
154
154
154
155
155
155
155
155
154
154
154
153
183
152
152
1S2
152
182
152
152
152
152
152
153
182
153
153
154
154
154
155
154
154
154
153
153
152
153
151
141
131
124
120
118
114
F
80
80
80
81
82
82
82
82
82
82
83
82
82
81
80
79
79
80
80
81
81
81
81
81
81
82
82
82
82
82
81
80
78
79
79
79
79
80
80
80
81
81
81
81
81
81
81
82
82
82
82
82
82
81
80
79
79
78
80
80
81
. 81
81
81
81
81
78
77
76
75
74
73
F
162
162
163
163
163
163
164
163
164
164
164
164
164
164
164
164
164
164
164
165
164
165
165
165
165
185
165
165
168
165
165
166
165
165
165
165
166
1(6
166
166
186
186
186
166
166
167
187
167
167
187
187
187
167
188
168
187
188
188
168
168
188
188
188
188
169
188
169
168
188
169
188
168
F
188
169
169
189
169
188
170
170
170
170
170
170
171
170
171
171
171
171
171
171
171
171
171
171
172
171
171
172
172
172
172
172
172
172
172
172
172
172
172
173
173
173
173
173
173
173
173
173
174
174
173
174
174
174
174
174
174
175
175
175
175
175
175
175
175
175
175
175
175
175
175
175
F
886
891
691
691
688
884
881
880
879
882
878
683
887
887
675
661
651
64S
641
637
635
83S
635
838
840
640
640
837
638
636
632
632
830
632
632
633
832
832
632
634
635
835
634
834
633
633
635
632
833
633
633
632
833
633
633
630
629
827
624
621
619
617
817
618
615
620
818
885
558
532
513
498
F
75
74
74
74
75
75
75
7$
75
75
75
78
75
75
75
74
74
74
74
74
74
74
74
74
74
74
74
75
75
78
75
75
75
74
74
74
74
74
74
74
74
74
74
78
75
78
75
75
78
75
78
76
78
76
78
75
75
74
74
74
74
74
75
78
75
78
75
75
78
75
75
73
F
188
189
189
189
189
188
188
188
188
189
189
189
189
189
188
187
146
184
184
183
182
181
181
181
181
181
181
182
182
182
182
182
162
182
182
182
182
182
182
182
183
183
182
183
183
183
184
184
184
163
183
184
184
184
183
183
182
182
182
182
182
183
183
184
184
184
174
181
152
144
138
134
ppm
15238
14685
14437
15039
18056
16842
17171
17346
17588
17668
17525
17114
17310
17167
16724
17277
17753
18075
18624
18595
18778
18697
18832
18665
18608
18453
18241
18038
18132
18034
17891
17753
17639
17517
17480
17334
17147
16938
16768
16881
16541
18380
16158
16052
15995
15780
15558
18328
15202
151 12
15047
14893
14811
14714
14624
14528
14558
14861
14783
14768
14746
14683
14832
14608
14624
14657
13852
14290
2012S
22387
22.115
21088
COdki
ppm
1110.0
1100.4
10342
1055.7
1131.7
11878
1228.8
1243.2
1267.8
12699
1277.2
1248.4
1252.3
12505
12081
1235.0
1266.4
13018
13302
13325
1353.0
1334.8
1328.3
13353
13296
13182
1300.8
1287.9
12941
12879
1280.4
1277.3
1268.8
12607
12531
1248.4
1231.8
1213.1
11982
1183.9
1175.0
11732
1157.1
11470
1138.5
1128.3
1108.9
1093.8
10B71
10802
10781
1070.1
1061.4
1085.5
10460
10423
1043.9
1082.1
1059.2
10584
1053.1
1048.6
1047.4
1047.7
10426
10430
7656
220.8
293.5
333.7
329.3
323.4
CO low
ppm
8011.4
5012.8
5011
5011.4
5012.2
8011
5011.4
5011-8
5010.6
5011.8
5008.1
5011
5011.8
5010.6
5010.6
SOU
8010.2
5009.8
5011.4
5009.8
5010.6
5009.8
8010,2
5011
5011.4
5011 4
5010.6
S012.2
8010.2
8010.2
5012.2
5011.8
5011,4
50098
8010.6
5012.6
8012.6
8011.4
5011.4
5010.6
5012.2
5011.4
5009.4
5010.6
8011.8
5010.2
8011.8
50098
50118
5013
5011,8
5010.2
8010.2
8009.8
5011.4
5012.6
8012.2
50106
5012.2
5011
8010.2
50122
5010.2
8012.6
50098
8013.4
8011.8
50106
S011.8
5013
5012.2
8013.8
02
^
9.65
9.58
9.48
9.7
9.97
10.06
10.18
10.23
1034
10.28
10.23
10.4
10.28
10.18
10.77
11.11
11.35
11.33
11.37
11.46
114
11.42
11.38
11.26
11.16
11.08
11.06
11.08
11.06
1122
1123
11.32
11.29
11.25
11,17
11.13
11.09
11.07
1103
11.02
11.06
11.07
11.08
1102
1102
11.02
11.01
11.01
11-05
1108
11-07
11.06
11.04
11.02
1103
11.05
11.09
11.08
11.12
11.18
11.16
11.17
11.17
11.2
11.19
11.24
11.72
12.18
103
8.57
9.53
9.84
CO2 JUM-THC
% ppm
10.42
10.58
10.86
104
10.13
10
8.9
9.84
9.77
98
9.86
8.87
9.83
9.83
922
8.95
8.74
S8
8.71
862
888
8.63
882
8.7
8.77
8.81
8.81
8.8
8.75
878
878
867
8.68
8.67
8.7
874
8-74
8.75
878
8.75
874
8.73
8.72
8.78
879
8.8
8.8
8.81
876
8.75
8.75
8.77
8.79
8.81
881
8.77
6.75
8.78
8.73
8.7
869
8,69
S-69
8.66
8.67
86
809
7.88
8.44
9,96
997
9,83
Water
:0 ictual flow rate
22
22
22
215
21.5
21
21
21
20.5
20.5
20.S
20
20
20
20
20
18.5
19.S
19.5
19
19
1»
18,5
18,5
185
181
18
18
18
17,5
17.5
17.5
17.5
17.5
17.5
17.5
17
17
16.5
16.5
16.5
18.S
16
16S
16
16
18
15.8
155
15.5
15.5
15.5
15
15
15
15
15
IS
15
14,5
14.5
14.6
14.S
14
14
14
14
4
4
4
4
4
y*n E
82
8.2
82
6.2
8.2
8.2
6.2
8.2
82
62
82
i.2
6.2
8.2
6-2
e.2
82
82
8.2
6,2
62
8.2
62
6.2
6.2
62
8.2
6,2
a.2
8.2
6,2
«,2
6.2
«,2
6.2
6.2
8.2
e.2
6.2
6.2
6.2
6.2
«2
82
8.2
6.2
8,2
6-2
6.2
6.2
6.2
6.2
8.2
6.2
6.2
6.2
»,2
6.2
8,2
8.2
6.2
6.2
8,2
6,2
82
6.2
82
6,2
6,2
6.2
6.2
8.2
Iwat out
u/lntervml
303.70
354.31
303.59
303.59
30359
303.59
30348
354.19
303.49
303.49
28325
303.48
3S4.07
303.49
354.07
3S4.07
354,07
3S407
354.07
30338
3S4.d7
303.38
303.38
303.38
353.94
30338
303.38
353.94
353.84
353.84
353.94
303.28
35394
330.35
353.94
353.84
30328
303.28
303.28
35382
353.82
3S3.82
35382
353.82
353.82
303.17
303.17
303.17
353.70
353.70
303.17
353.70
353.70
303.06
303,06
353.70
282.86
3S3.S7
353.S7
353.57
353.S7
353.S7
353,57
383-57
30285
35357
302.SS
302.85
353.57
30285
353.57
353,57
Oral
On/Off *
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
on
Off
Off
on
on
Off
Water meter
Coot water reading
tally, Ugi!
8.15
8,18
8,15
8.15
8.15
8.15
8.14
8.15
814
8.14
8.14
8.14
614
814
8.14
8.14
8.14
8.14
8.14
8.14
814
814
6.14
814
8.14
8.14
814
8.14
814
8.14
8.14
8.14
8.14
8 14
8.14
814
8.14
8.14
8.14
8.14
8-14
914
8.14
8.14
8.14
8,14
8,14
8,14
8.14
8.14
8.14
B.14
814
8.13
8.13
8,14
8.13
4.13
813
813
8.13
8.13
8.13
8.13
8.13
8.13
8.13
813
813
8.13
813
8.13
gpm
8.1
8.1
6.1
81
6.1
6.1
81
6.1
8,1
6,1
61
8.1
8,1
61
61
6.1
61
8.1
8.1
61
61
6.1
6.1
8.1
6.1
8.1
8.1
8.1
8.1
61
8.1
8.1
8.1
6.1
6.1
8.1
8.1
6.1
61
6.1
6.1
8.1
8.1
6.1
8.1
6.1
8.1
8.1
81
6.1
61
8.1
8-1
8.1
61
81
6.1
61
8.1
8.1
6.1
61
8.1
81
6.1
61
6 1
6.1
6.1
8.1
8.1
B.I
-------
FURNACE A WITHOUT CATALYST-LOW HEAT HtMOVAl RATE
2fl-Jur>-85 Run TTD-1A
time stacked diuHon water in water out fire-bo* flmfcfent stack CONgJt
sec "" " "
24320
24380
24440
24500
24560
24620
24680
24740
24796
24856
24918
24976
25036
25096
25156
25216
25276
29336
25386
25456
25518
28876
25636
25696
25756
25816
25876
25936
25996
26056
26116
_, 2*1"
D z8232
OJ 28292
KJ 26352
26412
26472
26532
26592
28652
26712
26772
26832
26892
26852
27012
27072
27132
27182
27252
27312
27372
27432
27492
27548
27608
27668
27728
27788
27848
27908
27868
28028
2(088
2(148
28208
2(268
2(328
28388
2(448
2(508
28566
r
112
111
108
108
107
105
104
104
103
102
102
100
100
98
99
88
87
96
86
m
95
84
94
93
93
S3
92
91
81
90
80
80
90
BO
90
80
88
88
(9
(8
89
89
90
80
80
90
80
80
90
80
90
90
90
90
80
90
90
80
80
90
80
80
90
90
89
88
88
89
88
88
at
88
r
73
73
72
72
72
71
71
71
71
70
71
70
70
70
70
70
70
70
71
72
72
72
72
73
73
73
73
73
73
71
71
71
70
70
70
70
68
71
72
74
75
76
76
75
75
75
7S
75
75
75
75
75
75
75
75
75
75
75
75
75
74
73
73
72
72
73
73
74
74
75
75
74
f
189
168
168
168
168
168
188
168
168
188
188
168
168
168
188
ier
16T
187
187
187
167
187
186
168
166
168
188
166
166
166
166
188
16S
169
165
18S
169
165
185
189
165
169
165
185
189
16S
185
184
164
184
184
164
184
164
184
184
163
164
183
163
163
183
183
182
182
182
182
162
162
182
162
182
r-
175
175
175
176
175
175
175
17S
175
175
178
175
175
175
175
175
174
174
174
174
174
174
174
174
174
173
173
173
173
173
173
173
173
172
172
172
172
172
172
172
172
172
171
171
171
171
171
171
171
171
171
171
170
170
170
170
170
170
1(8
169
169
169
168
169
169
169
169
168
169
186
168
168
F
465
474
484
455
448
439
432
427
421
416
411
407
402
387
393
389
385
382
379
375
373
370
388
365
383
381
399
397
385
354
393
391
349
348
347
348
34S
344
343
341
338
337
336
334
332
331
329
S27
326
32S
323
323
321
320
319
317
316
31S
313
311
310
309
308
306
306
308
309
309
304
303
303
302
F
74
74
73
73
72
72
71
71
71
70
70
70
70
68
70
69
a*
68
69
68
69
68
68
88
89
6S
89
88
70
70
70
70
70
70
70
69
69
88
89
70
70
70
70
70
71
71
72
72
72
72
72
73
73
73
73
73
73
73
74
74
74
74
73
73
73
73
72
72
73
73
73
73
F
131
128
127
125
123
122
120
119
118
117
116
115
114
113
113
112
111
111
110
109
108
108
108
107
108
108
108
108
105
108
108
108
109
109
104
104
104
103
104
103
104
104
104
104
109
108
109
105
108
109
109
108
108
109
109
105
108
109
108
109
109
108
104
104
104
103
103
103
103
104
104
103
ppm
18738
18787
17788
18903
18052
1940S
14864
14368
13884
13477
13163
12769
12529
12284
12081
11888
11799
11578
11458
11308
11214
11084
11100
11027
11019
11039
10933
10887
10848
10783
10885
10868
10832
10811
10779
10783
10759
10748
10738
10921
10929
11003
11068
11068
11018
10880
107(5
10714
10628
10579
10559
10478
10498
10510
10488
10470
10428
10405
10409
10421
10429
10295
10132
10046
9989
10091
10177
10380
10466
10653
10714
10791
COoWl
281.5
2700
254.7
234.8
223.8
206.7
188.7
190.8
178.2
172.8
169,1
161.5
189.8
151.9
1480
142.8
136.7
138.0
133,6
128-2
126.3
125.3
124.2
1217
121.1
117.2
120,1
114,3
118.2
114.7
112.6
114.7
112.6
111.9
111.3
111.0
111.0
108.1
102,4
108.0
87.5
083
965
938
96,5
88.8
96.0
83.9
984
94.8
83.8
944
82.8
93.1
913
808
90.8
81.1
88.5
890
823
978
993
987
98.3
83.8
900
88.7
902
928
81 5
87.6
CO low
pprn
5013,4
5009
5011
5011.8
5013
5011.8
9010.6
9011
50102
9011.8
8010.2
5011.4
5012.6
5013
50126
5011.8
80118
90094
9010.8
5012.2
50116
50122
50102
50102
5011.4
5012.2
8012.2
9010.2
9011.8
50122
8011.6
5010.2
5013
5011.8
5011.4
50100
501X8
8011.4
50118
5011.4
50106
9010.6
50114
50118
5011,8
5013,4
5010.2
90122
5011.8
5011
50122
5013
50096
5011
50108
9011 4
5010.6
9011.8
8010.6
5012.2
80088
5013
5011
50114
50106
5011.6
5011
90116
5012.8
5011.8
5011
5008.5
O2
9.81
8.89
992
9.99
10.07
10.11
1011
1012
1018
10.24
10.23
10,3
10.33
10.35
104
10.41
1041
10.48
10.47
10 §1
10.48
1088
10.5
10.49
10.47
10.39
10.48
10.48
10.47
10.51
10,43
10,42
10.42
1042
1048
10.47
10.48
10.42
10.43
10.28
10.22
10.13
10,04
10.02
998
1008
10.18
10.17
10.24
10.31
10.3
10.37
10.37
10.35
1038
10.41
10.47
10.81
10.57
10.93
10-88
10-73
10.92
11.09
11.14
11 18
11,13
11.07
11.02
10.93
1088
10,(4
C02 JUM-THC
* pom
9.63
995
9.44
9.31
917
9.09
80S
8.88
8.91
8.83
88
8.72
8.67
884
858
8.54
852
(.45
8,43
6.38
8.38
8,33
836
835
838
8,43
8.37
8.36
834
831
8.37
8.37
837
8.36
834
634
(.34
(33
8.33
(.47
8.8
8.57
865
865
8.68
8.55
(.48
(.48
(.39
(33
8.33
828
8.28
829
8.24
(.26
82
8.18
(.14
8.18
8.14
(.01
7.87
778
7.72
7.7
7.76
7.S3
7.69
7.97
a
8.08
Water
balance actual Sow rate
be
14
14
14.5
14.5
145
145
149
14.5
14.5
145
145
148
14.8
14.5
14.8
145
14.8
18
18
15
18
147
14.5
14.6
14.8
14.5
14.5
148
14.9
14.5
15
18
15
15
15
IS
19
16
19
19
14S
145
14.5
14.9
145
14.5
14.9
14,9
14
14.5
14
14
14
14
14
14
14
14
14
14
14
14
14
14
14
14
14
14
14
14
14
14
heat out
gpm Btu/Mervil
6.2 30288
82
82
62
62
6,2
82
82
62
62
6.2
6.2
62
62
6.2
82
82
6.2
6.2
62
62
62
62
62
62
62
6.2
62
62
6.2
62
82
62
6.2
62
6.2
62
6.2
8.2
62
6.2
8.2
6.2
8.2
8.2
82
8.2
6.2
82
8.2
6.2
62
8.2
82
82
8.2
62
8.2
8.2
8.2
8.2
8.2
82
82
6.2
6,2
6.2
8.2
8.2
62
6.2
8.2
3S3.S7
353.57
40408
353.57
353.57
353.57
330.00
393.97
393.97
35357
353.57
353.57
353.87
393.57
404.22
353.70
393,70
393,70
353.70
383.70
353.70
404.37
40437
404,37
353.82
353.82
393.82
383.82
383.82
330.23
353.82
404.91
383.84
353.84
35394
383.84
19384
38394
38384
35384
39384
30338
303.38
303,38
303.38
303,38
354,07
384.07
384.07
1S4.0T
354,07
303.48
283.25
30348
303.49
384.18
303.49
303.88
303.89
303.98
303.89
303.99
354.31
354.31
384.31
39431
15431
384,31
30370
303,70
303.70
Prtntaejon 02-Apr-98
Water meter
Draft Cool water readng
OnfOff *
Off
Off
Off
Off
Off
OB
Off
on
Off
Off
on
Off
Off
Off
Off
Off
on
Off
Off
Off
on
Off
Off
Off
Off
Off
on
OS
Off
Off
Off
Off
Off
on
Off
Off
Off
on
Off
Off
on
Off
Off
Off
on
on
Off
on
Off
Off
Off
Off
Off
Off
on
Off
Off
on
Off
OB
OB
Off
on
Off
on
Off
on
OB
on
Off
Off
Off
8,13
813
8.13
813
8,13
8-13
813
8.13
8 13
6.13
813
8.13
8.13
813
813
8-14
8,14
8.14
8.14
8.14
8.14
6.14
814
6.14
8.14
8.14
8.14
8.14
t-14
814
(.14
814
6.14
8.14
(14
8 14
8.14
8.14
814
8.14
1.14
(.14
8.14
(.14
8.14
(.14
814
8.14
114
(.14
8.14
8.14
814
814
8,14
8.14
8.18
8.14
815
8.19
8.18
8.15
8 15
818
8.19
8.19
818
8.16
8 15
8.15
8.18
8.15
6.1
6.1
6.1
61
6.1
8.1
6.1
8.1
6.1
61
8.1
6.1
6.1
6.1
6.1
81
81
61
6.1
81
6 1
6.1
61
81
8.1
6.1
6.1
8.1
81
6.1
8.1
8.1
61
81
8.1
8.1
8.1
8.1
8.1
61
8.1
6.1
61
61
6 1
8.1
8.1
81
8.1
81
8.1
61
6.1
6.1
6.1
81
6.1
8.1
61
6.1
8.1
8.1
6.1
6.1
61
6.1
6.1
6.1
8.1
6.1
6.1
61
-------
FURNACE A WfmOUT CATALYST-LOW HEAT RiMOVAl RATE
28-Jun-95
time st
sec
28626
28688
28748
28808
28868
28924
28984
28044
29104
29184
28224
29284
29344
28404
29464
29524
28584
29644
29704
29764
29824
29884
29944
30004
30064
30124
30184
30244
30300
30360
30420
30480
rt 30940
Jj 30800
^j 30680
30720
30780
30840
30900
30880
31020
31080
31140
31200
31280
31320
31380
31440
31500
31560
31620
31676
31738
31796
31856
31918
31978
32036
32096
32158
32216
32276
32336
32396
32456
32516
32578
32636
32696
32?5«
32816
32876
RunTTtMA
ICK exit dlutiGn water "m water out f
F F F F
88 75 182 168
88
88
gg
88
aa
gg
68
M
87
g?
»7
87
g7
87
87
gg
87
(7
87
g?
87
83
101
107
111
115
117
118
121
123
125
126
128
128
130
131
133
134
136
137
138
139
140
141
142
142
142
143
144
145
145
148
147
147
147
148
148
149
149
14B
150
151
1S1
151
151
1S1
151
151
152
152
152
75
7S
74
73
72
72
72
72
73
74
74
75
74
74
74
74
74
73
73
72
71
72
74
74
75
75
76
76
76
77
77
77
77
77
77
77
77
7?
78
7g
77
76
76
75
74
75
75
76
77
77
77
77
77
78
78
78
78
78
78
78
78
78
79
79
79
79
78
79
79
78
79
162
182
161
161
1B1
181
160
181
181
160
160
180
180
180
180
160
180
160
100
159
159
159
159
158
159
159
158
158
158
158
158
158
1S8
158
158
158
159
158
158
1S8
158
isa
tsa
156
158
158
158
159
189
159
160
180
'90
180
180
180
160
160
181
181
181
181
181
1«1
161
162
181
182
182
1*2
182
168
168
168
168
187
167
167
187
187
167
167
18?
187
166
188
188
166
196
189
188
189
189
195
185
195
195
185
195
185
185
195
195
194
184
194
194
194
19!
185
185
195
195
195
165
195
165
165
185
196
166
166
168
168
166
16S
187
167
167
187
197
167
167
168
167
168
19*
168
188
188
188
168
re-box ambient
F F
302 73
300
300
299
298
29?
286
296
285
295
285
295
294
284
293
283
282
291
290
288
289
288
275
260
257
284
276
283
310
328
346
364
381
38*
414
429
444
459
473
4*e
497
507
517
525
531
537
540
542
543
545
548
551
SSS
580
564
594
59?
597
see
S98
572
574
575
57S
573
572
571
570
Sta
588
S87
587
73
73
73
73
73
73
72
72
n
72
73
72
73
73
73
73
73
73
73
73
72
72
71
72
72
72
72
72
72
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
73
73
73
73
72
73
73
73
73
73
73
stack CO Hfr
103 10888
104
103
104
104
104
103
103
102
102
102
102
102
102
102
102
102
102
102
103
102
102
10?
117
125
131
138
140
142
149
147
150
152
154
156
15?
158
181
183
184
165
188
167
189
169
170
171
171
172
173
173
174
174
175
176
178
177
177
178
178
178
178
179
179
179
178
178
ISO
180
180
180
180
10828
10870
10882
10881
10873
10488
10480
10490
10518
10868
10477
11084
11210
11332
11340
11377
11357
11300
112*3
11153
11011
11178
8142
6299
7739
9041
9904
10941
11320
12024
12622
12878
13188
13265
13308
13623
14180
14485
14644
14798
14558
14140
14071
14018
13861
1398S
13883
1399?
14083
13924
13847
13847
13802
13684
13485
13306
13265
13212
13180
13058
12833
12541
12486
12459
12423
12573
12577
12622
12781
12889
12935
COdlu
905
80.7
81.5
95.1
102.1
100.8
101.6
1030
1007
80,3
908
82.0
92,1
91.6
80.5
82.4
926
820
93.1
101.1
100.7
101,6
375,5
4*8.6
421.5
547.4
8359
6855
7S0.8
798.7
848,5
885.7
908.8
823.3
9287
830.8
954.8
885-1
101SO
1027,3
1042.2
1025.4
887.7
888,2
991.5
8*3.6
990.2
888.0
9*5,2
895.8
8*4.0
876.4
978.7
977.5
971.4
858.8
950,7
840.3
9380
838.7
8354
8124
892.4
8*8.2
M7.2
885.3
3896
899.7
682.8
9064
919,7
825.8
CO low
5011
5012,8
5011 8
5013.4
5013
50118
5011.4
SOOT 8
5011
5010.6
5011.8
5011.8
501 1.S
5011.8
5008.5
5010.8
5011.4
5013
5011.4
50094
5011
5010.*
5013.*
50102
50138
5010.9
5011.4
5011
5010.2
5009.4
5011.4
5011.4
5011
5010.2
5010.6
5011.8
5012.2
5012.2
5011
5011
5010.8
5009.4
5012.2
§010.2
50118
50118
5010.2
5012.6
5009.8
5010.8
5010.2
5012.6
5012.2
5011
5010.8
5012.6
5013
5010.8
5011
5011.4
5010,8
5010.6
5011.4
5010.8
50084
5011
50118
5011.4
5012.6
5011
5010.2
5008.8
O2
10.8
10.77
10.75
10.77
1085
11.08
11 23
1129
1137
11.4
11 34
11.23
11.1
11
1093
10.92
10.9
1082
1097
10.8?
11.08
11.21
11.13
13,34
1835
19.56
18.22
15.85
1547
1509
14.71
144
14.11
13.88
1368
1349
13.23
12.95
12.71
12.51
12.38
12.24
12.18
12-08
11.95
11.71
11.59
11.58
11.57
11.81
11.57
11.52
11.47
11.45
11.43
11.43
11.41
11.44
1149
11.5
11.53
1152
1154
11.57
1182
11.54
11.61
11.84
11.88
11.45
11.83
11.97
CO2 JUM-WC
% ppm
80S
8.12
8,14
813
8.0?
7.82
7.77
7,74
7,71
7.66
7,79
7.86
7.8?
6.05
813
8.13
8-15
814
S.t
g.1
8.02
7,83
8.02
6,08
3.98
4.02
4.35
4.71
508
5.41
5.78
6.05
8.3
6.51
6.7
888
7.08
7.35
7,55
7.78
7.68
798
8.09
8.16
8.28
8.41
8.41
8.44
8.44
8.4
9.43
848
848
8.52
8.53
854
8.58
8.52
8.48
845
8.41
8.49
8.43
«.4
8.37
8.49
8.39
8.37
8.35
8.38
8.3S
832
Water
balance actual ftow rate heat out
Iba gpm Btuflnterval
14 6.2 303.70
13.5
13.5
135
135
135
13.S
13.5
13.8
14
14
13.7
13.5
135
13.S
13.5
13.5
13.1
13
13
13
13
13
12.7
12.5
12,5
125
12,5
12.5
125
12.5
12
125
12.5
12
12
12
12
US
11.5
115
11.6
11.5
11,5
11.5
11.3
11
11
11
11
11
10.8
10.5
105
10.5
10.5
10.5
10.5
10
10
e.2
8.2
62
6.2
62
82
6,2
6-2
62
6.2
62
6.2
8.2
8.2
62
82
8.2
82
82
82
62
82
8.2
9.2
6.2
9.2
9,2
6.2
62
8.2
6.2
8.2
9-2
6.2
6.2
62
82
e.2
62
8.2
6.2
92
92
9.2
9.2
9.2
82
6.2
6.2
82
6.2
82
6.2
82
e.2
6.2
6.2
9.2
6.2
8.2
e.2
6.2
e.2
82
e.2
t.i
82
8.2
303.70
303.70
354.43
330.80
303.80
303.80
354.55
30380
303.80
354.55
35455
354.55
35455
30390
30380
30390
30390
303.80
303.90
354.87
354.87
354.87
304.00
30400
30400
304.00
283.74
304.00
30400
354.79
35479
30400
304.11
304.11
30411
304.11
25334
354.79
354.78
354.79
35479
354.79
354.79
304.00
304.00
304.00
30400
304.00
3546?
331.03
303.90
30390
303.80
303.90
303.90
354.55
354.SS
354.55
303.80
303.80
30380
303.80
354.43
303.60
354.43
303.70
354.43
30370
303.70
303.70
30370
Water meter
Draft Cool water readnfl
On/Off density, 1*311 apm
Off 815 6.1
Off
Off
Off
Off
Off
Off
Off
OB
Off
Off
Off
on
Off
on
Off
Off
Off
Off
Off
Off
on
Off
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
8.15
S.15
815
8.15
815
815
816
a 15
815
8.16
8.18
816
816
8.16
816
816
818
816
8.18
816
818
8.16
8.18
816
8 10
818
816
8.16
816
8.18
*.16
8.18
8 18
8.18
8.19
8.16
8 18
8.18
1. 18
a ie
a, is
i.18
8 16
8.16
8.18
8.18
818
8.18
a. is
8.16
8.16
fl 16
8.16
8.16
8 16
8.18
8.18
8.18
8.15
8.15
8.15
815
815
815
a. 15
8.15
(.15
8.15
*.15
815
8.15
6.1
81
81
61
81
61
81
81
8.1
8.1
81
8.1
81
8,1
81
6.1
91
81
8.1
8.1
8.1
9.1
61
9.1
8.1
81
8.1
8.1
8.1
8.1
8.1
9,1
8.1
9.1
9.1
8.1
61
8.1
8,1
8.1
8.1
6,1
6.1
81
8.1
8.1
6.1
9.1
8.1
6.1
61
8.1
8.1
61
9.1
9.1
6.1
9,1
e.t
8.1
8.1
e.1
8.1
8.1
81
6.1
8.1
81
9,1
8.1
p
-------
FURNACE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE
2B-Jun-95 RunTTCMA
tim« *taefcetft dlution watarln water out fire-box ar
sec
32936
32996
33052
33112
33172
33232
33292
33352
33412
33472
33532
33592
33652
33712
33772
33832
33892
33952
34012
34072
34132
34192
34252
34312
34372
34428
34488
34548
34608
34688
34728
34766
-1 34848
Jj 34908
^ 35028
35088
35148
3S208
35288
35328
35388
35448
35508
35568
35828
35688
35748
35804
3S884
35924
35984
36044
36104
38194
38224
36284
38344
38404
38484
36524
38584
38644
38704
38764
38824
38884
38944
37004
37004
37124
37180
F
183
153
153
153
153
183
15S
183
153
153
153
183
153
153
153
152
152
1S2
1SJ
154
154
184
155
154
154
184
155
150
188
150
188
186
157
157
186
158
15O
157
157
158
155
158
156
155
188
155
158
1S5
155
155
155
154
155
154
154
155
15S
158
155
155
155
155
154
184
153
153
152
151
143
133
125
120
F
80
80
79
79
79
79
78
78
78
77
76
76
77
77
77
77
78
79
80
81
82
82
82
83
83
83
83
84
84
84
84
64
84
84
85
85
85
85
85
85
85
84
83
82
82
82
81
81
81
81
81
80
80
80
80
80
80
81
81
81
81
81
80
80
80
80
81
81
80
78
77
77
F
182
182
182
182
163
162
183
183
183
183
183
163
183
163
163
183
104
104
104
104
184
164
104
194
164
184
104
189
188
185
185
105
105
165
195
185
1M
185
105
16S
188
185
186
169
198
188
188
108
189
188
108
189
too
196
188
100
187
188
107
107
187
167
107
167
187
187
187
107
187
187
107
107
F
186
169
169
169
169
189
189
189
169
170
170
170
189
170
170
170
170
170
170
170
170
170
170
170
171
171
171
171
171
171
171
171
171
171
172
171
172
172
172
172
172
172
172
172
172
171
172
173
173
173
173
173
173
173
173
173
173
173
173
174
173
174
174
174
174
174
174
174
174
174
174
174
F
568
589
889
570
570
588
586
565
S84
504
583
581
580
559
557
559
594
584
854
554
583
550
847
544
541
840
539
538
537
535
533
531
530
528
526
524
523
521
520
510
517
515
515
515
513
513
514
513
512
512
512
511
511
512
511
510
500
808
507
505
504
501
403
400
480
487
485
4(5
404
481
404
446
nHent Mack COHgti
F
73
74
73
73
73
73
73
73
73
73
72
72
72
72
72
72
72
72
72
72
72
73
72
73
73
73
73
73
73
73
74
74
74
74
74
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
78
75
75
74
74
74
73
73
71
73
73
73
73
73
F
180
180
180
181
181
181
181
181
111
181
181
181
180
180
180
100
180
181
181
182
102
183
183
183
184
184
105
188
185
185
115
185
185
185
185
185
IBS
184
184
184
184
184
183
183
183
182
182
182
182
182
182
182
182
182
1B2
182
182
183
182
182
182
182
182
181
180
170
179
180
174
182
151
144
12904
12948
13086
13277
13281
13167
12944
12870
12810
12822
12705
12855
12732
12793
12707
12883
12902
13040
13051
13094
13090
12869
12431
12455
12718
12663
12594
12581
12500
12504
12549
12577
12504
12565
12557
12504
12354
12304
12301
12158
12048
11898
11808
11648
11905
11088
11523
11454
11309
11251
11100
11113
11104
11035
10968
10925
1092S
10852
10009
10974
10938
10009
10872
11133
11243
11271
11180
11104
10060
9900
13102
15813
COdkj
927.8
918.8
925.0
938,3
947,9
041,8
026.1
017.8
917.0
915.5
917.0
007.9
906.6
011.3
912.4
917.3
923-7
0295
032.1
034.4
9384
0338
901.5
891.9
010.2
918.0
9087
005.8
9081
0070
9046
001.4
901 0
9015
004.8
902.5
8082
8906
8885
•787
8704
882.8
8486
837.2
8308
1338
820.4
819.0
811.4
8052
702.8
790.7
7931
788.1
783.4
7800
770.1
770.5
7775
700.3
779.0
777.S
708.4
780.4
803.9
803.2
7079
794.0
750.0
220.4
155.3
104,2
CO tow
ppro
SOU
50098
5010.9
501 IB
5010.2
5011
5013
5012.2
5011.8
son
5010.6
5011.4
50102
50098
5012.2
5010.2
5011.4
5011.8
5010.8
5012.8
5012.8
5011
5009.6
5008.5
5013
5011.4
5008.1
5011
5013.4
5010.2
5013
50001
50102
50114
5013
50102
5010.6
5012.6
50098
5011
5010.8
5011
5011
5012.6
50118
50085
5011.8
5011
5010.2
5000.4
5010.0
5011
5013
50085
5010.9
5009.4
5011
50118
8013.4
5011.8
5010.0
5010.2
50096
5010.8
50114
50114
5011.8
5011
5011
5010.2
5011.4
5012.2
O2
11.59
11.57
1159
11.53
11.52
11.53
11.59
11.88
1108
11,71
11.72
11 74
11.74
11.73
1178
11.78
11.71
1187
ties
1159
11.57
11.93
11.81
11.85
11.84
11.84
11(3
11.81
11.8
11.82
11.12
1183
1101
11.92
11.9
1104
12.01
12.11
1212
12.14
12.23
12.25
12.22
12.23
12.2
12.2
12.22
12.22
13..2
12.17
12.21
12.19
1218
12.21
12.21
12.28
12.20
12.28
12.3
12.28
12.31
12.33
12.51
12.78
128
12.74
1281
12.83
12.03
1S.78
12.2
1083
C02 JUM-THC
% ppra
8.37
838
838
8.41
84
8.4
8.33
829
8.25
823
8.21
8.19
8.19
8.19
8.19
8.19
8.24
820
8.31
8.37
830
635
8.18
614
6.15
8.15
819
0.2
822
8.24
822
8.2
817
815
8.17
8.14
8.04
7.95
793
7.87
78
778
779
7.78
7.81
781
7.79
7.81
7.85
7.17
785
7.85
7.88
7.85
788
783
778
7.70
7.78
7.81
7.78
7.78
758
733
732
732
7.91
7.32
7.2
844
704
9.1
Water
balance actual flow rate
bs
10
10
10
9.5
0.5
05
8.8
98
95
95
98
05
95
8.5
8.5
85
85
85
7.5
7.S
7.5
7.5
7.5
7
7
7
7
7
7
6.8
6.5
6.5
95
9.5
04
81
0
8
8
0
8
5.5
5.5
5.5
5.5
5.9
5.5
S.5
5.5
5
5
5
5
5
5
5
5
52
4.0
4.5
45
4.5
Iwatoul
gpn Btufintervxl
9.2 303.70
62
9.2
92
9.2
02
6.2
8.2
8.2
02
62
82
62
6.2
82
82
8.2
82
8.2
0.2
62
62
02
6.2
8.2
02
82
8.2
82
62
82
8.2
62
92
8.2
82
0.2
8.2
8.2
8.2
8,2
02
8.2
8.2
62
82
62
8.2
82
8.2
9.2
62
62
9.2
92
92
9.2
02
82
8.2
0.2
8.2
8.2
82
8.2
62
6.2
8.2
82
8.2
0.2
82
33089
35431
35431
303.59
35431
30389
30358
303.59
35410
354.18
354.10
30359
354.10
154.10
354.19
303.40
10340
10340
303.49
303.40
103.49
30349
30349
330.48
35407
354.07
30338
303.38
301.38
30338
30338
303,38
30338
353,94
30338
103.28
383.84
S53.04
35394
303,28
383.84
30328
303.28
303.28
353.82
301.28
110.23
353.82
351.82
153.12
351.12
35312
35382
353.11
351.82
301.17
353.12
301.17
353.70
303.17
35370
353,70
35370
353,70
35S70
353.70
353.70
35370
35370
330.12
3S3.70
Dm*
Water meter
Coot water readng
OrVOff density, MgH
On 8.18
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
Off
Off
Off
Off
8.15
815
8.15
815
8.15
8.15
8.15
«.15
8.1S
8.15
815
8.15
8.15
815
8.14
8 14
8.14
(.14
1.14
1.14
8 14
814
8.14
8.14
8.14
8.14
8.14
8.14
8.14
8.14
814
814
8.14
814
8.14
814
(.14
8.14
8.14
8.14
8.14
8.14
8.14
8.14
§.14
8.14
8.14
8.14
8.14
814
814
8 14
8.14
8.14
8.14
8.14
8.14
0.14
(.14
8.14
0.14
8.14
8.14
8.14
(.14
8.14
814
*.14
814
8.14
81
61
9.1
91
8.1
8.1
0.1
0.1
0.1
6.1
8.1
81
9.1
9.1
9.1
81
8.1
0.1
0-1
0.1
8.1
8.1
8.1
9.1
91
91
81
81
0.1
01
0.1
81
91
91
91
91
81
01
01
8.1
81
61
91
81
6.1
8.1
0.1
81
81
01
61
8.1
81
8.1
01
8.1
0.1
0.1
8.1
8.1
8.1
6.1
61
01
91
81
0.1
8.1
8.1
01
9.1
61
-------
FURNACE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE
02-Apr-96
28-Jun-95 RunTTD-1A
time stack exit dlution water in water out fire-box ambient
sec
37240
37300
37360
37420
37480
37540
37600
37660
37720
37780
37840
37900
37960
38020
38080
38140
38200
38260
38320
38380
38440
38500
38556
38816
38678
38736
38796
38856
38916
38976
39036
_. 39096
J 39156
•J 39216
ft 39276
39336
39396
39456
39516
39576
39636
39696
39756
39816
39878
39932
39992
40052
40112
40172
40232
40292
40352
40412
40472
40532
40592
40652
40712
40772
40832
40892
40952
41012
41072
41132
41192
41252
41308
41368
41428
41488
F
116
113
111
109
107
106
104
103
102
101
100
99
98
97
96
95
94
94
93
93
93
93
93
93
93
92
92
92
92
91
90
90
89
89
88
88
88
87
87
86
86
86
86
85
86
85
85
85
86
86
86
86
86
88
85
85
85
85
85
85
85
85
85
85
85
85
85
84
84
84
84
84
F
77
76
77
76
76
76
76
76
76
76
75
73
73
73
74
75
77
78
79
79
78
77
78
76
76
75
74
74
75
74
74
74
74
74
74
73
73
73
73
73
72
73
73
73
74
74
75
75
75
75
74
74
73
73
73
73
73
74
74
75
76
75
75
74
74
74
73
73
73
73
74
74
F
167
167
167
167
167
167
167
167
167
167
167
167
167
167
167
167
167
166
167
166
166
166
166
166
166
166
165
165
165
165
165
165
165
184
184
164
164
164
164
164
164
163
163
164
163
163
163
163
163
163
183
162
162
162
162
162
182
162
162
162
162
161
182
161
181
161
161
161
161
161
161
160
F
174
174
174
174
174
174
174
174
174
174
174
174
174
174
174
174
173
173
173
173
173
173
173
172
172
172
172
172
172
172
172
172
171
171
171
171
171
171
170
171
170
171
170
170
170
170
170
170
170
169
169
169
169
169
169
169
169
168
168
168
168
168
168
168
168
167
167
167
167
167
167
167
F
429
416
406
398
391
384
379
374
370
366
362
358
354
352
349
347
345
342
339
336
334
332
330
328
327
325
323
321
319
318
318
317
315
314
314
312
311
310
309
308
307
306
305
303
303
302
301
300
298
297
296
294
294
293
292
291
291
290
290
289
289
288
286
285
285
284
283
282
282
281
281
281
F
73
74
74
74
75
74
75
75
75
75
75
75
74
74
73
73
73
73
73
74
74
74
74
74
74
74
74
74
73
73
73
73
72
72
71
71
71
71
71
71
70
70
70
70
70
70
70
70
71
71
71
71
71
71
70
70
70
71
71
71
71
71
72
71
71
71
71
71
71
71
71
71
stack CO high
F
137
132
129
126
124
122
120
119
118
117
116
115
114
113
112
111
111
110
110
109
109
109
108
108
108
107
107
107
106
106
106
105
105
104
104
104
103
103
103
103
102
102
102
102
102
102
102
102
103
103
102
102
102
102
101
101
101
101
101
102
102
102
102
102
101
101
100
100
100
100
100
101
pffn
15999
15418
14628
13790
13078
12419
11922
11414
10999
10579
10291
10038
9701
9424
9261
9188
9176
9184
9151
9151
9180
9009
8972
8919
8761
8687
8634
8561
8553
8549
8521
8549
8643
6679
6704
8712
8651
8683
8716
8716
8773
6781
8736
8720
8785
8919
8976
9025
9017
8927
8785
8748
8744
8744
8720
8634
8671
8793
8907
8997
9045
9111
9045
8927
8875
8789
8728
8724
8740
8757
8793
8927
COdkj
ppm
2067
2025
1860
1727
1608
146.6
1392
1296
1243
119.0
1157
1141
112.5
105.8
101.2
95.4
91 5
890
869
841
91.0
864
854
889
85.4
863
837
868
81 4
841
824
799
81 1
807
812
80.6
815
81 5
799
801
791
81.4
81.4
77.1
729
72.1
72.6
74.4
775
77.5
78.1
765
77.5
763
781
80.1
688
715
71 0
713
695
706
762
767
752
757
763
745
71 1
750
667
679
CO low
ppm
50094
50106
5011.4
501 1 .4
50114
5011
5011 8
5011 4
5011
5011 8
5011.8
5011.4
5011 4
5011
50126
5011
5011
50122
50102
50122
50134
50118
5012.6
5009
50122
50106
5012.6
5011 8
50126
50128
5013.4
5013
5009
5011
50114
50122
50118
5011 8
50114
50118
5011.4
5011.4
5013.4
5011 8
50114
5011 4
50122
50106
5011
50118
50106
50126
5011
50134
50114
50102
50126
5011
50108
5011
50102
5011
50138
50126
50122
50094
5013.4
5011.4
5008 1
50122
5011.8
50126
02
1028
1028
1038
1048
1056
1063
1064
107
1072
1076
10.75
10.78
1086
10.96
1099
1099
1089
10.84
1077
1074
1065
10.74
1076
1078
1092
1101
11.07
11.17
1122
1123
11.29
11.27
11.22
11.2
11.21
11.23
11.29
11.33
1133
11.35
1135
11.21
11.12
11.2
11.18
11.09
11.08
1104
11.08
11.16
11 3
1136
1139
11.41
11.44
11 56
11.59
11 5
1142
1133
11.3
1126
11.32
11 46
11.52
116
11.7
11.72
11.76
11.75
11.78
1167
C02 JUM-THC
% ppm
934
928
91
896
886
877
872
865
859
8.52
85
8.47
839
8.3
826
827
835
84
846
849
855
8.47
8.46
845
833
828
8.22
8.16
8.13
613
811
813
819
821
823
8.24
82
819
82
8.18
821
8.23
8.17
8.17
821
829
834
839
838
827
817
813
813
81
809
8.01
7.99
8.1
6.16
823
825
829
8.26
8.13
608
801
793
793
792
791
7.9
8
Water
balance actual flow rate
tx
45
4.5
45
45
45
45
4.5
4.5
45
4.5
4.5
45
4.5
5
5
5
5
5
45
4.5
4.5
45
45
45
45
4.5
45
5
5
5
5
5
5
5
5
5
55
5.5
5.5
5.5
5.5
5.5
5.5
55
5.5
5
5
5
5
5.4
55
5.5
5.5
55
55
5.5
55
52
5
5
5
5
5
5
5.4
55
55
55
55
5.5
5.4
5
heat out
opm Btu/lnterval
62 35370
62
62
6.2
62
6.2
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
82
62
83
63
6.3
63
83
63
63
63
63
63
63
63
63
63
63
83
63
63
63
63
63
63
63
63
6.3
63
63
63
63
6.3
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
35370
35370
35370
35370
35370
35370
35370
353.70
35370
353.70
35370
35370
35370
35370
35370
30317
35382
30317
35382
35382
33023
35382
30328
30328
30328
35907
35907
35907
35907
35907
35907
30778
35920
35920
35920
35920
35920
30788
35920
30788
41065
35932
30788
33537
35932
35932
35932
35932
307.99
30799
35944
35944
35944
35944
35944
35944
30810
30810
30810
30810
35957
30810
35957
35957
30820
30820
287.65
308.20
30820
30820
35969
Draft
Water meter
Cool water readna
On/Off density, IVgBl
Off 814
Off
Off
Off
Off
Off
Off
Off
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
Off
Off
Off
Off
Off
Off
on
on
on
Off
Off
Off
Off
on
on
on
on
on
Off
Off
Off
Off
on
on
Off
Off
Off
Off
Off
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
Off
Off
Off
Off
8.14
614
814
814
814
814
8.14
814
814
814
8.14
814
814
814
8.14
814
814
8.14
814
814
814
814
814
8.14
814
814
814
814
8.14
8 14
614
814
814
8.14
814
814
8.14
8.14
8.14
814
815
815
814
815
815
815
8.15
8.15
815
815
815
815
815
8.15
815
815
815
815
815
815
815
815
815
815
815
815
815
815
8.15
8.15
816
61
61
61
6.1
61
61
61
61
61
8.1
61
61
61
61
61
81
61
61
61
61
61
6.1
61
61
6.1
61
62
62
62
62
62
62
62
62
62
62
6.2
62
62
62
62
62
62
62
62
62
62
82
62
62
6.2
62
82
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
6.2
-------
FURNACE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE
2S-Jun-9S RunTTD-1A
time slack exit rJlutlon water in water out fire-box ambient
see
41548
41808
41881
41728
41788
41841
41801
41 Dei
42028
42088
42148
42208
42288
42328
42388
42446
42508
42588
42828
42884
42744
42804
42884
42924
42884
43044
43104
43184
43224
43284
43344
,_, 43404
U 4M'<
1>J 43524
ON <3584
43844
43704
43764
43824
43884
43844
44004
44080
44120
44180
44240
44300
44360
44420
44480
44540
44600
44880
44720
44780
44840
44800
44980
49020
45080
45140
49200
45280
49320
45380
49436
49488
45568
45818
49876
45738
45796
F
84
84
84
84
84
84
84
80
99
108
110
113
117
118
121
124
128
127
128
130
130
131
132
133
133
134
135
138
137
137
138
138
139
140
140
140
141
141
142
142
142
142
142
142
143
143
143
144
144
145
145
14S
145
145
145
145
145
145
148
146
146
148
148
147
147
147
147
148
145
146
148
148
f
75
75
75
74
74
73
73
74
74
75
76
76
77
78
78
78
78
78
77
77
77
78
76
76
77
77
78
76
79
79
79
80
80
79
79
78
78
78
77
77
77
78
78
79
80
60
80
80
eo
10
79
79
78
78
78
78
78
78
80
80
80
81
81
80
79
79
78
78
79
79
80
80
r
180
180
180
160
180
199
158
159
159
159
159
159
159
199
158
159
158
158
158
151
158
158
151
151
158
158
151
151
158
158
158
158
158
158
158
158
198
158
158
19*
198
198
158
159
198
198
159
158
199
159
158
159
158
159
159
158
158
180
160
160
180
180
180
160
160
180
180
190
160
180
160
161
f
187
186
188
188
188
166
iee
188
188
185
185
186
185
185
185
165
185
185
164
164
185
184
184
184
184
184
184
165
164
185
185
185
165
165
165
165
185
185
185
165
185
185
185
166
185
186
165
188
166
188
186
166
168
168
168
166
168
188
188
166
188
188
166
187
168
187
168
167
167
187
167
187
F
280
280
279
278
277
278
278
269
260
257
260
287
277
288
300
313
326
340
351
381
370
378
380
317
382
397
401
405
408
413
418
420
421
422
424
429
432
433
438
435
433
430
426
424
424
429
425
428
428
427
429
426
421
421
423
423
423
425
424
422
422
423
429
427
430
434
434
435
438
438
439
436
F
71
71
71
71
71
71
71
70
70
70
70
70
71
71
71
71
71
71
71
71
71
70
70
71
70
70
70
71
71
71
71
71
72
72
72
71
71
71
71
70
70
71
71
71
70
71
72
71
72
72
72
72
71
71
71
71
71
71
71
71
71
72
72
72
72
72
71
71
71
71
71
71
stick CO Ntft
F
101
101
101
101
101
100
100
105
115
123
130
139
138
142
144
147
148
150
152
153
154
199
158
158
158
198
160
181
162
163
163
164
165
169
165
165
165
166
188
167
187
167
167
168
188
188
169
189
189
169
169
169
169
168
189
170
170
171
171
171
171
171
172
172
172
172
172
172
172
172
172
172
ppra
8033
8115
9135
9021
1880
8960
1854
8084
6722
4492
5001
6120
7058
7511
7810
8181
8354
8578
17i7
8021
9285
•477
9570
8741
8800
•812
9855
8823
9831
9835
9835
9758
9848
9848
8766
8816
S878
8812
10028
10075
10075
10158
10188
10217
10278
10339
10380
10457
10478
10508
10567
10584
10563
10728
9208
8037
10681
10583
10384
1042S
10405
10315
10319
10360
10449
10490
10608
10641
10824
10877
10722
10726
COfJUl
pfatn
682
70-5
74.5
77.0
72,8
770
77.5
2882
388.6
211,4
338.2
423,0
490.1
5226
551.1
570.3
586.8
8028
618.3
637.4
654.1
881.3
677.1
682,8
6898
882,9
668.9
684,8
888.2
6883
688.2
684,6
8797
678.2
8878
694.0
688,4
S999
704.1
707,0
707.7
706-2
708.2
719.0
717,0
723,1
728-7
733.2
733.7
738,4
746.4
7485
7487
799,0
762.7
752.0
748.4
740.4
733.1
723.8
727.2
712.2
71B.6
728.8
7328
738.8
744.8
7503
7458
741.8
7487
749.5
CO low
ppm
5010.8
5010.6
5010.6
6013.4
5010.8
5012.2
50106
9011
5009
4485.3
41735
5012.2
5012.2
50108
50085
5011.4
9011 8
50118
5009.8
5012.2
5011.4
5010.6
5011.8
90098
5010.8
5011
9010.6
9010.8
50102
5011
5012.6
90138
5011.8
9010.2
90106
50094
9011
9012.6
501 DO
50106
9012.6
5012.2
S009.1
50094
9010.2
5011.1
5012.2
9012.2
Ml 1.1
9012.8
50118
5011.4
SO1 1.4
50122
4720.5
4083.7
5009.4
9011.4
50094
9011
9011.4
SO1 1.4
5011
S012.2
5011.1
5010.8
5010.8
9013
5013
5008.5
50122
$012.8
O2
11.58
11-53
11.93
11-86
1172
11.75
11.15
11.7
131
17
17.41
17.08
1666
1636
16.06
15.78
1552
15.26
15.08
14.8S
14,72
14,81
14.61
14.58
14.4
14,27
14.18
14.12
14.05
13.98
13.95
1395
1395
13.93
1386
1361
13.75
1371
1389
137
13.72
13-73
13,75
1373
13-71
1384
1365
1362
13.81
138
1381
1359
1363
1366
14.21
15.38
137
13.88
13,5
1348
13,47
1348
13.44
13.43
13,41
13-38
13.38
1336
13.34
13.41
13.42
1333
CO2
%
8.08
1.13
8.13
8.03
7.98
7.98
7,18
8,02
8-16
3.89
3.48
3.83
4.21
4.46
4.75
5.03
8.27
5.49
5.66
511
588
8,08
809
811
8,28
638
6,44
840
8.99
6.81
8.82
684
683
6.84
8.71
8.73
8,82
8.87
8.88
8.88
885
8.81
6,79
6,79
6,82
6.89
8,15
8,M
6,88
6,88
688
688
6.14
682
8.07
501
688
691
683
6.88
8.80
6,88
692
8,93
695
8,86
8,98
8.98
701
6.94
892
693
balance
(a
5
S
5
5
5
5
5
55
55
54
5
5
5
5
4.5
45
45
4.5
45
4.5
4.5
4,5
4,5
4,5
4.5
45
4
4
4
4
4
4
3.5
39
4
4
4
4
4
38
3.5
3-5
S.S
3.5
3,5
31
3
3
3
3
3
3
3
3
3
29
2,9
25
2.5
2.3
2
2
2
2
2
2
2
2
2
1,5
15
1,5
Water
actual How rate
gprn
63
6,3
8.3
83
8.3
8.3
8.3
6.3
8.3
8.3
63
6.3
63
63
6.3
8.3
8.3
8.3
8.3
9,3
8,3
8,3
83
8,3
8.3
83
8.3
6.3
6.3
6.3
6.3
63
63
63
63
63
8,3
8.3
8.3
S3
8,3
8-3
6.3
83
5.3
8.3
83
6.3
6.3
63
8.3
63
63
6.3
6.3
83
63
63
6.3
6.3
8.3
83
8.3
8.3
6.3
8.3
63
6.3
83
63
6.3
63
Water meter
ntxtom
BtuMwil
39988
308.30
308,30
308.30
308.30
359,11
359-81
35981
359,81
308,41
308.41
359.81
308.41
301.41
30841
308.41
358.83
358.83
21784
308.51
399.83
308.51
308.51
308,91
308.51
308.51
301.51
J59.93
301.51
359.93
358.93
358.83
35893
39883
35983
358,93
35883
35883
35993
308.41
30141
2(7,85
30841
358,81
30841
35981
308.41
35881
358.81
35881
35881
35881
358,81
358,81
35981
35881
359.81
308.30
30830
308.30
30830
30830
308.30
359.68
287.75
35888
90830
35988
35988
35968
35989
308.20
On*
OnfO*
OR
Off
Off
OB
Off
Off
Off
Off
Off
Off
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
Cool water
density, Ugal
8.18
8.16
1.16
8.18
1.18
8,18
8.18
8.16
1.18
818
8.18
816
8.16
816
lie
8.16
816
8.16
1.16
8.18
8.18
8.18
8,16
8.16
1.16
lie
6 16
818
8.16
816
816
818
816
816
816
816
816
8,16
816
818
8.18
816
8.16
8.16
8.16
816
6.16
818
8.16
8.16
816
8.16
816
8.16
816
816
818
816
818
1.18
8.18
8.18
8 16
8,18
8.18
816
8.16
1.18
8.18
8.18
8.18
8.15
readng
gprn
8.2
8,2
8,2
82
8,2
8,2
8-2
6-2
82
6.2
62
6.2
6.2
62
6.2
8.2
6.2
8,2
6.2
82
8.2
6.2
8.2
8.2
8.2
8,2
8,2
8?
8,2
62
62
8,2
6.2
6.2
6.2
6.2
82
6.2
6.2
6.2
62
6.2
82
8.2
8,2
62
6.2
6.2
82
8.2
62
8.2
8.2
62
6.2
62
6.2
8.2
62
8.2
62
82
8.J
8.2
8.2
62
82
6.2
8-2
6.2
62
62
-------
FURNACE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE
02-Apr-96
28-Jun-95 RunTTD-IA
time stack exit dlution water in wi
sec F
45856
45916
45976
46036
46096
46156
46216
46276
46336
46396
46456
46516
46576
46636
46896
46756
46812
46872
46932
46992
47052
47112
47172
47232
47292
47352
47412
47472
47532
AVERAGE
12414444 test hrs
61.86667 test min.
2 24:52 hrmvsc
V>J
146
146
146
147
147
147
147
147
147
146
145
146
146
146
146
146
146
146
146
145
145
144
144
144
143
144
144
144
134
F
81
81
81
ao
80
79
79
78
78
79
79
79
80
80
81
81
80
80
79
79
78
78
79
79
80
80
80
BO
79
F
161
161
161
161
161
161
161
161
161
161
161
161
161
161
161
161
161
161
161
161
161
161
161
161
162
161
161
162
161
iter out fire-box ambient stack CO Ngti
F
167
167
167
167
167
167
167
167
167
167
167
167
168
168
168
168
168
168
168
168
168
168
168
168
168
168
168
168
187
F
439
439
438
438
438
436
435
434
433
432
432
432
433
431
430
429
428
427
425
420
418
416
415
415
414
414
414
414
483
F
72
72
72
72
72
72
71
71
71
72
71
71
71
71
71
72
72
72
72
71
72
71
71
71
72
72
72
72
73
F
173
173
173
173
172
172
172
171
171
171
171
171
171
171
171
171
171
171
170
169
169
168
168
168
168
168
168
166
155
ppm
10697
10857
10714
10714
10474
10441
10453
10445
10457
10433
10364
10201
10030
9973
9884
9770
8676
9615
9587
9509
9538
9581
9676
9648
9623
14567
COdkl
ppm
750.2
7500
7471
7554
744.1
733.7
7388
7331
7373
7342
7256
7173
705.6
693.5
8914
8847
6776
673.7
6729
6670
8685
6683
670.2
671.1
6685
CO low
ppm
50106
5011
5011 a
50102
5011
50098
50106
50118
5013
50102
5011.4
5011 8
50094
5010.2
5011.4
5010.2
50126
50122
5011
50102
50126
50098
50114
50134
50118
O2
1318
1318
13.18
132
1325
1325
1325
1329
1331
1331
133
1333
1337
13.4
13.47
13.5
1352
1353
13.54
1369
1385
1387
1381
1383
1384
11.01
CO2 JUM-THC
% ppm
693
689
69
689
6.87
685
685
683
678
679
679
6.77
675
67
68
658
655
655
652
637
624
624
627
627
625
882
Water
balance actual flow rate
heat out
fee gpm Btuflnterval
15 63 30820
15 63
1 63
15 63
1.5 6.3
1.5 6.3
1.5 63
1.5 6.3
1 63
1 63
1 63
1 6.3
1 63
0.5 63
05 63
06 63
05 63
05 63
0.5 63
05 82
05 62
05 62
0.5 82
0 82
0 62
0 62
03 62
0 62
Total Blu out =
Total Blu In =
Efficiency =
Water flowrate =
Bumrate =
Wood moisture =
30820
308.20
30820
30820
308.20
308.20
30820
30820
30820
30820
30820
35957
35957
35957
33560
35957
35957
35957
35443
35443
35443
354.43
35443
303.70
35443
354.43
30370
33088
247.498
533,471
4639%
6.25 i
Draft
Water meter
Cod water readng
On/Off density. Ib/gal
On 815
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
Blu/hf out =
, Btufhr In =
gpm
815
815
815
8.15
815
815
815
8 15
815
815
815
815
8 15
8.15
8.15
815
8 15
815
8.15
815
815
815
815
8.15
8.15
815
a. 15
8 15
19,936
42.972
62
62
62
62
62
62
82
62
62
6.2
62
62
62
62
62
62
62
62
82
61
61
61
6.1
61
61
61
8.1
6.1
2.42 d-yko/hr
21 76%
-------
FURNACE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE Wrted"" 02-Apr-96
^ff-Ajfaj m*! 1 it^-so
time stack eat dkJon water in water otf tire-box ambient
sec *"
1944
2004
2064
2124
2184
2244
2304
2364
2424
2484
2544
2604
2664
2724
2780
2840
2900
2980
3020
3080
3140
3200
3260
3320
3380
3440
3500
3580
3820
3880
3740
O 3800
Jj 3860
OO 3920
3980
4040
4100
4156
4218
4276
4336
4396
4456
4518
4576
4636
4696
4758
4818
4876
4936
4998
5056
5118
5176
5236
5298
5358
5416
5478
5532
5592
5652
5712
5772
5832
5892
5952
6012
6072
r
159
154
152
152
154
155
15?
157
158
159
159
158
157
1S7
158
157
158
158
161
164
188
169
171
174
175
176
174
174
174
176
17?
179
160
182
183
183
183
182
181
181
181
179
179
178
179
179
179
179
182
185
189
192
195
199
200
201
201
201
201
201
201
201
200
201
201
203
205
208
206
207
r-
88
84
83
84
84
84
85
85
85
85
84
83
83
82
82
81
80
80
80
81
82
84
85
86
86
84
83
82
82
82
83
83
85
88
87
88
87
86
84
84
82
82
82
83
83
84
85
86
87
87
87
87
86
87
87
87
87
87
88
89
89
89
88
67
87
87
87
88
88
88
r
153
153
153
154
154
154
154
154
154
154
153
153
153
153
153
153
153
152
152
152
153
152
152
153
153
153
153
153
153
153
153
153
154
154
154
154
155
155
155
155
155
155
155
155
155
156
156
156
156
156
157
157
157
157
157
157
158
156
158
159
159
159
159
159
159
160
160
160
161
161
t-
160
160
160
160
160
160
160
160
159
160
159
159
159
159
159
158
158
158
158
158
158
159
158
158
159
159
159
159
159
159
160
160
160
160
160
161
161
161
161
161
161
162
181
161
182
182
162
162
182
182
163
163
163
163
164
164
184
165
165
165
166
166
168
166
166
166
187
18?
16?
168
t-
236
284
299
313
326
333
335
342
351
350
351
351
348
345
349
359
393
395
394
405
448
435
411
402
402
396
398
400
410
430
473
4?0
446
446
441
444
451
451
456
476
498
496
491
507
540
554
541
545
572
599
601
614
640
671
683
895
708
711
712
718
721
732
7J8
751
75?
765
772
779
791
791
F
89
70
70
70
71
71
71
72
72
72
72
73
73
73
73
73
73
73
72
72
72
72
72
72
72
73
72
72
72
72
71
71
71
71
71
71
72
72
72
72
72
72
71
71
71
71
71
72
71
72
72
72
72
72
72
71
71
71
71
71
71
71
72
72
72
71
71
71
71
71
Mack
F
178
177
175
176
176
176
177
177
177
177
177
176
175
174
174
174
175
175
177
180
182
184
187
189
191
192
191
189
190
191
193
195
196
198
200
201
200
199
198
198
199
198
197
197
197
197
196
197
199
203
207
211
215
218
221
221
221
221
221
221
221
221
222
223
223
225
227
228
230
230
CO high
pprn
7605
11922
17167
18451
15967
15845 '
15499
15564
16048
16325
16349
18496
18520
17110
17788
16205
18107
17208
17114
17692
17664
16420
21847
23584
23315
22607
21749
21867
22119
22306
22878
23881
23488
24422
28929
28381
26375
24996
24797
24040
22734
20726
20146
19836
20658
21432
21741
21916
23405
25435
29704
31587
32174
32629
33370
32987
33258
32894
32418
32263
32487
32467
33000
33350
33936
34644
35893
36979
37150
36560
COtlKj
pom
1425.9
1049.3
1174.3
12S2.1
1158.7
1148.3
1119.6
1107.7
1123.7
1153.3
11646
1159.3
1154.3
1188
1239.1
1286.9
1314.1
1259
11976
1300.5
1276
1272.8
1509.1
1730.3
1759.3
1898.3
1595.1
1572.4
1641.6
1639.3
1893.4
1760-8
1797.5
1782.7
1970.7
2004,4
2002,9
1888.4
1891
18413
17646
15897
14(83
1457.5
1481.9
1577.3
1604
1617.8
16844
1891.1
2003.1
2005.9
20049
2005.2
20042
2004.7
2005.2
2005.2
2004.9
20054
2005.5
2005-2
2005.7
2005.9
2004.6
2005.2
2005.4
2005.2
2006
2005.4
CO low
ppm
5011.8
5011
5010.6
5011
5013
5013
50106
5010.2
5012.2
5010.8
5011.8
5012.2
50126
5009
5010.8
50126
5013.4
5011.8
5012.2
5011.4
5011.4
50106
5010.2
5009.8
50118
5011.8
5012.6
5011.4
5012.6
50114
5010 8
50108
5011.4
5012.8
5011
50122
50073
5009.8
50114
5011
50102
5009.8
5009
50108
5011.8
5011.4
5011
5011
5011
50098
5008.1
5010.8
5011.4
5011.4
5010.2
5008.5
5011.8
5011.4
50118
5010.2
5011.8
50116
5011.4
5009
5011.4
50098
50102
5009
5014.2
5011.4
02
17.07
15,24
1327
12.56
12.12
12.05
1226
12.26
12.27
1238
12.15
12.39
1302
13.08
12.99
1288
12.78
12.03
12.43
1104
10.45
10.72
9.71
8.82
8.79
8.72
926
999
9.95
9.63
9.09
8.54
851
8.19
7.35
7.09
7.89
6.57
888
894
9.07
938
9.89
9.73
9.8
9.94
988
9.92
9.83
9.1
8.12
7.8
7.07
6,54
6.27
6.47
8.65
681
7.07
7.23
7.17
7.31
7.25
7.23
696
6.71
627
5.81
5.39
525
Water
CO2 JUM-THC balance actual Dow rate heat out
% ppfn
323
54
7.14
7.79
8,19
817
795
7,92
7.89
781
8.02
762
7.13
712
7.23
734
7.64
8.2
8
9.61
9.83
9.6
11.01
1148
1147
11.53
1072
10.22
10.38
10.78
11.37
11.91
1182
12.41
13.22
1301
12.05
11.49
11.31
11.26
11.13
1071
10.53
10.5
1042
10.34
104
10.39
1088
1179
12.69
1308
13.56
14.03
14.33
14.09
13.94
1378
13.52
13.39
1346
1333
13.36
13,39
1S.64
13.85
14.27
14.88
15.03
15.06
83.0
83.5
83.0
83.0
83.0
82-5
82.5
82.0
82-0
81.5
81.5
810
810
80.5
80.5
800
80.0
79.5
79.5
79.0
76.7
785
78.0
77.6
77.5
77.0
78.5
765
76.0
75.9
75.5
75.0
745
74.0
73.5
73.1
73.0
72.5
72.0
71.5
71.5
71.0
70.5
70.5
700
69.5
69.0
685
88.0
67.5
87.0
865
660
85-5
65.0
84.5
84.2
63.9
63.0
82.5
62.0
61,5
61,0
605
80,0
59,5
590
58,5
58.0
57.5
gpm 8tu4rtervBl
6,3 380 i
63
8,3
6.3
6.3
8.3
63
6.3
8.3
6.3
63
8.3
6.3
8.3
8.3
8.3
6.3
6.3
6.3
8.3
6.3
83
8.3
6.3
6.3
8-3
8.3
6.3
8.3
63
6.3
6.3
6.3
6.3
6.3
6.3
63
6.3
6.3
6.3
8.3
6.3
6.3
6.3
6.3
8.3
6.3
63
8,3
63
6.3
6.3
63
83
63
63
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
8.3
6.3
63
8.3
63
6.3
3605
3605
3089
3089
3089
3089
308.9
257.4
308.9
309.0
309.0
3090
288.4
3090
2575
257.5
309.1
3091
309.1
257.5
380.6
3091
257.5
309-0
309-0
3090
309.0
309.0
3090
360.5
360.5
3089
308.9
3089
3604
288.2
308.8
3086
308.8
308.8
360.3
308.8
3088
3803
308.7
308.7
308.7
308.7
308.7
3086
308.6
308.6
308.6
3600
380.0
308.5
3599
359.9
287.8
3598
359.8
359.8
359.8
3598
308.3
3597
3597
308.2
3596
Draft
On/Off
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
Water meter
Coot water readng
density, Ib^al gpm
8.17 8,2
617 62
817 6.2
8.17 6.2
8.17 6.2
8,17 6.2
817 62
8.17 6.2
8.17 6.2
8.17 6.2
6.17 82
8.17 6.2
8.17 6.2
8.17 62
8.17 6.2
8.17 6.2
8.17 6.2
8.18 6-2
8.1B 6.2
818 6.2
817 62
818 6.2
8.18 6.2
8.17 62
8.17 6.2
8.17 6.2
8.17 6.2
8.17 6.2
817 62
817 62
817 62
B.17 6.2
817 62
8.17 6.2
8.17 6.2
8.17 62
8.17 6.2
817 62
8.17 6.2
817 62
817 62
8.17 6.2
8.17 8.2
817 62
8.17 8.2
8.17 6,2
817 62
8.17 8.2
8.17 6,2
817 82
8.16 6,2
816 62
816 62
8.18 6.2
816 62
8.18 6.2
8.18 6.2
816 62
8.16 S.2
8.16 6.2
816 62
8.18 6.2
818 62
8.16 8.2
».16 8.2
8.18 8 2
8.16 6.2
•.IB 8.2
815 62
•.IS 6.2
-------
FURNACE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE
02-Apr-96
29-JUT-95
time st;
sec
6132
6192
6252
S312
6372
6432
8492
8552
6812
6872
8732
6792
6852
6908
8968
7028
7088
7148
7208
7268
7328
7388
7448
7508
7S68
7626
7688
7748
7808
7868
7928
H 7988
JrS 8046
*£> <1oe
8168
8228
8284
8344
B404
8484
8524
8584
8644
8704
8764
8824
8884
8944
9004
9064
9124
9184
9244
9304
9364
9424
9484
9544
9604
9660
9720
9780
9840
9900
9960
10020
10080
10140
10200
10260
RuiTTD-18
F
207
206
206
206
205
205
206
206
206
207
207
209
211
213
214
215
216
216
216
215
213
212
210
209
208
207
207
207
184
177
168
160
156
153
150
148
146
144
143
142
140
138
137
135
134
133
132
131
130
129
127
126
125
124
123
123
123
122
122
121
122
121
119
119
118
118
117
117
116
117
89
90
89
89
88
87
88
88
86
86
87
89
90
91
90
89
88
87
88
86
86
86
88
89
89
87
86
84
78
76
75
75
75
75
77
78
78
77
75
74
73
72
73
75
76
78
76
74
73
72
72
72
73
74
74
75
76
76
75
74
72
72
71
72
73
73
74
75
76
78
ralertn water out tre-box ambient
161
162
162
182
163
163
183
183
163
163
184
164
165
165
16S
186
168
166
166
167
186
167
187
168
168
168
188
188
168
169
18S
188
169
188
169
168
169
169
189
188
189
188
188
188
168
167
168
187
167
16S
186
186
165
165
185
165
165
1S5
16S
165
164
165
164
164
164
164
164
184
164
184
F
168
168
169
169
169
170
170
170
170
170
171
171
171
172
172
172
173
173
173
174
174
174
174
175
175
175
175
176
176
176
176
176
176
176
178
176
176
176
176
176
176
176
178
175
175
175
175
174
174
174
173
173
173
17Z
172
172
172
172
172
172
172
171
171
171
171
171
171
171
171
171
F
797
806
813
820
825
828
834
841
850
867
888
804
927
948
951
951
943
939
934
925
931
933
936
944
949
953
955
962
874
751
683
641
609
584
564
546
532
520
507
498
489
482
475
470
464
459
455
449
444
440
437
434
431
429
427
425
422
420
418
418
415
414
412
412
411
410
409
409
408
406
F
71
71
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
71
71
72
72
72
72
72
72
72
72
72
72
71
71
71
72
72
72
72
72
72
71
72
72
72
72
71
72
72
72
72
72
71
71
72
72
72
72
72
72
72
72
71
71
71
71
71
71
72
slack
F
230
229
229 '
229
230
231
231
232
232
233
233
235
237
240
242
243
245
246
245
244
242
241
240
238
237
236
238
236
228
211
198
188
180
175
170
188
163
181
158
158
154
152
150
148
146
144
143
142
141
140
139
137
137
135
135
134
133
133
133
132
132
131
131
130
129
129
129
129
129
129
COH01
ppm
34900
33492
32865
32577
32402
32259
32227
31954
31926
31995
32837
34591
38739
38273
38858
38135
37634
36389
34485
32817
31152
30005
29285
29057
29065
29203
29842
30168
28906
39840
49784
45858
38745
32821
28691
26135
24174
22282
20882
19482
18250
17159
18382
15829
15373
15141
14775
14433
14213
14164
14136
13973
13940
13900
13973
14038
13985
13997
13977
14042
14205
14209
14282
14441
14620
14954
15336
15735
16056
18301
COdkj
Ppm
2005.2
20055
2008.3
2005-5
20063
2005.7
2004.2
2005.7
20055
2005.7
2005.7
2005.5
20054
2005.7
200S.4
2005
2005
2005
2004.9
200S.S
2005.5
2005.7
20082
2004.9
2005.7
2005.4
20046
2005,5
1850.9
10889
1352.2
1173.2
9277
757.3
633.8
558.1
5046
457.8
410.8
378-1
3436
318.2
299
281.3
2699
259.8
252.9
244.1
235.5
2326
228.5
226.1
2222
2198
211.3
210.8
2098
213.7
211.1
209.8
2085
212.7
211.3
211.9
2157
217.9
214.4
219.7
222.7
230.8
CO low
ppm
50094
5012.2
5011.8
5011.4
50126
5010.8
5011
5011
5010.6
5010.8
5011
5010.2
5012.6
5010.2
5013
5009
50102
5009
50088
5009.4
5012.2
5011.4
5010,6
5011.4
5011.8
5007.3
5011
5013
50098
5011.4
5010.2
5010.2
5010.6
5010.2
5012.2
5011
5010.6
5010.8
50118
5011.4
50118
5010.2
5011.4
5013
5012.2
5013.8
5011.4
5009
50114
5010.6
5010.6
5011
5009.8
5011.4
5009.4
5011.4
5013.4
5011
5012.8
5012.2
5011,4
5009.4
5011
5010.2
5010.6
5009,4
5009,8
5011,8
50094
50108
O2
5,51
5,73
5-76
5,74
5.74
5.7
5.64
5,56
5.42
5.25
488
4.41
3.87
3.5
3.27
3.29.
3.21
316
329
3.57
3.91
414
4.34
4.57
4.67
4.74
476
4-73
47
6.27
8.07
9.22
9.77
10.08
10.3
10.44
10.55
10.67
10.64
10.63
10.68
10.73
1082
10.82
10,85
108
10.95
10.95
10.9
1085
1082
10.86
1083
1081
10.89
10.6
10.6
1056
1056
10.54
10.47
10.49
10-54
10-49
10,5
10.45
1039
10.33
10.31
10.27
Water
CO2 JUM-THC Marat actual tow rata hortou
% ppm
14.71
14.43
1432
14.34
14.36
14.41
14.48
14.55
14.71
14.92
15.29
15.8
1633
16.69
16.93
16.92
16.97
16.96
1876
16.44
16.08
15.83
15.58
1S.32
15.17
15.04
14.96
14.92
14.69
13.76
12.87
12.08
11.51
11.05
10.63
1031
10.05
9.78
9.86
9.5
933
9.15
901
8.96
8,89
8,91
886
681
878
8,78
8.75
8.68
8.69
8,72
8.8
888
888
8.91
8.92
895
9.02
9
6.99
9.04
906
9.13
9.22
9.3
933
9.37
57.0
S6.5
56.0
55.5
55.0
54.5
$4.0
53,5
53.0
53.0
52.5
51.5
51,0
50,5
50,0
49.5
490
48.5
48.0
47.8
47.5
47.0
48.5
48.0
45.5
45.0
44.5
44.5
44.0
440
44.0
440
440
44.0
43.5
43.5
435
43.0
430
43.0
430
43.0
43,0
43,0
430
42.9
42-5
42-5
42.5
42.5
425
425
42.5
42.5
42.5
425
425
42.5
42.0
420
420
42.0
42.4
42.5
42.5
426
42.0
42.0
42.0
42.0
gpm Btuirterval
6 3 359.6
8.3
6.3
8.3
6.3
8,3
83
6.3
6.3
8.3
8,3
63
63
6.3
83
83
6.3
6.3
8,3
6,3
6,3
6,3
8.3
8.3
6.3
8.3
8.3
8.3
63
6.3
6,3
63
6.3
6,3
83
6.3
8.3
63
8.3
6.3
6.3
6.3
83
6,3
63
6,3
8.3
8.3
6.3
6.3
8.3
6.3
6.3
6.3
63
8.3
6.3
6.3
6,3
6.3
63
6,3
8,3
6.3
6,3
6,3
8.3
63
6.3
8,3
308.1
359.4
359.4
308.0
359.3
359.3
359.3
3593
3S9.3
359.2
359.2
2873
359.1
359.1
307.7
3589
358.9
358.9
3588
410,2
3588
358,8
358,7
358,7
358,7
358.7
409.9
4099
358.8
3588
409.9
358.8
4099
358.8
3347
358.6
3586
358.6
358.6
3586
4099
409.9
358-7
358.7
410.1
358.7
358.8
3588
410.2
3589
358.9
4104
359.1
359.1
359.1
3591
359.1
335.1
359.1
410.5
307.8
3592
358.2
359.2
359.2
359.2
3592
359.2
359.2
Water malar
Draft Cool water read no
On/On (teraty. Ib/oal
On 8.15
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
OB
on
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
815
8.15
8.15
8.15
8.15
8.15
8.15
8.15
8.15
8.14
8.14
8.14
8.14
•.14
814
8.14
8.14
8.14
8.14
814
8 14
814
8.13
813
8.13
8.13
8.13
8,13
8.13
8.13
8.13
8.13
8,13
8.13
8.13
8.13
8.13
813
8.13
8.13
8.13
6,13
8.13
8.13
8.14
6,13
8.14
8.14
8.14
8,14
8.14
814
814
8.14
8.14
8.14
814
814
814
8.14
8.14
8.14
8.14
614
814
814
814
614
814
gpm
62
62
6.2
6.2
6.2
62
8.2
6.2
6.2
6.2
62
6,2
62
62
8.2
6.2
6.2
6.2
6.2
62
6.2
62
6.2
6.2
6.2
62
62
6.2
6.2
62
82
6.2
62
62
6.2
6.2
6.2
6,2
6.2
62
6,2
6,2
6.2
62
62
6.2
8,2
62
62
62
62
8.2
62
6.2
6-2
6.2
62
62
6,2
62
62
62
6,2
6,2
62
6,2
6,2
62
6.2
6.2
-------
FURNACE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE
02-Apr-96
29-Ju>95 RmTTO-IB
time slackest EfhJjon witerin w
sec
10320
10380
10440
10500
10560
10620
10680
10740
10800
10860
10920
10980
11036
11096
11158
11216
11276
11336
11396
11456
11516
11578
11836
11686
11758
11816
11876
11838
11998
12058
12116
M '2176
V 12236
o 1229S
VJ 12356
12412
12472
12532
12592
12652
12712
12772
12832
12892
12952
13012
13072
13132
13192
13252
13312
13372
13432
13482
13552
13612
13672
13732
13788
13848
13908
13968
14028
14088
14148
14208
14288
14328
14388
14448
F
117
116
116
116
115
114
114
113
113
112
112
112
112
112
112
111
111
111
111
110
109
109
109
109
108
108
108
107
107
107
108
107
107
107
107
106
105
105
105
105
105
105
105
105
105
105
104
104
104
111
110
113
120
130
141
149
157
184
170
174
178
182
165
186
188
189
189
191
191
193
F
75
74
73
72
71
72
72
73
74
75
78
78
75
74
72
72
71
71
72
73
74
74
75
75
73
72
71
71
72
73
74
75
75
73
72
71
71
72
73
73
75
75
74
73
72
71
71
72
72
74
75
76
77
78
80
81
82
83
83
84
85
85
85
8S
84
83
83
83
83
84
F
164
164
164
163
163
163
163
163
163
163
163
183
163
163
162
162
162
182
162
162
162
182
161
162
181
161
161
161
181
161
181
161
181
160
180
160
160
180
160
160
180
160
159
160
159
159
159
1S9
158
158
158
158
158
158
159
159
159
1S9
160
181
181
182
182
182
182
183
163
1E4
164
164
liar »J Itre-bat emUert
F
171
171
170
170
170
170
170
170
170
170
170
170
169
169
18S
169
169
169
189
169
18B
189
168
188
188
168
168
188
168
167
187
167
167
187
167
167
187
167
167
168
166
166
166
168
168
166
186
165
165
165
165
165
185
165
165
165
166
166
167
167
168
188
169
189
170
170
171
171
171
172
F
406
404
402
400
399
399
397
397
396
393
390
388
386
385
384
383
383
382
362
382
382
381
381
380
379
379
379
378
376
375
373
372
370
369
367
366
368
386
388
363
361
359
357
3S6
355
357
359
359
359
387
412
486
584
832
885
719
749
780
746
747
754
782
787
778
791
820
845
860
868
879
F
72
72
72
72
72
72
71
71
72
71
72
72
72
72
72
72
72
72
71
71
71
71
71
72
72
72
72
71
71
71
71
71
72
72
72
71
71
71
71
71
71
72
72
72
72
72
71
71
71
71
70
71
70
71
71
71
71
71
72
71
71
72
72
72
72
72
72
71
71
71
stack
F
128
128
127
127
127
127
128
125
125
125
124
124
124
124
124
123
123
123
122
121
121
121
120
121
121
120
120
120
120
119
119
118
118
118
119
119
118
118
117
117
117
117
117
117
117
117
117
116
116
121
126
133
141
150
160
170
178
186
192
198
202
206
210
212
214
216
216
217
219
221
CON01
ppm
16378
16272
16215
16182
18085 .
15845
15731
15723
15702
15706
15877
15987
16089
16085
15855
15780
15678
15518
15430
15430
15428
15487
15592
15580
15397
15422
15210
15084
14905
14905
15055
1507*
15084
14884
14821
14848
14785
14734
14758
14884
15078
15112
15112
14998
14946
15031
15088
15038
15031
15470
13493
14823
16020
15552
15190
16016
17240
19208
20789
20972
21798
22575
23254
23930
24540
25183
24898
22948
23043
24756
co dm
ppm
235.5
232.1
229.2
224.3
2253
2204
2196
2166
205.2
2098
2048
2093
211.4
2131
212.8
2091
209
203.8
202
2028
185.8
1885
1908
185
1953
1903
1828
1878
168.2
180.2
172.7
178.9
175.6
182
180.5
181.6
179.7
180
1774
168.1
170,1
169.6
1712
1792
178.4
1792
181.2
180,8
1781
3271
813.2
9053
1034
1109
1067.5
1085.6
1144.9
1278.8
1433.4
1503,9
1507.8
1614.4
1653
1738.4
1771.5
1857.7
1867.2
1757.6
1658.9
18192
CO low
ppm
5011
5011.8
5011.4
50118
5013.8
5011
5011,8
50118
5009.6
5012.2
5012.6
5009.8
5012.2
5012.2
50114
50134
50102
5011.8
5010,6
50102
5010.2
5009
5013
5013.4
5012.2
50114
5013
5010-8
5011
50118
5012.2
5014.2
50106
5011.4
5012.6
50122
5012.2
5013
50122
5010.2
5011.4
5011.4
5011.8
5013
5011
50118
5011.8
5013,4
50106
5011.4
5009
5011
5011.4
5012.8
5011
5009.8
5011.8
5008.4
5011.8
5012.2
5010.2
5011
5010.8
5011
5010.6
50106
50122
5012.2
5010.8
5009
O2
10.27
10.3
1024
10.17
10.13
1018
10.19
1013
10.09
10.01
983
10
1003
10.03
10.08
10.06
10.04
10.08
10.07
10.03
10.02
9.92
9.82
9.77
981
9.74
9.81
9.88
995
9.96
99
992
9.96
10.02
10.05
10.1
10.14
10.2
10.18
10.13
10.06
10.17
10.26
1042
10.51
10.53
10.52
10.85
1073
10,49
12.59
1288
11.67
10.29
8.58
721
6.39
5,58
491
4.71
4.18
387
3.79
3.92
4.15
43
4.37
4.43
423
3.82
Water
CO2 JUM-THC balance Mual Dmrate heal out
% ppm
9.38
8.35
94
9.44
9.48
8.39
9.38
8.42
8.46
9.51
8.56
944
9.41
9.39
9.36
9.35
9.36
».35
936
943
8.46
9.55
966
8.7
9.89
9.73
9.86
9.6
9.55
9,54
9.59
9.54
9.52
9.44
9.42
838
9,35
9.3
934
9.39
9.43
9.32
9.23
9.07
8.98
899
8.88
8.89
882
899
7.09
7,33
85
9,83
11,39
12.43
13.2
14,04
14.87
14.86
15.43
15.76
1585
1572
15,48
15.26
15.15
15.1
15.28
15.66
Ibs
41.7
42.0
42.0
420
42.0
420
420
42.0
42.0
420
41.5
41.5
41.5
41.5
415
41.5
41.5
41.5
415
415
41.5
41.5
410
41.0
41.0
410
41.0
41.0
41.0
41.0
41.0
41.0
410
410
410
410
41.0
41.0
410
41.0
410
40.5
40.5
40.5
40.5
405
41.0
41.0
410
41.0
40.5
405
40.4
40.0
39.7
39.5
39,5
39.0
390
38.5
38.0
380
37.5
37.5
37.0
37,0
365
36.5
36.0
35.5
gpm BlLrirtarva!
6.3 359.2
8.3
63
63
6.3
6.3
6.3
6.3
6.3
6.3
83
8.3
6.3
8.3
6.3
6.3
63
6.3
83
6.3
63
63
63
8,3
6.3
6.3
8,3
8.3
63
6.3
8.3
63
63
6,3
6.3
63
8,3
6.3
8.3
63
63
83
6.3
8.3
6.3
6.3
8.3
8.3
63
6.3
6.3
6.3
63
6.1
6.3
63
6.3
8.3
63
8.3
8.3
6.3
6.3
8.1
63
63
6.3
6.3
8.3
6.3
359.2
3079
359.3
359.3
359.3
3593
3593
359.3
359.3
3S83
335.4
3080
3060
358.4
3594
359.4
358.4
3594
3594
3594
359.4
3596
308.1
358.6
359.6
359.8
358.6
3596
308.2
308.2
308.2
308.2
359,7
335.7
358.7
359,7
359.7
359.7
308.3
308,3
308,3
3596
308.3
359.8
359.8
359.8
308.4
359.9
3S9.9
3S99
359.9
359.9
359-9
3084
308.4
359.8
335-8
359.7
308.2
359.6
3081
359.4
3SB.4
410.6
359.3
4107
359.2
359.2
410.5
Water meter
Draft Coot water readna
On/Off density, IMosI
on 8.14
on
Off
on
on
Off
Off
on
on
Off
on
Off
Off
on
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
on
Off
Off
Off
OH
OH
on
on
Off
Off
on
Off
Off
on
on
Off
on
OH
Off
on
on
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
814
8.14
8.15
8.15
8.15
815
8.15
8.15
815
8.15
8.15
815
815
8.15
8.15
8.15
8.15
8.15
8.15
8.1S
8.15
615
8.1S
8.15
8.15
8.15
8.15
815
8.15
8.15
8.15
8.15
8.18
8.18
616
8.18
8 16
8.16
8.16
8.16
816
8.16
8.16
8.16
8.16
8.16
8.18
816
8.18
8.16
616
8.16
8.16
816
8.16
8.16
8.16
816
815
8.15
8.15
8.1S
815
8.15
815
815
814
814
8.14
flpm
8.2
62
62
62
6.2
62
62
6.2
62
82
6.2
62
62
6.2
8.2
6.2
6.2
8.2
82
6.2
6.2
62
62
62
8.2
62
8.2
8.2
62
82
82
62
6.2
8.2
62
6.2
6.2
62
62
8.2
82
6.2
62
62
62
62
8.2
6.2
6.2
8.2
8.2
62
8.2
8.2
6.2
6.2
6.2
6.2
62
6.2
8.2
62
8.2
6.2
62
62
6.2
62
62
8.2
-------
FURNACE A WITHOUT CATALYST-tOW HEAT REMOVAL RATE
02-Apr-96
29-JltvB5
Kme sti
sec
14508
14568
1462S
14688
14748
148G8
14863
14928
14988
15048
15108
15184
15224
15284
15344
15404
1S4S4
15524
15584
15844
15704
15764
15824
15884
15)44
18004
18064
16124
18184
16244
1*304
O 16384
K, 16424
_ 16484
16540
16600
16660
16720
16780
16840
16900
16960
1?020
17080
17140
17200
17260
17320
17380
17440
17500
17580
17820
17680
17740
17800
17860
17916
17976
18036
18096
1815S
18216
18276
18338
18396
18456
18518
18578
18638
Rir>TTD-1B
Bckest dUfon water In WileroU fire-box ambient
P
195
1%
187
198
198
196
185
193
192
189
187
185
185
184
184
164
178
161
149
141
137
134
132
130
128
128
126
125
124
123
123
121
120
118
117
116
115
113
112
111
112
111
110
109
109
108
106
108
105
104
104
104
104
103
104
103
103
102
101
101
100
99
99
99
99
99
99
98
»a
98
h
85
86
86
87
87
86
85
84
83
82
82
83
83
84
85
85
82
78
77
78
75
75
75
75
76
77
78
78
78
78
77
76
76
75
74
75
75
75
76
77
77
77
77
76
75
75
74
74
74
74
75
76
77
77
78
77
75
73
72
72
73
73
74
75
76
77
77
77
76
75
t-
165
165
165
166
166
166
167
167
167
167
167
168
166
168
168
168
169
168
IN
168
168
168
168
169
169
169
169
166
169
168
166
166
168
167
167
187
186
186
166
166
166
166
166
165
185
165
165
164
184
164
164
164
165
164
164
164
164
184
164
163
163
163
163
183
163
163
163
163
163
163
F
172
172
173
173
173
174
174
174
175
175
175
175
175
175
176
176
178
176
176
176
176
176
176
176
176
176
176
176
178
176
178
175
175
175
175
174
174
173
173
173
173
173
173
172
172
172
172
172
172
172
1T2
171
171
171
171
171
171
171
171
171
171
171
170
170
170
170
170
170
170
170
F
886
890
906
946
940
i33
920
900
897
888
878
875
876
872
868
872
840
755
694
649
618
595
576
582
548
537
525
518
507
500
493
487
482
477
473
461
418
483
459
455
451
448
444
439
435
432
428
426
424
421
418
416
414
412
410
406
405
403
401
399
398
396
394
393
391
387
385
363
361
379
F
71
71
72
72
72
72
72
72
72
72
71
71
71
72
71
72
72
73
72
72
71
71
71
71
71
71
71
72
72
72
72
72
72
72
71
71
71
71
72
72
72
72
72
72
72
71
71
71
71
71
71
71
72
72
72
72
72
72
72
72
71
71
71
72
72
71
72
72
72
72
stack
F
223
224
226
228
228
227
225
222
220
218
216
214
214
214
213
213
209
194
179
169
161
156
151
147
144
142
140
139
138
137
135
134
132
131
129
128
127
126
126
125
124
123
123
122
121
120
119
118
118
117
117
116
116
115
115
115
115
114
114
113
112
112
112
111
111
111
111
111
111
110
CONdl
ppffl
25916
27010
28475
27250
25806
25458
24064
22953
22298
20911
20011
19360
18994
18852
18652
18351
17973
18823
33757
39010
37708
35820
33258
30770
28434
26546
24793
23348
21936
20703
19560
18433
17550
16716
16016
15448
14893
14482
141T2
13794
13546
13265
12918
12545
12329
12166
11991
11902
11816
11812
11755
11764
11735
11678
11890
11625
11507
11418
11292
11198
11189
11161
11267
11340
11349
11401
11344
11292
11178
11039
COdkj
ppm
1923.3
19954
2005.4
1989.8
1913.2
1M8.5
1797.4
16867
1646.5
1548
14S2.8
1313.2
1371.6
1351.7
1334.3
1326.8
1295.2
»94.5
577.6
772.1
737.8
6914
6388
570.1
512.4
460.3
419.3
3833
353.4
3255
305-7
2S1J
2651
242.2
231.4
220.4
208.3
194
184.1
1784
1706
165.4
165.4
155.3
153
1468
145.3
142.3
140.1
134.4
131.7
132
128.9
128.6
126.1
126.3
128.9
127.3
12?
122.2
125.3
116.9
117.7
118
115.4
1149
1133
1144
1165
113.4
CO low
ppm
50094
5010.2
5011
50122
50106
5009.4
5011.8
5011.4
5010.6
5011.4
5010.8
5011.4
5012.2
5013
5010.6
5011
5009.4
5011
501 J
50114
5009
50126
5008.5
5013
5011.4
5011
5010.2
5011.8
5011
5009.8
5011.4
5012.6
50106
5009.4
5010.6
5010.2
5010.6
5014.2
5009.8
50114
5011.4
5011.8
5012.6
5012.6
5011.8
50126
50114
5010.6
5013.4
5012.2
5010.6
5009.8
5011.8
50114
50098
5011.8
5011.8
5009.4
5013.8
5012.2
5011
501 1.6
5011.4
5009.4
5012.2
5010.6
5013
5011.4
50126
5013
O2
%
343
336
3.66
3.69
354
402
446
486
533
5.74
6.52
7.13
725
7.15
7.17
7.26
7.36
8.51
794
769
813
669
8.99
9.11
9.21
9.23
929
928
932
9.34
9.36
9.43
9.45
944
9.46
9.45
9.47
9.43
937
9.36
9.3
928
936
9.53
9.56
959
9.63
963
9.62
9.61
9.57
952
9.47
9.47
943
9.44
9.5
956
9.66
9.78
9.81
S.86
9.78
9.72
9.69
9.65
963
9.67
9.73
Ml
Water
CO? JUM-THC balance actual low rale heatoJ
% ppm
16
16.05
15.62
15.69
15.82
15.34
14.99
14.66
142
13.81
13.1
12.61
1257
1268
1264
12.59
12.49
11.34
12.21
1263
12.32
1178
11.45
11.29
11.14
11.06
10.94
10.84
10.73
10.83
10,48
10.35
10.28
10.19
10.1
10.07
10
10
10
9.98
9.99
9.97
9.83
9.67
9.8
9.55
9.46
9.48
9.46
9.48
9.5
9.54
9.55
9.55
9.59
9.58
951
945
9.36
9.28
9.24
9.19
9.27
933
9.36
8.39
9.39
9.37
93
923
IDs
35.1
35.0
34.5
34.5
34.0
335
33.5
33.5
33.0
33.0
33.0
32.5
325
320
32.0
31.5
31.5
31.5
31.5
31.5
31.5
31.5
31.5
31.0
31.0
310
310
310
31.0
31.0
31.0
31.0
31.0
31.0
31.0
31.0
310
30.5
305
305
30.5
30.5
30.5
30.5
30.5
30.5
305
305
30.5
30.5
30.5
30.5
305
305
30.5
30.5
305
30.5
30.5
30.5
30.5
30.5
30.5
30.0
30.0
30.0
30.0
30.0
300
30.0
gpm BtuAnterval
6.3 359.1
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
8.3
6.3
6.3
63
6.3
6.3
8.3
8.3
63
6.3
63
6.3
6.4
8.4
64
84
64
6.4
6.4
64
8.4
6.4
64
6.4
6.4
6.4
6.4
6.4
6.4
84
6.4
6.4
6.4
8.4
6.4
64
64
6.4
6.4
6.4
6.4
6.4
6.4
6.4
6.4
8.4
8.4
6.4
6.4
6.4
6.4
64
6.4
6.4
6.4
6.4
64
6.4
6.4
6.4
3591
410-4
358.9
358.9
410.2
3588
3588
410.1
410.1
382.7
358,7
3587
3587
409.9
409.9
3588
409.9
358.8
409.9
409.9
409.9
41S.8
383.7
363.7
3637
3637
415.8
3637
4158
415.8
363.8
363.8
3882
415.9
3639
416.1
364.1
364.1
3641
3641
364.1
364.1
364.2
3642
3842
3642
4164
416.4
416.4
416.4
3643
312.2
3643
364.3
364.3
340.0
364.3
3643
416.5
4165
416.5
3845
384.5
3645
364.5
3645
364.5
364.5
384,5
Water meter
Draft Cod water read no
On/on density, (ti/ga
On 8.14
On
On
On
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Oft
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Oft
Off
Off
Oft
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Oft
Oft
Off
Off
Off
Off
on
Off
Off
Off
Off
Oft
Off
on
Off
Off
Off
Off
Off
on
Off
814
8.14
8.14
8.14
6.14
8.14
814
6.14
8.14
8.14
813
8.13
813
8.13
8.13
8.13
8.13
8.13
813
813
813
813
8.13
8.13
8.13
8.13
6.13
8.13
8.13
8.13
8.13
8.13
8.14
8.14
8.14
8.14
8.14
8.14
8.14
6.14
814
6.14
8.14
8.14
8.14
814
8.14
8.14
8.14
8.14
6.14
8.14
8.14
8.14
814
6.14
8.14
8,14
815
8.15
8.15
815
B.1S
8.15
8.15
815
6.15
6.15
8.15
opm
62
62
6.2
8.2
82
6.2
6.2
6.2
8.2
8.2
6.2
62
62
62
6.2
6.2
6,2
8.2
6.2
8.2
6.2
6.2
6.3
8.3
6.3
8,3
6.3
6.3
8.3
63
63
8.3
63
63
6.3
83
8.3
8.3
6,3
6.3
6.3
6.3
63
6.3
6.3
6.3
6.3
63
6.3
8.3
6.3
8.3
8.3
6.3
6.3
6,3
6.3
83
6,3
6.3
6,3
6.3
8.3
8.3
6.3
6.3
6.3
63
63
6.3
-------
FURNACE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE
02-Apr-86
29-JltvSS RuiTTD-IB
time tticNeat dlubon walirln watweut Ire-box »mUert
sec
18S96
18756
18816
18876
18836
18996
19058
1911B
19176
19236
19292
19352
19412
19472
19532
19592
19652
19712
19772
19832
19892
19852
20012
20072
20132
20192
20252
20312
20372
20432
20492
j 20552
^ 20612
j 20668
20728
20788
20848
20908
20968
21028
21088
21148
21208
21268
21328
21388
21448
21508
21568
21628
21688
21748
21808
21868
21928
21988
22044
22104
22184
22224
22284
22344
22404
22464
22524
22584
22644
22704
22764
22824
h
98
97
96
95
95
94
85
95
94
94
95
95
95
94
94
94
94
93
83
92
82
82
92
92
93
92
92
92
92
92
92
91
91
91
91
91
91
95
102
109
116
121
126
128
131
133
138
138
139
140
141
142
143
143
144
145
146
147
148
149
150
151
151
152
153
153
153
153
154
155
I-
74
74
73
73
73
74
75
76
77
77
77
78
78
77
76
75
74
74
73
74
74
75
76
77
77
77
76
74
73
72
72
73
73
74
75
76
76
77
79
80
80
79
78
78
78
77
78
79
79
80
81
80
79
79
78
78
78
78
80
81
82
81
81
80
78
79
79
78
79
80
F
163
162
162
162
182
1*2
162
162
162
162
162
162
161
161
161
161
161
161
160
161
160
160
180
160
160
160
160
160
158
158
159
159
158
159
159
158
159
159
158
159
158
158
158
158
158
158
159
158
158
156
158
158
158
158
158
158
158
158
159
159
159
158
159
159
159
159
159
159
180
160
F
170
169
168
169
169
188
168
168
168
168
168
188
168
168
168
168
167
168
187
167
167
167
187
167
167
166
186
166
168
166
166
166
165
166
165
165
165
165
165
165
185
165
164
184
164
164
184
164
164
165
165
164
165
185
165
165
165
185
165
166
168
tee
166
166
166
168
166
166
167
168
r
377
375
373
372
371
370
369
387
367
365
364
362
361
359
357
356
356
355
354
353
352
351
351
350
34S
347
346
345
344
343
343
342
342
341
341
339
339
332
340
389
409
449
473
493
518
547
576
595
811
623
636
647
660
681
869
659
658
663
669
877
687
695
700
702
701
701
702
701
704
704
F
72
71
71
71
70
71
71
71
71
71
71
72
72
72
72
72
72
72
71
71
71
71
71
71
72
72
72
72
72
71
71
71
71
71
71
71
72
72
72
72
72
72
72
72
72
71
71
72
72
72
72
72
72
71
71
71
71
71
71
71
72
72
72
72
72
71
71
71
71
71
st«* CON0
F
110
109
109
108
108
108
108
108
107
107
107
107
107
107
107
107
106
106
108
105
104
105
105
105
105
105
105
105
104
104
104
104
104
104
104
104
104
107
118
125
132
138
142
146
149
152
155
157
159
161
182
163
165
166
167
168
168
169
171
172
174
175
175
175
176
176
176
177
178
179
ppm
10895
10982
10881
10880
10897
11003
11137
11186
11231
11267
11300
11312
11308
11239
11100
11084
11084
11011
11047
11068
11113
11218
11318
11422
11471
11499
11544
11503
11410
11235
11168
11202
11182
11320
11430
11564
11719
11983
10262
10291
11979
13070
13473
12487
12720
13131
13928
14535
15007
15609
16227
16630
17049
17348
17139
16968
17745
18323
18661
19088
19340
18901
18213
18380
18713
18974
19214
19169
19242
19194
COdlu
ppm
1123
1118
111.8
110.5
109.7
1051
105
105.3
1032
1038
1045
1025
1025
108.7
108.1
107.1
1086
103.7
103.4
108.8
99.3
100.6
99
98
101.4
98
100.1
104.2
108.1
106
1007
1069
99.9
991
97.5
98.5
98
147.9
860.2
884.7
800.5
8636
8382
845.5
880.2
873
913.1
854.3
887.3
10168
10594
11043
11331
11701
1188.3
1174
1154.5
1209
1247.6
1269.9
1300.1
132S.5
1307.8
1250.3
12846
12876
1310.4
1330.8
1327.8
13281
CO low
pom
5010.6
50118
50114
5009.8
5011.8
5012.6
5011.8
50138
5011.4
50138
50114
5010.6
5011
50102
50122
50114
5011
5010.2
5012.2
5011.4
5011
5013
50114
5010.6
5011.8
5010.6
5011.4
5010.2
5011
50122
50122
5011.8
50118
50122
50122
5011.4
5011
5009
5010-2
50098
5010.6
50114
50126
5011.8
5011.8
50118
5012.2
50118
50126
50106
5012.2
50122
50102
50102
50094
5012.6
5011
5011.8
5011
5010.2
5010.2
5011.4
5011.8
5013
50098
501 1.4
5010,2
5012.2
50098
5008.4
O2
988
8.87
8.85
999
10
8.84
9.82
976
974
974
9.75
9.75
9.77
984
9.98
10.02
10.01
10.08
10.11
10.12
10.08
10.03
10
9.88
9.88
9.88
9.84
9.86
9.94
10.1
1017
1021
1026
1017
10.13
1002
993
972
1139
143
14.12
13.46
12.83
13.13
12.98
12.78
12.41
12.2
12.07
11.94
1178
11.71
11.64
1153
1147
117
118
1173
1164
11.52
11.38
11.29
11.36
11.35
11.34
11.29
1127
11 15
11
10.96
OO2
92
92
913
9,1
811
9.17
9.28
9.38
9.36
9.36
9.35
9.33
9.32
9.25
9.13
9,11
912
906
9,07
907
9,1
9,18
919
9.25
9.27
931
935
8.33
826
9.14
909
908
9.06
914
919
927
9.38
9.57
8.08
6.02
6.42
7.09
7.54
7.28
7.42
f.83
792
807
816
8.27
8.4
8.47
854
8.61
8.88
846
8.34
8.38
8.5
881
872
882
871
8.68
8.72
8.8
885
6.97
911
9.18
Water
ce actual flowrate hestcxJ
gpm BMhtervai
300
30.0
300
30.5
30.3
300
300
300
300
300
300
300
300
300
300
300
300
300
300
300
30.0
30.0
30.0
300
30.0
300
30.0
30.0
30.0
300
300
300
30.0
300
300
300
30.0
29.5
29.5
29.5
295
29.5
295
295
29.0
29.0
29.0
29.0
28.5
285
285
285
285
28.5
28.5
280
260
260
275
27.5
27.3
27.0
27.0
27.0
27.0
27.0
26.5
28.5
26.5
26.0
64
6.4
8.4
64
8.4
64
84
8.4
6.4
S.4
6.4
6.4
6.4
64
6.4
6.4
84
6.4
6.4
6.4
8.4
6.4
6.4
6.4
64
6.4
6.4
6.4
6.4
64
64
8.4
63
6.3
6.3
6,3
63
83
63
63
8.3
6.3
8.3
8.3
63
63
63
6.3
6.3
6.3
6.3
6.3
63
6.3
6.3
6.3
63
6.3
8.3
8.3
6.3
8.3
6.3
8.3
63
63
6.3
63
6.3
6.3
364.5
364.8
364.6
364.6
364.6
364.6
364.6
364.6
312.5
291.7
312.5
312.5
364.7
364.7
384.7
364.7
312.6
364.7
3648
3128
384.8
364.8
364.8
364.8
364.8
3127
312.7
312.7
384.9
3649
364.9
364.9
2878
3598
3084
308.4
308.4
308.4
359.9
308.4
359.9
359.9
308.5
308.5
308.5
308.5
308.5
308.5
306.5
3599
359.9
308.5
359.9
3599
359.9
335.9
359.9
358.8
308.4
359.8
359.8
3598
359.8
359.8
359.8
359.8
359.8
3598
359.7
308.3
Water meter
Draft Cod water rearing
OrtOff density, IbJ&al
Off
OB
Oft
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
on
on
Off
on
on
Off
Off
on
Oft
Oft
Oft
Oft
on
Off
Off
Off
on
Off
on
Off
Off
Off
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
8.15
8.15
8.15
8.15
815
8.15
815
8.15
8.15
8.15
8.15
815
815
8.15
815
8.15
8.15
8.15
8.16
8.15
8.18
8.16
8.16
8.16
8.16
618
816
816
616
6.16
616
816
816
816
816
816
816
816
8.16
8-16
816
8.16
8.16
816
8.16
818
816
816
816
816
816
8.16
8.16
816
8.16
816
816
8.16
816
8.16
8.16
816
816
816
8.16
8.16
816
8.18
8.16
8 16
gptn
6.3
6.3
6.3
6.3
8.3
6.3
6.3
6.3
8.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
83
6.3
63
8.3
6.3
6.3
6.3
6.3
8.3
6.3
6.3
6.3
6.3
6.3
6.2
6.2
6.2
6.2
62
6.2
52
8.2
8.2
6.2
8.2
6.2
6.2
8.2
8.2
8.2
62
6.2
62
62
6.2
6.2
6.2
82
6.2
6.2
6.2
6.2
8.2
8.2
6.2
6.2
6.2
6.2
6.2
62
62
6.2
-------
FURNACE A WITHOUT CATALYST-tOW HEAT REMOVAL RATE
02-A|jr-96
29-Ju>95
time st
see
22884
22944
23004
23064
23124
23184
23244
23304
23364
23420
23480
23540
23800
23860
23720
23780
23840
23900
23980
24020
24080
24140
24200
24260
24320
24380
24440
24500
24580
24620
24680
t) 24740
TT 24796
t^j 24656
24916
24976
25036
25096
25156
25218
25278
25336
25396
25458
25516
25578
25838
25698
25756
25816
25876
25938
25996
26056
26116
26172
26232
26292
26352
26412
26472
26532
28592
26652
26712
28772
28832
28892
26952
27012
RmTTD-18
«cke«it dUion water In water out flre-tox amWent
F
157
157
157
157
1S6
156
158
156
158
156
156
158
156
156
156
156
156
156
158
155
156
155
154
154
153
153
153
153
153
153
154
154
154
154
154
155
155
155
155
158
156
158
157
157
157
157
157
157
157
158
156
156
158
156
156
157
158
158
159
159
160
160
160
160
160
180
160
160
160
160
f-
81
82
83
82
82
80
79
79
79
79
79
79
81
81
82
83
83
83
83
82
81
80
79
79
79
78
79
81
81
82
83
83
83
82
80
80
80
79
79
80
81
82
82
83
S3
81
80
78
78
79
79
80
81
82
83
83
83
82
81
60
78
77
78
78
78
79
80
81
82
82
F
160
160
160
161
160
181
180
161
161
161
181
181
161
161
161
162
162
182
162
161
162
181
162
182
161
162
162
162
162
162
162
162
162
162
162
162
162
182
162
163
163
163
163
183
163
163
183
163
163
183
183
163
163
164
164
164
164
164
164
164
164
164
164
164
164
164
164
165
165
165
F
167
16?
18?
167
167
16?
187
187
187
168
18S
188
188
168
168
168
168
168
168
168
168
169
188
189
189
169
169
169
169
169
169
169
169
169
169
169
169
189
170
170
170
169
170
170
170
170
170
170
170
170
170
170
170
170
170
171
171
171
171
171
171
171
171
171
172
171
172
171
172
172
F
706
708
718
720
717
714
714
715
720
719
718
713
710
708
707
703
699
695
691
691
688
682
678
878
869
666
864
663
882
681
661
662
681
685
881
655
660
671
674
663
853
648
646
645
840
638
838
838
838
634
640
650
648
843
633
624
622
623
627
629
831
634
637
640
639
632
629
629
628
630
F
71
72
72
72
72
72
72
72
71
71
71
71
71
71
72
72
72
72
72
73
72
72
72
72
71
71
71
71
71
72
72
72
72
72
72
72
72
72
72
72
71
72
72
72
72
72
72
72
72
72
71
71
71
71
72
72
72
72
72
72
72
72
72
71
71
71
H
71
71
71
stack CON*
f
180
182
182
182
181
160
180
180
180
180
180
180
180
180
180
181
180
180
180
179
179
178
178
178
177
177
177
177
178
178
178
178
178
178
178
179
178
160
180
181
180
181
181
182
182
162
182
182
181
181
180
180
160
180
180
181
162
182
183
183
183
183
184
183
183
183
184
184
184
184
ppm
18840
18478
• 19177
19251
19198
19287
19352
19413
19198
18608
18534
18579
18734
18866
18665
18490
18445
18578
18583
18644
18730
18616
18848
16962
19917
18579
18368
18298
16127
17957
17851
17651
17574
17505
17582
17623
17683
18180
18095
18005
18201
18510
18722
18876
18998
19047
19019
18815
18791
1883S
18921
18380
18648
19214
19450
19535
19405
18202
19047
18861
18351
18184
17839
17537
17328
17249
17680
17896
17835
17839
COdkj
ppm
1328-9
1301-3
1318.1
1329.6
1333.3
1333.3
133S9
1341.5
1345.5
1320.5
1281.4
1276.5
12863
12974
13006
1285.5
1273.4
1275.7
1285.2
1285
1288.6
1287.1
1284.7
1306
1307.3
1288.3
1286.6
1259.9
1255.2
1241.7
1226.4
1220,7
1207.4
1204.4
1207.5
1208.7
1219.6
1238.8
1259.1
1248.4
1239.3
1255.4
12803
1294.1
1303.9
1314
1318.6
1309.1
1293.9
1299.8
1307.3
1314
1288.7
1300.5
1338.S
1355.8
1366.7
1356.4
1336.8
1327.1
1294.9
1276.5
1260.3
1236.3
1221.4
1201.2
1191,6
1224.9
1239.8
1241.7
CO low
Ppm
5011.4
5009
5009.4
5011.8
5011.8
5013
50098
50114
5010.6
50102
5009
50102
5011.8
50118
5011.4
5010.6
50098
5011
50114
50106
5010.2
501 1.8
5011
5009
5012.8
5010.8
5010.2
5006.5
5012.2
5012.6
5011.4
5011.8
50098
5012.6
50122
5011
5011.4
5009.8
5010.6
5013
5011
50094
5011
50094
5010.8
5010.6
5011
5013.8
5012.2
5009
5011.8
50098
50102
5011.4
5011.8
50102
5012.2
5011.4
50106
5011.4
5014.2
5010.2
5011
5011
5010.8
5011.4
5010.8
5011.4
5011.4
5013
O2
10.86
10.88
10.95
11.06
11-18
11-18
11.19
11.21
11.18
11,11
11.17
11,24
11,31
1133
11.3
11.26 .
11.29
11.38
11,41
1146
11,48
11,47
11.56
11.57
11.59
11.64
11.65
11,64
11.82
11.6
11.56
1155
1152
11.52
11.45
11.32
11.06
11.05
11.17
11.22
11.16
11.15
11.2
11.28
11.24
1122
11.1?
11.14
11.23
11,28
11.29
11.39
11,56
11.68
11.64
11,5
11.37
11.26
11.21
11.07
10.97
1095
10.83
10.73
10.7
10.72
1092
1095
10.93
11
Water
CO2 JUM-THC balance actual (low rate heat out
% ppm
931
926
9.22
8.1
9.03
9
89?
8.94
698
9,02
89?
8.85
8.77
8.71
675
876
872
8,64
8.57
8.51
8.49
8.48
8.36
8.34
833
8.3
831
8.33
8.33
8.3?
6.4
8.4
8.44
844
8.49
8.64
885
884
8.73
8.73
8.79
883
88
8.77
8.81
8.85
6.9
«.95
8,84
8,81
8.8
8.72
854
8.48
8.54
8.67
$.82
$.93
8,98
9,14
9,21
9,24
9,36
9.44
9.49
9.45
9.25
924
9.24
9.1 8
Ibs
280
25.5
25.5
25.5
25.0
25.0
25.0
250
250
24.5
24.5
245
24.0
240
24.0
235
235'
23.5
230
230
230
230
23.0
22.8
22.5
22.5
22.5
22.0
22.0
22.0
21.5
21.5
21.5
21.5
21.4
21.0
210
210
21.0
20.5
20.5
20.5
20.0
20.0
19.5
19.5
19.5
19.5
19.5
19.5
19.0
1S.O
19.0
18.5
165
18.0
18.0
17.5
17.5
17.5
17.0
17.0
17,0
17.0
17.0
16.5
18.5
18.0
16,0
18.0
gpffl Btulnterval
6.3 359.7
8.3
8.3
6.3
6.3
8.3
8.3
8.3
63
6.3
8.3
8.3
6.3
6.3
6.3
6.3
6.3
63
63
6,3
8,3
8,3
63
8.3
8.3
8.3
63
6.3
8.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6,3
6,3
6.3
6.3
6.3
6.3
8.3
6.3
6.3
6.3
8.3
6.3
8.3
6.3
6.3
6.3
8.3
63
6.3
6.3
6.3
B.3
6.3
8.3
8.3
8.3
8.3
6.3
63
6.3
8.3
6.3
6.3
63
359.7
369.7
3082
359.7
308.2
359.7
308.2
287.7
359,6
359.6
3596
359.6
359.6
359.6
308.1
3081
306.1
306.1
359,6
308.1
4109
3081
358.4
410.9
3594
359.4
358.4
359,4
3594
359,4
335.5
359.4
3594
359.4
359.4
359.4
359,4
416.8
359,3
359.3
308.0
359.3
359.3
359.3
359.3
359.3
359,3
359,3
359.3
359.3
359.3
359.3
307.9
287.4
359.2
359.2
359.2
359.2
359.2
359.2
359.2
359.2
359.2
410.5
359.2
410.5
30?.8
359.1
359,1
Water meter
Draft Cod water reatSra
Crvoff dHTsMy.lWflal
On 8.16
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
8.16
8.16
8.15
8.18
8.15
816
8.15
8.15
8.15
8.15
8.15
8,15
8,15
8,15
8,15
8,15
8.15
8.15
8.15
8.15
8.15
8.15
815
815
8.15
8.15
8.15
815
815
815
8.15
8.15
815
815
815
815
815
8.15
8.15
8.15
8.15
815
8.15
8.15
8.15
8.15
815
815
815
8.15
6.15
815
814
8.14
814
814
8.14
8.14
8.14
8.14
8.14
8.14
8.14
814
8.14
8.14
8,14
8,14
8,14
gpm
6.2
8.2
6.2
62
8.2
8,2
82
82
62
6.2
6.2
6.2
8,2
62
6.2
6.2
6.2
6.2
6.2
6.2
6,2
8.2
8.2
6,2
6,2
6.2
62
62
62
6.2
6.2
6.2
6.2
62
62
62
6.2
82
62
6.2
62
6.2
62
6.2
8.2
8.2
62
6,2
6,2
8.2
6.2
6.2
6.2
6.2
62
6.2
8.2
6.2
62
6,2
6.2
6.2
82
8.2
6.2
62
62
6.2
62
6.2
-------
FURNACE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE
02-Apr-96
29-Jl/>95 RuiTTD-18
time stack eidt dtubcn waterln waferoti 1Sre~bQx ambient
sec
27072
27132
27192
27252
27312
27372
27432
27492
27548
27608
27888
27728
27788
27848
27908
27968
28028
28088
28148
28208
28268
28328
28388
26448
28508
28568
28628
28666
28748
28808
28868
O 28924
X 28984
TT 29044
29104
29164
29224
29284
29344
29404
29484
29524
29584
29844
29704
29784
29824
29684
29944
30004
30064
30124
30184
30244
30300
30360
30420
30480
30540
30600
30880
30720
30780
30840
30900
30980
31020
31080
31140
31200
F
160
160
161
181
161
181
162
162
161
161
160
160
160
160
180
160
160
160
160
181
161
181
160
160
159
159
159
160
160
161
161
160
161
162
162
162
162
181
161
161
160
160
159
159
160
155
143
134
128
124
121
119
117
116
114
113
111
109
108
107
105
105
104
104
103
103
102
102
101
100
F
83
83
84
84
84
84
83
83
62
61
80
60
79
60
60
82
82
83
83
62
81
80
60
79
79
80
80
81
62
83
63
64
84
64
84
85
64
83
62
61
81
80
80
80
81
79
76
78
79
79
79
79
76
77
76
75
75
74
74
74
75
76
77
77
77
78
78
77
76
75
F
185
185
185
165
165
185
166
165
166
166
166
166
166
166
186
168
166
168
167
167
166
167
167
167
187
187
167
187
167
167
167
167
167
166
168
168
186
168
168
188
168
188
168
168
168
168
169
169
169
169
169
169
169
168
168
168
168
188
168
188
188
166
169
169
188
168
168
168
167
167
F
172
172
172
172
172
172
172
173
173
173
173
173
173
173
173
173
173
174
174
174
174
174
174
174
174
174
174
174
174
174
175
174
175
175
175
175
175
175
175
175
175
175
175
175
176
176
176
176
176
176
176
176
176
176
178
178
176
178
178
175
176
176
178
175
175
175
175
175
175
175
F
630
623
631
633
640
645
651
651
652
656
659
660
658
654
848
645
843
644
642
644
643
641
645
644
636
829
828
626
827
628
628
632
637
639
635
836
638
626
838
637
632
629
626
828
833
644
«14
582
563
545
531
518
507
499
490
483
476
466
462
457
451
446
442
436
434
426
425
420
418
413
F
72
72
72
72
73.
n
73
72
72
72
72
71
71
71
71
71
71
72
72
72
72
72
71
71
70
70
70
70
71
71
71
71
72
72
72
72
73
73
72
72
72
72
71
71
71
71
71
71
71
72
72
72
73
72
72
72
72
71
71
71
71
71
71
71
72
72
72
72
72
72
sta* COHdl
F
184
185
185 .
185
185
185
188
186
185
185
164
184
184
184
164
184
184
184
185
185
185
185
185
185
184
184
184
165
185
165
186
186
186
187
167
187
167
187
187
166
187
186
166
185
186
163
173
182
154
147
143
139
136
133
131
129
127
125
123
122
121
120
119
119
118
117
117
116
116
115
ppm
17785
17878
17872
17839
17497
17086
16777
16333
18146
15975
15938
15857
15698
15890
16215
16431
18488
16695
16850
18870
16793
16996
17045
17236
17688
18421
18713
19308
19764
19946
20134
20190
20215
19674
19428
19535
18831
18838
19466
18518
18378
18258
18420
19177
18933
17879
16026
26042
34438
35026
32971
30448
28149
25985
24296
22571
21033
19670
18404
17415
16642
15975
15470
14913
145*7
14217
13684
13615
13302
12988
COdkl
1242.5
1231.1
1229
1236.7
1228
1217.8
11885
1166
1132.2
11239
1115.4
1109
11043
10936
11017
1117.8
1134.1
1141
1159.2
1168.6
1171.8
1169.1
1182-9
11918
1195
1225.1
1279.1
1292.2
1333.7
1371.3
13*8.7
1404.1
14118
1416.7
1379.2
1352.1
1362,8
13118
12926
1360
1284
1275.8
1266.1
1278.2
1330.4
1310.2
1068.5
365.4
487.6
561.2
542.8
4937
444.3
4036
368.2
331.7
301.8
274-3
250.5
228.7
2083
194.3
181.8
175.5
165.7
1584
152.2
154
147.6
1471
CO low
ppm
5011,4
5010.6
5012.2
5011.4
5010.2
50102
50106
5010.2
5010.2
5011
50126
5009.4
50106
50114
50106
50094
50102
50106
5009
5010.6
5010.2
5011.4
5010.2
50106
5012.2
5009.4
5008.5
50118
5011.4
50094
5011
5011.8
5009.6
50096
50102
50114
5011
50126
5010.6
5010.8
5011.4
5010.2
5012.2
5009
501 1.4
50094
5009.8
5010.6
5011.6
5011.8
5011
50094
50114
5009.4
5010.6
50118
50126
50098
5013
5012.8
5013.4
5013.4
5012.8
5012.8
5011.8
5012.2
5011.4
5013.4
5010.2
5011
O2
10.96
10.95
10.96
10.93
10.87
10.87
10.61
10.46
10.45
10.45
10.44
1049
10.52
1064
10.75
10.79
10.78'
10.76
10.74
10.74
10.71
10.69
10.75
10.83
10.94
11-06
10.97
11.07
11.08
11.04
11.06
1104
11.02
1085
1075
10.85
10.75
10.87
11
10.72
10.77
10.75
10.93
11.01
10.86
10.85
11.36
9.59
815
6.08
6.25
838
847
86
8.67
8.8
8.85
8.89
8.96
8.93
8.68
8.66
8.78
8.79
873
87
875
872
884
6.97
Water
CO2 JUMTHC balance acU tow rate twetoJ
% ppm
9.2
9.19
9.17
9.2
9.24
9.44
948
963
962
9.62
9.82
958
9.53
9.39
8.31
8.26
9.28
9.29
9.29
9.3
9,31
9.32
828
9.18
9.08
8.95
9.04
892
8.94
8.95
6.92
8.94
695
9.15
9.21
9.08
9.16
9
893
916
909
9,05
884
8.77
8.9
9.1
8.43
10.32
11.39
11.37
11.2
11.1
10.96
10.84
10.74
1058
1045
10.34
10.21
1015
10.14
1012
10.13
10.08
10.1
10.07
10.01
1001
9.87
975
15.5
15.5
15.5
150
ISO
150
14.5
145
145
145
14.0
140
140
140
13.5
13.5
13.5
13.0
130
13.0
13.0
12.5
12.5
12.5
12.5
12.1
12.0
12.0
115
11.5
11.5
11.3
11,0
110
107
10.5
105
10.5
10.0
10.0
10.0
10.0
10.0
10.0
9.5
9.5
9.5
95
9.0
90
90
9.0
90
90
90
90
9.0
93
9,0
90
9-0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
90
9.0
gpm BaJIntervai
8,3 359,1
6,3
6.4
6.4
6,4
64
64
6.4
8.4
64
6.4
6.4
6.4
6.4
64
64
64
6.4
8.4
6.4
8.4
8.4
84
8.4
6.4
8.4
64
6,4
6.4
6.4
64
6.4
6.4
6.4
6.4
6.4
6.4
6.4
6.4
8.4
6.4
8.4
6.4
6.4
8.4
6.4
6.4
6-4
6.4
8.4
8.4
6.4
64
64
64
6.4
8.4
6.4
8,4
8,4
64
6.4
6.4
6.4
6.4
6.4
64
64
6.4
64
359.1
364.2
384.2
384.2
384.2
312.1
3885
364,1
364.1
384.1
3641
364.1
3641
364.1
364.1
364.1
418-1
3639
363-9
418.1
3839
363.9
363.9
363.9
3639
3639
363.9
363.9
363.9
388.2
363.9
4159
363.8
363.8
3638
363.8
383.8
3638
3638
383.8
363.8
3838
363.8
4158
415,8
383.7
383.7
3837
363.7
363.7
3637
363,7
386.1
415.8
415.8
415.8
415,8
415.8
363.8
4158
415.6
363.7
311.7
3636
3638
3638
3638
4159
415.9
Water meter
Draft Cod water readna
CnOff density, IWgtl
On 8.14
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
OH
OH
Oft
OH
Off
Off
OH
Off
Oft
Off
Off
Off
OH
Off
Off
Off
Off
Off
OH
Off
Off
Off
Off
Off
8.14
814
6.14
8.14
8.14
8.14
814
814
8.14
8.14
8.14
814
6.14
8,14
8.14
8.14
8.14
8.14
8.14
8.14
8,14
814
8,14
814
814
814
8.14
814
814
8.14
814
6.14
813
8.13
813
B.13
8.13
8.13
8.13
8.13
8.13
8.13
8.13
8.13
813
613
8.13
613
613
8.13
813
813
8.13
613
813
813
813
813
813
8.13
813
8.13
8.13
8.13
8.13
8.13
813
814
814
gpm
6.2
62
63
8.3
63
63
6.3
63
63
8.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
63
8.3
8.3
6.3
8.3
83
6.3
63
8.3
6.3
63
63
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
63
6.3
6.3
6.3
6.3
63
8.3
63
63
6.3
63
8.3
6.3
63
63
8.3
63
8.3
63
63
6.3
83
63
6.3
63
63
-------
FURNACE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE
02-Apr-96
29- An- 95
RuiTTD-IB
time stBd*e»t dUion water in i
sec
31260
31320
31380
31440
31500
31560
31820
31676
31736
31796
31856
31916
31976
32036
32096
32156
32216
32276
32336
32396
32458
32516
32576
3283S
32696
32756
32818
32876
32936
32996
_. 33052
C7 33112
[^ 33172
lyi 33232
33292
33352
33412
33472
33532
33592
33652
33712
33772
33832
33882
33952
34012
34072
34132
34192
34252
34312
34372
34428
34488
34548
34608
34668
34728
34788
34848
34908
34968
35028
35088
35148
35208
35288
35328
35388
99
99
98
98
97
97
98
96
96
96
96
96
96
96
96
96
96
95
95
95
94
94
93
93
92
92
92
92
92
92
92
92
92
92
92
91
91
91
90
90
89
89
90
90
80
90
90
90
80
90
90
90
90
90
90
90
90
89
89
89
89
89
89
89
89
89
88
88
89
89
F
75
74
74
73
74
75
75
76
77
77
77
78
76
78
78
79
79
78
76
75
75
74
73
74
74
75
78
77
77
78
78
78
77
76
75
74
74
73
73
74
74
75
76
77
77
77
78
78
78
78
78
78
77
74
73
71
72
72
74
75
76
78
77
77
78
78
78
78
78
78
F
187
187
187
188
187
167
167
186
187
166
166
166
168
166
166
166
166
185
185
185
185
185
185
185
164
184
184
184
184
164
164
164
164
164
164
163
183
183
183
183
163
163
183
183
163
163
162
183
162
182
182
182
162
182
161
161
161
161
181
181
181
181
181
181
180
160
180
180
160
180
water ott
F
174
174
174
174
174
174
173
173
173
173
173
173
173
173
173
173
172
172
172
172
172
172
172
172
172
172
171
171
171
171
171
171
171
170
171
170
170
170
170
170
170
170
170
189
169
169
169
189
169
169
169
169
168
168
168
168
188
168
168
167
187
187
187
187
187
187
167
166
166
166
fire-box
F
410
408
408
404
402
400
398
395
394
391
390
387
385
384
381
380
378
376
374
373
372
372
371
370
389
368
367
385
363
362
360
359
358
356
355
356
358
354
352
351
351
351
350
349
348
345
343
341
339
337
336
335
333
332
331
331
332
330
330
331
330
329
329
328
327
327
326
324
324
323
amttert
F
71
71
71
71
71
71
71
72
72
71
72
72
72
72
73
73
73
73
73
73
72
72
71
71
71
71
71
72
72
72
72
72
73
72
72
72
72
71
71
71
71
71
71
71
71
72
72
72
72
72
73
73
73
72
72
72
71
71
71
71
71
71
72
72
72
72
72
73
73
73
stick
F
114
114
113
113
112
111
111
111
110
110
110
110
110
109
109
109
109
109
108
109
109
108
107
107
107
106
107
108
106
106
107
106
106
106
106
105
105
105
104
104
103
104
104
104
104
104
104
104
104
104
105
105
105
105
105
104
103
103
103
103
103
103
103
103
103
103
103
103
103
103
COH0I
ppm
12*50
12813
12891
12614
12594
12855
12691
12740
12699
12614
12581
12524
12476
12431
12321
12280
12158
12012
11792
11621
11993
11560
11556
11601
11641
11727
11853
11947
11943
11979
11979
11938
11951
11808
11711
11694
11686
11707
11759
11808
11926
12040
12244
12297
12231
12195
12126
12068
12012
11926
11804
11778
11617
11373
11271
11174
11100
11125
11287
11511
11878
11747
11812
11829
11784
11739
11788
11784
11735
11739
codlu
Ppm
144.4
139.2
141.3
138
132
128.4
127.8
126
124.2
122.4
121.7
120.4
117,7
116
117
113.3
113.9
1204
115.2
116
117.2
1134
114.6
114.4
108.1
105.5
105.6
104.2
105.3
104.7
106
104.2
1069
1097
111.2
109
1094
1089
111.3
1053
104.5
103
100.9
102.5
101.4
99.4
100.3
994
97.3
97.7
97.8
97.5
110.5
101.4
1042
1042
1032
99.1
939
96
96.4
95.2
95.9
95.4
93.6
94.1
92.9
91.5
92,1
915
CO low
ppm
5013
5011.4
5010.2
5010.2
5010.6
5011
5008.5
5009
5013
5010.8
5007.7
5011
50138
50118
50118
5009.4
50102
5011
5011.8
50094
5011
5013
5010.2
5010.8
5011.4
5010.2
5011
5011.4
50118
5011.4
5010,6
5012.2
5011
5010,2
50118
50106
5011
50114
5011.8
5011.8
5011.8
5012.2
5008.5
5012.6
5011.4
5011.4
50098
5011.8
5012.2
5011.8
50094
5008.5
5011,8
5012.2
5010.6
5010.6
5011
5009.4
5009.4
5011.8
5011
5011.8
5012.6
5010.2
5011
5011.4
5012.2
5010.2
5011.4
50106
O2
8.99
8,98
901
903
9,03
8,96
889
8.79
8.81
8.83
8.79
8,8
8.78
8,77
8.82
88
8.83
89
9,1
923
926
932
936
9.35
9.33
927
9-14
9.05
9.03
6,89
9.02
9.12
9.14
929
9.42
9.49
9,55
9.6
961
9,84
9.5t
9.52
9.37
8.29
9.34
9.37
9.37
9.42
9.46
9,51
9.6
9.62
9.73
9.97
10.07
10.21
10.29
10.36
10.28
10.13
10
9.95
8,89
8.87
989
992
988
9.86
9.86
9.85
CO2 JUM-THC
% ppm
9.72
9.72
9.7
9.67
9.87
9.73
9.8
9.88
9,87
986
9,87
9.87
9.88
9.89
9.84
9.88
9.81
9.75
9.6
9.49
9.46
9.42
9.4
8.43
9.44
9.49
9.62
9.7
9.71
9.73
9.7
9.63
9.61
9.47
94
9,33
9.3
9.25
9,26
924
9.29
9.38
9.49
9.54
9.5
948
945
9,41
9.36
9.3
9,22
9,21
9,11
892
8.85
8.74
8.88
8.85
8.73
8.88
898
9.03
91
9.1
9,0*
9,07
9.1
9,12
9.12
9,13
Wat»r
yU*rffrn*«*M-
balance actual flow rate heat atA
Ibs
9,0
8,0
9.0
9.0
9.0
9.0
9.0
90
9,0
9.0
90
90
90
9.0
9.0
7.5
7.5
7.5
7.5
8.0
8.0
8.0
8-0
8.0
8.0
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
8.0
8.0
7.9
7.5
7.5
75
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7,5
7,5
7,5
7.5
7.5
7,5
75
7.5
7.5
7.5
75
7.5
75
gpm St
6,4
8.4
8.4
8.4
8,4
8,4
6.4
64
8.4
6.4
64
6.4
6.4
6.4
8.4
6.4
6,4
6.4
6.4
64
*4
6.4
6.4
84
84
64
6.4
6.4
6,4
84
6.4
6.4
8.4
64
8.4
6.4
64
6.4
8,4
8.4
84
8.4
6.4
64
84
8.4
8.4
6.4
6.4
6.4
8.4
6.4
6.3
6.3
63
6,3
6.3
8.3
63
6.3
63
8.3
6.3
6.3
6.3
8.3
8.3
8.3
6.3
8.3
utttewt
383,9
363,9
363.9
4181
383.9
363.9
291.2
3641
312.0
364.1
364.1
384.1
3641
3641
3641
3641
3121
364.2
384.2
364.2
364.2
364.2
364,2
364.2
416.4
416.4
364.3
384.3
364.3
340.0
3643
3643
364.3
312.3
3643
3645
3645
384.5
384.5
364.5
384.5
364.5
3845
312.4
312.4
312.4
364.6
312.4
384.6
364.6
364.6
3648
2876
308.1
3596
359.8
359,6
359.8
3596
308.2
308.2
308.2
308.2
308.2
359.7
359.7
3597
308.3
308.3
308.3
Draft
OrVOH
Off
Off
Off
Off
Off
OH
Off
Off
Off
OH
OH
OH
OH
OH
OH
OH
OH
OH
Off
Off
Off
Off
Off
Off
Off
Off
OH
OH
OH
OH
OH
OH
OH
OH
Off
OH
Off
OH
OH
OR
OR
Off
Off
OH
OH
OH
Off
OH
OH
Off
OH
OH
OH
OH
OH
OH
OH
OH
OH
OH
OH
Off
Off
Off
Off
OH
OH
Off
Off
Off
Cool water readnct
density, IWgal
8.14
8.14
8.14
814
814
814
814
814
814
8,14
814
8.14
8.14
8,14
814
8.14
8.14
8.14
8.14
8.14
6.14
614
8.14
*.14
8.14
814
8.14
8.14
8.14
8.14
814
8.14
8.14
814
8.14
8.15
8.15
8.15
8.15
8.15
8.15
8,15
8,15
815
8,15
8.15
815
8.15
8.15
8.15
8.15
8.15
8.15
8.15
8.15
8.15
8.15
8.15
8.15
8.15
815
815
8.15
8.15
8.18
8.16
816
8,16
8,16
8.16
8.3
8.3
6.3
63
83
63
6.3
6.3
6.3
8.3
63
63
6.3
6.3
63
8.3
8.3
6.3
6.3
83
83
8.3
83
63
8.3
8.3
8.3
8,3
8,3
6,3
63
6.3
6.3
63
63
6.3
63
8.3
6.3
6,3
6,3
6.3
8.3
6.3
8.3
8.3
6,3
6.3
6.3
6.3
6,3
6,3
6,2
6,2
6.2
6.2
6.2
6.2
6.2
6.2
62
62
8.2
62
8.2
8.2
8.2
6,2
6,2
6.2
-------
FURNACE A WITHOUT CATALYST-LOW HEAT REMOVAL RATE
02-A|r-96
29-Jm-95
RuiTTD-18 uy**»r
ttme stack oft dMon water hi wi
e»f G i- *"
ScC
35448
35508
35568
35628
35688
35748
35804
35864
35924
35984
36044
36104
36164
36224
36284
36344
36404
38484
36524
36584
36644
36704
36764
36824
36884
36944
37004
37064
37124
37180
37240
O 37300
S 37360
-------
FURNACE A WITHOUT CATAIYST-IOW HEAT REMOVAL RATE
Prtttedon
02-Apr-96
29-JUV9S RunTTCMB
Cmr stack e»l dfUSen water in w
eut p C tr
sec r
39636
39896
39756
39818
39676
3993J
39992
40052
40112
40172
40232
40292
40352
40412
40472
40532
40592
40852
40712
40772
40832
40892
40952
41012
41072
41132
41192
41252
41308
41368
41428
rt 41488
2 <1548
~J 41808
41888
41728
41788
41848
41908
41968
42028
42088
42148
42208
AVERAGE
11.167778 leShrs
670.06667
155
156
155
158
158
158
156
156
156
158
157
1ST
156
156
157
158
158
158
158
156
156
157
158
156
157
157
157
158
158
159
159
159
160
160
160
160
161
161
160
159
158
157
157
139
84
34
64
84
84
64
84
85
84
85
85
85
85
85
85
85
85
85
85
85
85
85
85
85
as
85
86
86
86
86
86
86
66
86
86
86
86
85
84
83
82
81
81
79
161
161
181
181
162
162
182
162
162
162
162
162
162
162
162
162
162
182
162
162
163
183
163
183
163
163
163
163
183
163
163
163
163
164
163
184
164
164
164
164
164
164
164
162
•ter oil fi
168
168
168
168
168
168
168
168
168
188
168
169
169
169
169
189
189
169
169
169
169
169
17Q
170
169
170
169
170
170
170
170
170
170
170
170
170
170
171
171
171
171
171
171
189
re-box n
F
555
555
554
553
551
549
649
548
547
547
548
544
543
542
543
543
544
543
542
542
541
540
540
541
541
540
540
540
539
539
538
538
538
538
529
523
521
519
520
516
511
511
510
532
ntitrt
74
74
75
74
74
74
74
75
74
75
75
75
75
74
75
75
74
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
75
74
73
72
Mack
f
160
180
180
180
181
181
181
181
181
181
181
182
182
181
181
181
181
180
181
181
181
181
181
180
181
181
162
163
163
183
183
184
184
183
183
184
184
184
183
183
163
181
181
159
COHcji
ppm
14087
13938
13814
13818
13542
13623
13676
13908
14250
14193
14103
14152
14099
14144
14099
14026
14010
13892
13794
13725
13623
13595
13815
13627
13391
13086
12956
12797
12765
12883
12581
12520
17519.19
COdb
ppm
976.1
963.7
9564
948.1
932.5
9351
942.1
942.1
972.5
979.2
9684
873.1
974.1
968.9
973.5
968.4
960.1
980.8
951.2
946,5
9417
935.9
938.5
939.S
938.3
911.3
898.4
891.1
8817
884.3
8717
868.9
CO low
ppm
5010.2
50098
5013
50114
5009
5009.8
5009
5010.6
5012.2
5009.8
5009.8
5011
5011 4
5011 8
5012.2
5010.2
5010.2
5011.4
5010.6
5012.6
5009.4
5009
5011
50094
5011.8
5012.2
5009
5011
5011
5013
5011
5013.4
O2
11.57
11.59
11.5B
11.81
1167
11.67
11 66
11.84
11.6
11.49
11.55
11.6
1163
11.76
11.8
11.8
11.78
11.81
11.82
11.82
1183
11.82
11.73
11.69
11,68
11.82
11.57
11.59
11.57
11.59
11.8
11.49
10.00
Water
CO2 JUM-THC brim* tctual (low rale
% ppm
847
846
849
6.45
841
8.41
8.41
845
a.46
8.4
835
832
8.21
8.19
8.19
8.22
8.18
6.18
8.18
8.17
6.19
8.26
8.3
6.32
8.39
845
844
848
8.49
847
8.51
9.75
!bs
3.0
30
3.0
3.0
3.0
30
30
25
25
25
2.5
2.5
2.S
2.2
20
20
20
2.0
2.0
2.0
2.0
1.5
1.5
15
1.5
15
1.5
15
1.5
10
1.0
1.0
1.0
10
1.0
1.0
05
0.5
0.5
0.5
0.5
0.0
00
heat oil
gpm Btuftnterval
6 3 359.6
63 3596
8.3
S3
63
6.3
63
63
6.3
8.3
8.3
6.3
6.3
6.3
63
6.3
8.3
6.3
6.3
63
6.3
6.3
6.3
8.3
6.3
6,3
6.3
8.3
63
8.3
63
6.3
63
6.3
6.3
8.3
6.3
8.3
6.3
6.3
8.3
6.3
6.3
359.6
359.8
287.6
308.1
3081
308.1
308.1
308.1
308.1
359.4
359.4
359.4
359.4
3594
3594
359.4
359.4
359.4
308.0
3080
359.3
3593
3080
359.3
308.0
3354
359.3
359.3
359.3
359.3
359.3
307.9
359.3
307.9
307.9
3592
359.2
359.2
359.2
3592
359.2
350.76
Water meter
Draft Cool water reaefng
OVOtt density, IWgal
On 8.15
On »15
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
6.15
8.15
8.15
815
8.15
815
8.15
8.15
815
8.15
815
6.15
8 15
8-15
8-15
8.15
815
815
8.15
6.15
615
815
8.15
8.15
815
815
815
8.15
8-15
815
815
814
815
814
8.14
8.14
814
8.14
614
814
8.14
8.15
gpm
62
62
6.2
8.2
6.2
6.2
6.2
6.2
62
S.2
6.2
6.2
62
6.2
6,2
6.2
6.2
8.2
6,2
62
6.2
6.2
62
6.2
6.2
6.2
62
62
62
6.2
6.2
6.2
62
62
6.2
6.2
6.2
6.2
6.2
6.2
62
6.2
62
TotdBtuoU* 236.087 . BtuhrcU =
Total Btuln = 556,252 , Btuhr In =
Efficiency . 42 44%
Water flowrate * 6.33 gpm
Bunrate * 2.81 <
Wood molstire = 20 40%
21.138
49,809
-------
FURNACE A WITH CATALYST-HIGH HEAT REMOVAL RATE
27-Od-95 Run TTCD-2
time stacK dlrfion nmfcierl water~oul water in sf ova exit ftre-faox C
3500
3580
3620
3980
3740
3800
3690
3920
3980
4040
4100
4158
4216
4276
4338
4396
4456
4518
4578
4636
4898
4758
48t8
4878
4936
4996
5059
5119
5176
5238
5288
5359
. , 5418
O 5479
4^ 5532
OQ 5582
S»52
5712
5772
5832
5892
5952
6012
8072
6132
6192
6252
6312
6372
6432
9492
6552
6812
6972
8732
6792
8852
8908
6888
7028
7088
7148
7208
7288
7328
7388
7448
7508
7568
7828
7688
7748
7808
7888
123
107
101
98
97
88
98
98
99
88
99
88
99
98
89
98
88
88
100
88
89
100
102
101
101
101
102
88
100
101
100
101
101
100
100
103
102
101
101
101
102
103
102
104
103
102
101
103
103
102
102
103
102
102
102
102
101
103
104
106
107
107
107
109
118
138
144
154
165
174
184
188
212
228
75
71
71
72
74
75
75
78
78
75
74
74
73
73
73
73
72
73
73
74
74
75
76
78
75
74
73
73
72
72
72
72
71
71
71
71
71
71
71
71
71
71
71
71
71
70
70
70
70
70
70
70
70
70
71
71
72
73
74
75
75
74
73
73
78
87
aa
93
88
98
100
102
105
109
67
67
67
67
67
67
88
68
68
68
68
68
68
97
87
87
87
87
66
96
67
97
87
67
68
68
68
88
68
68
87
67
9?
67
97
97
98
96
97
96
68
66
86
66
66
66
66
66
98
66
66
66
99
86
89
68
87
87
67
87
69
88
68
68
89
68
68
61
68
88
68
88
89
89
r
86
83
88
88
88
188
188
188
188
188
188
188
188
188
187
187
187
187
187
187
186
184
182
180
179
178
177
176
175
175
174
174
174
173
173
173
173
172
172
172
172
171
171
171
170
170
170
170
170
169
189
168
168
198
166
188
167
187
167
167
196
166
186
165
185
164
194
194
185
185
166
167
167
186
r
170
174
166
187
167
183
171
171
172
170
170
170
170
170
17U
170
172
173
172
172
173
172
171
168
188
198
195
194
163
193
163
182
162
1*2
161
161
181
161
191
191
191
160
tea
160
159
159
158
158
158
158
1S8
158
158
157
157
157
157
157
157
158
157
159
155
155
155
154
154
154
154
155
159
156
157
157
r
173
148
137
132
132
132
131
129
128
129
129
129
130
129
126
129
128
128
136
127
126
137
127
127
127
128
128
128
128
128
128
128
128
129
129
130
130
130
129
129
129
129
128
129
128
129
128
128
130
128
129
128
129
128
128
128
128
128
128
130
130
130
130
130
153
198
202
213
230
236
254
269
279
292
t-
237
251
255
255
254
252
251
250
249
250
250
250
250
250
251
249
247
247
246
246
245
246
245
244
244
243
242
242
242
243
243
245
247
253
255
258
280
263
265
267
298
270
270
271
272
272
272
273
275
277
278
278
275
288
268
293
261
260
258
258
257
257
257
258
322
807
1150
1154
1154
1154
1154
1154
1154
1154
Oristi
%
0.5
0.3
0.9
09
0.9
09
09
08
0.8
0.7
07
0.7
0.7
0,7
08
0,8
0.8
08
0.8
0.9
0.8
08
0.8
0.8
08
08
0.8
0.8
08
0.8
0.8
0.8
0.9
0.9
09
0.9
0.9
0.6
08
0.8
0.8
08
0.8
0.8
06
0.8
0,8
08
08
0,8
0.7
07
0.7
0.7
07
0.7
07
07
0.8
08
0.8
09
0.9
OB
09
0.8
18
3.0
30
3.0
3.0
3.0
3.0
3.0
COdtu
ppm
343.7
89.8
174
212.4
207.8
185.1
182.8
182.1
174.3
1688
1684
171.5
178.1
1831
182.5
1942
200
201 .8
203.1
2041
185
195
1942
194.7
1871
188.6
1882
2028
2056
213.2
219.8
223.6
23S
2344
235.2
2342
226.7
2223
2215
217
213.S
2098
208.2
2065
2078
2044
2084
203
203.3
184.5
189.6
1838
1834
179
1781
1802
1812
1851
195.3
203.8
219.1
2235
23S
245
7898
12927
20076
2008
20081
2007.6
2008
2007.5
2007.8
2008
CO tow
4544.7
3339
47734
50183
5018.3
5018.1
5018.3
5017.8
5017.9
5016.7
5015.5
5017.5
8019. 1
9019.1
50167
5010.8
5018.5
5019.5
5020-3
5019-1
5019.1
50199
5018.7
5018.7
50199
5018.1
5019.9
50183
50179
5018,1
5016.3
5019.1
5018.5
5020.3
5020.8
5019.5
5018.3
3546.1
4847.4
50187
5018.3
5018.1
50203
50191
5018.1
50191
50203
5018.1
50187
5020.3
5020.3
5017.9
50187
50203
5017,5
50195
50187
5018.3
50183
5017.8
5018.7
50195
50179
5017.8
50175
50183
5016.3
50183
50179
5018.7
5015.9
50179
5020.3
5017.9
02
16.18
18.88
18.07
18.13
15.09
14.7
14.58
14.77
15
15.29
15.38
is.se
1544
15.38
16.31
1533
1525
15.29
15.19
15.23
15.28
15.25
15.2
15.32
15.43
15.S4
15.55
1572
15.93
1557
15.58
15.41
15.34
1538
15.43
1528
1882
1616
15.47
1554
15.54
15.55
15,55
1547
1553
1564
1564
1552
1561
15.74
15.7
15.73
15.84
1578
15.76
15.77
15.75
15.54
15.36
15.23
15.15
1512
15.08
15.03
14.53
9.3
5.88
494
4.24
4.04
3.74
327
2.52
Water
CO2 JUM-THC balance catarjsi «3ual flow rate
4.14
1.88
2.88
479
556
5.81
9.8
5.55
5.28
S11
4.99
4.87
473
486
492
499
5
5.07
5.08
6.17
5.12
5.08
512
5.15
506
4.85
4.86
486
475
48S
4.81
483
5.1
5.18
8.13
9.12
i.2S
3.43
477
5.07
5
501
6.01
5
5.08
5.03
4.94
4.8S
5.08
502
495
5.01
497
485
4.88
482
482
498
5.19
S.37
i.49
S.58
5.58
5.93
5.89
941
11.57
14.24
1534
18.06
16.25
16.53
19.87
17.57
ppm
546
804
1337
1476
1403
1234
1061
840
847
75«
887
656
893
710
756
787
813
822
823
S18
785
778
766
741
708
980
874
667
668
676
681
688
703
983
878
870
840
60S
558
562
540
518
476
462
453
437
428
413
416
411
400
380
387
389
376
357
368
378
402
418
457
488
528
521
537
588
988
600
3502
5420
5783
5381
5682
5987
84
835
83
83
S3
835
825
125
84
82.5
82.5
125
825
82.5
83.2
83
83.5
83.5
83.5
83
83
83
82.5
82
815
815
61.5
81.5
82
82
82
82
82
844
82
82
82
82
82
82
818
82
82
82
82
82
81.8
82
82
92
81.5
81.5
815
81.5
81.5
61.5
81
81
805
80
785
78.5
78.5
78.5
788
76.5
78
78.5
75.5
74.3
73
71.5
70
98.5
f
322
328
328
324
320
315
311
308
302
288
294
291
288
288
283
281
279
277
274
273
272
270
268
268
287
268
285
285
284
264
264
363
293
263
263
293
263
263
283
263
263
263
264
294
264
294
264
264
285
286
266
265
265
264
364
264
264
264
264
284
263
263
263
263
265
307
371
432
482
547
587
641
880
708
FT
heatoul
gpm Bttifintervat
6.8 888.4
6.8
68
68
6.8
7.2
7,2
7.2
7.2
7.2
72
72
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
72
7.2
7.2
7.2
7.2
72
7.2
7.2
72
7.2
7.2
72
7.2
7.2
72
72
72
72
7.2
7.2
7.2
72
7.2
7.2
72
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
72
72
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
?,2
72
7.2
7,2
7.2
7.2
7.2
498.8
1224.7
11686
11686
14685
9944
8944
83S.S
10S3.2
8830
1053.2
10532
10532
984.7
8847
•771
818.3
877.1
877.1
7598
701.7
6434
843.8
8441
703.2
703.4
703.7
703.8
703.8
845.2
704.1
7041
9024
704,4
704.4
704.4
64S.7
845.7
64S.7
645.7
645.9
645,9
6459
949.1
649.1
6491
9491
705.1
946.3
6463
6483
587.6
846.5
6495
6485
548.6
S87.S
5878
648.8
5290
588.0
6470
5882
5982
5884
588.4
568.4
647.2
5882
847,0
6468
587.8
6465
ntaaon
Draft
OnTOff
off
off
off
off
off
off
off
off
off
off
off
off
off
of
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
of
off
of
off
off
off
off
off
off
of
off
off
of
off
of
off
off
off
off
of
of
on
on
on
on
on
on
on
on
on
on
m-pfjF-ss
Density of Water meter
oooi water read ng
Ugll
6.13
811
814
814
8.14
8.15
8.12
8.12
6.12
8.13
8.13
8.13
8.13
8.13
813
8.13
812
8.12
8.12
8.12
8.12
8.12
8.12
6.13
a 13
8.14
8.14
8.14
8.15
8.15
8.15
8.15
8.1S
8.15
8.15
9.15
8.15
8.1S
8,15
8 15
8.15
8.16
8.16
8.18
8 16
8.18
816
816
8.18
818
8.16
818
8.16
8 16
816
816
8.16
6.16
816
8.17
8.18
8.17
8.17
817
6.17
8.17
8.17
8.17
8.17
8.17
8.17
8-17
8.16
8.18
68
68
6.8
88
68
7.2
7.2
7.2
7.2
7.2
72
7.2
7.2
72
7.2
7.2
7.2
72
7 2
7.2
7.2
72
72
7.2
72
72
7.2
72
72
7.2
72
72
72
72
72
7.2
72
72
72
7.2
7.2
72
7.2
7.2
72
72
7.2
7.2
72
7.2
7.2
7.2
7.2
72
7.2
72
72
72
72
72
72
7.2
72
7.2
7.2
7.2
72
7.2
7.2
7.2
7.2
7.2
72
72
-------
FURrWCE A W11W CATALYST-HIGH HEAT REMOVAL RATE
Printed en 02-Apr-86
27-0*85 Run TTCD-2
tlrne stach cjlulton ambient water-out water in slove exit Hre-box CO hioji
sec
7928
7988
8048
8108
8168
8228
8284
8344
8404
8484
8524
8584
8844
8704
8764
8624
8M4
8944
8004
8084
9124
9184
9244
9304
8384
9424
8484
8544
9804
9660
9720
9780
9840
Q8900
fv 09BO
1^0020
10080
10140
10200
10280
10320
10380
10440
10500
10560
10620
10680
10740
10800
10860
10820
10980
11038
11096
11156
11216
11278
11338
11388
11456
11516
11578
11636
11698
11758
11818
11878
11938
11996
12058
12118
12176
12138
12298
242
254
266
274
261
288
293
287
296
284
231
201
185
173
164
158
153
152
149
146
144
143
143
141
140
139
136
138
139
137
137
138
137
137
135
137
135
134
134
134
134
134
135
133
134
134
134
133
132
132
135
133
133
134
133
133
133
133
132
133
132
131
132
132
131
130
131
131
128
131
131
132
131
132
1
113
116
121
123
125
126
127
127
126
116
98
90
87
85
82
81
60
78
78
78
78
78
77
77
77
76
76
78
78
76
76
76
75
75
76
75
76
76
75
75
75
75
76
75
78
78
75
75
75
75
75
75
75
75
75
75
75
75
75
74
75
75
75
75
75
75
75
75
75
75
75
75
75
75
r
69
69
69
69
88
69
89
69
89
69
70
70
70
71
71
71
71
71
71
71
70
70
70
70
69
69
6G
69
88
89
69
68
68
69
68
89
68
68
88
69
69
89
88
88
69
88
69
69
69
69
68
69
88
88
69
68
68
89
69
68
69
89
68
68
69
69
69
69
68
88
69
69
68
m
r
168
170
171
172
173
174
175
176
178
177
178
178
178
178
178
178
178
178
178
178
178
178
178
178
177
177
177
176
178
175
175
174
174
174
174
173
173
173
173
173
173
173
173
172
172
172
172
172
171
171
171
171
171
171
170
170
170
170
170
170
170
169
168
168
168
189
168
168
188
188
168
188
188
168
r
158
158
160
181
161
182
183
164
164
165
168
167
167
186
166
166
166
168
188
166
166
168
166
186
166
165
165
165
164
184
163
183
163
163
162
162
182
182
162
162
162
162
181
161
161
161
181
181
161
160
160
160
160
160
159
160
159
159
159
159
159
159
159
158
158
158
158
158
157
158
157
157
157
157
i-
305
319
333
345
352
359
363
365
363
345
280
242
220
208
196
189
185
181
179
176
174
172
171
170
169
167
167
166
185
184
164
164
184
183
162
182
162
162
181
161
161
181
161
ISO
180
160
160
160
160
160
160
158
159
159
159
159
158
158
158
158
157
156
158
156
156
158
158
158
156
158
156
156
1S8
156
r
1154
1154
1154
1154
1154
1154
1154
1184
1154
1154
1154
1006
842
784
748
713
682
657
830
811
585
585
578
570
568
558
550
544
$36
538
•18
SIS
514
S12
$10
507
503
502
500
489
489
499
501
502
504
502
502
503
510
511
509
811
511
812
515
$12
512
513
517
•21
52$
$28
526
527
529
533
538
535
538
537
540
542
•43
540
%
3.0
30
3'.0
3.0
3.0
3.0
3.0
3.0
3.0
3.0
3.0
3.0
3.0
2.4
1,8
1,8
1.6
1.6
1,6
1.6
16
18
1.8
1.7
1,8
1.8
1.8
18
18
19
19
2.0
2.0
2.1
2.2
2.2
2.2
2.2
2.2
2.2
2.3
2.4
2.4
2.8
2.5
2.5
2.8
2.6
26
2.6
2.8
2.7
28
2.6
2.7
2.7
2.7
2,7
2,7
2.7
2.7
2.7
2.8
J.7
2.7
2.8
2.8
2.8
2.8
2.8
2.8
2.8
28
2.7
COtttl
ppm
2008
20085
2007.8
2006
2008
2007,8
2008
20072
2007.8
2007.6
2008
1862.5
1184.7
8607
7443
6855
682
873.8
884.4
663.1
658.5
680.6
875.5
8948
706.4
710.4
7205
7233
732.8
7331
754.1
777.7
798.2
8234
8299
828.8
8241
8273
8405
854.5
8848
897.3
9158
9269
844
9548
962.6
975.1
8862
9764
874.1
988.9
9645
870.5
977.5
9838
882.1
974
964
966.1
980.3
976.2
9787
9871
9945
1016.1
1018.8
1018.7
1028
10244
988
983.2
975.1
8577
CO low
ppm
50163
5018.3
5017.1
S016.7
SO17.9
50163
5016.7
5016.3
50175
5017.8
50187
5015.9
5019.1
5020.3
5018.7
5015.1
5019.5
S017.1
S015.5
5019.5
50178
60187
5017.5
5018.3
5016.7
50208
50179
5018.3
5018.3
5015.5
6017.5
S017.1
5017.9
5018.7
5017.1
5018.7
S017.1
801 7.1
5018.3
5019.5
S0179
50175
5017.9
5018.7
5015.1
5018.7
5016.7
50187
50171
5017.5
5017.1
5017.8
S0175
S0179
5017.5
5016.3
5018.7
5018.1
5017.1
5017.8
5018.7
5018.7
$018.7
$019.5
S017.1
5019.5
50183
5018.7
5017.5
50183
5018.7
5019.1
S018.3
5018.3
O2
%
2.06
1.68
1.4
1.18
107
1.08
1.08
1.14
1.26
1.39
2.78
8.64
8.57
8.84
10.07
10.44
10.56
10.71
10.72
1088
1109
1102
11
11
10.88
11.01
11.01
11.07
1101
10.81
11.05
11.02
11.1
10,85
1088
10,94
10.13
10.86
10.88
10.85
10.77
10.74
10.71
10.58
10.68
1058
10.41
10.48
1057
10.8
10.59
10-32
10.48
10.47
1034
10.38
10.29
10.41
10.32
10.27
10.21
10.34
10.54
10.45
1038
10.38
10.42
10.43
10.45
104
1016
10.05
981
991
Water
CO2 JLMTHC balance catalyst actual flow rmte heitout
%
17.84
18.22
18.45
1857
18.58
1854
18.48
18.38
1823
18.07
17.31
14.84
12.4$
1084
1024
8.85
8.74
9.88
8.72
8.64
952
9.86
9.75
879
9.88
9.88
9,92
9,91
10
10.15
10.03
10.11
10.06
10.23
10.27
1026
10,35
10,33
10.33
1038
10.46
10.51
1056
1067
10.68
1089
10.8
1083
1089
10.7
1075
11.02
10.84
10.89
11.02
1088
11.05
10.9
11.03
11.02
11.01
10.9
10.7
10.61
10.88
109
10,84
10.83
10.82
10.88
11.11
11.23
11.43
11.3
pom
5503
5576
5155
5582
8030
6138
6129
5882
6336
8695
6695
6695
8554
5372
4568
4177
3866
3836
4087
4007
4014
4152
4304
4487
4611
4757
4815
5018
5156
5236
5518
5705
5831
6082
6248
6536
6480
8498
6595
6685
6898
8896
6695
8895
6698
6694
8686
8684
6698
6698
8688
8698
8695
6697
6695
6897
6694
6697
8696
6694
6898
6685
6695
6684
6684
8894
8696
8684
6694
6687
8882
6884
6695
6696
ta
67
65.1
63.5
62
eo.s
58
57.5
56
545
53
52
515
51
50
49.5
49.5
49.5
48
49
49
49
49
48
48.5
485
48.5
48.5
48
48
48
47.5
47.5
47.5
47.5
47
47
485
48,5
46.5
46
48
455
455
4S.5
45
45
445
44.5
44
44
44
435
43.5
43-5
435
43
425
42.5
42.5
42
42
41.5
41.5
415
41.1
41
40.5
40.5
40.5
40
40
399
38.5
39.5
F
735
762
793
823
850
872
891
909
919
919
875
823
774
735
702
678
• 655
834
818
802
587
571
558
548
«34
S23
514
505
497
481
484
480
475
471
467
464
462
460
458
458
456
454
454
453
453
4S2
452
452
452
451
451
452
452
452
452
452
452
452
451
451
451
451
451
452
450
450
450
450
449
450
450
450
450
450
7.2
7.2
7.2
7.2
7.2
7,2
72
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
72
7.2
7.2
7.2
72
7.2
7.2
7.2
7.2
72
7.2
72
7.2
7.2
7.2
7.2
7.2
72
72
7.2
7.2
7.2
7.2
72
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
72
72
7.2
7.2
72
7.2
72
7.2
7.2
7.2
7.2
7.2
72
72
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
72
7.2
72
uflnterwl
648.3
848.1
645.9
6457
704.4
657,2
7039
703.7
703.7
7034
703.2
644.3
644.3
703.2
703.2
703.2
703.2
703.2
7032
7032
703.2
703.2
7032
7032
644.8
703.4
703.4
8448
868.7
645.0
703.9
8452
845.2
845-2
704 1
8455
845-5
645-5
646.5
645.5
645.5
845.5
704.4
645.7
845.7
845.7
645.7
645.7
5870
8459
6459
602.8
845.9
645.9
848.1
587.2
6461
6461
848.1
648.1
646.1
5874
587.4
648.3
8483
848.3
587.6
$87-6
648.5
587.6
646.5
846.5
6485
646.5
draft
CWOff
on
on
Oft
on
on
on
on
on
on
on
on
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
Off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
Off
Off
off
Off
Off
off
off
off
off
off
off
off
off
off
off
off
off
off
Off
off
off
off
Density of Water meter
cool water readng
Ugal
8.18
8 16
8-18
8.15
8.15
8.15
8.15
814
8.14
8.14
8.14
8.14
814
814
814
614
8.14
8.14
8.14
814
614
8.14
814
8.14
8.14
814
8.14
8.14
614
8.14
8.15
8.15
815
8.15
8.15
8.15
815
8,15
8,15
8-15
8-15
8 15
8.15
8.15
8.15
815
8.15
815
8.15
8.18
1.16
8.16
8.16
8.16
818
8,16
8.18
816
818
8.18
8.18
8.16
8 16
8.16
8.18
8.16
818
816
6 16
8.16
8.16
8.18
816
816
ppm
72
7.2
7.2
7.2
7.2
7.2
7.2
7.2
72
7.2
7.2
7.2
72
72
72
72
7.2
7.2
7.2
7.2
72
7.2
72
7.2
72
7.2
7.2
7.2
72
7.2
7.2
7.2
72
7.2
72
7.2
7.2
7.2
72
7.2
72
7.2
72
7.2
72
72
7.2
72
72
7.2
72
72
7.2
72
72
7,2
72
7.2
7.2
7.2
72
7.2
7.2
7.2
72
7.2
72
7.2
7.2
7.2
7.2
72
72
7.2
-------
FURNACE A WITH CATALYST-HIGH H6AT REMOVAL RATE
02-Apr-S8
27-OM-95
time
sec
12356
12412
12472
12532
12592
12852
12712
12772
12832
12892
12852
13012
13072
13132
13192
13252
13312
13372
13432
13482
13552
13912
13872
13732
13788
13848
13908
13868
14028
14088
14148
14208
. 14289
^^14328
1^)14388
O*444S
14508
14568
14828
14888
14748
14808
14898
14928
14888
15048
15108
15184
15224
15284
15344
15404
15494
15524
15584
15844
15704
15784
15824
15884
15944
16004
16094
16124
16184
16244
18304
18364
19424
16484
16540
18600
18880
18720
RunTTCn-2
stack dilution ambient wattr-out water in stove exit lire-box COhioJi
F
132
132
133
131
130
131
130
129
128
129
128
129
145
156
180
223
241
251
260
299
271
277
283
276
217
178
161
153
146
141
137
133
131
129
126
124
123
121
118
119
120
119
119
117
lie
114
114
113
113
12
11
10
11
11
09
08
108
106
107
108
107
106
108
108
107
105
104
105
104
103
102
103
102
103
r
78
77
78
78
78
78
77
77
76
76
78
76
ee
92
101
108
111
111
113
114
118
117
118
111
91
84
81
78
78
78
77
77
76
78
75
75
75
78
77
78
79
79
78
78
77
77
78
78
76
76
75
75
75
75
75
75
75
75
74
74
75
74
74
74
74
75
75
75
75
74
74
74
75
76
r
89
89
70
70
70
71
71
71
71
71
70
70
70
70
70
70
88
70
70
70
98
70
70
70
89
70
70
70
70
70
70
70
70
70
70
70
70
70
70
70
71
71
72
71
72
72
72
71
71
71
71
71
71
70
71
70
70
70
70
70
70
70
70
70
70
70
70
70
70
70
70
70
70
70
i-
18?
187
167
167
187
187
167
167
188
186
188
188
168
188
187
188
169
171
172
173
174
175
178
177
178
178
178
178
178
178
178
178
17B
178
178
178
178
178
178
178
177
17?
177
176
176
175
175
175
175
174
174
174
173
173
173
173
173
173
173
172
172
172
172
172
172
172
172
171
171
171
171
171
170
170
f-
157
157
157
157
157
157
156
156
159
158
156
158
155
155
156
157
158
159
161
161
162
163
184
165
188
166
189
168
199
188
169
188
169
167
166
188
166
166
187
167
186
188
165
185
164
184
164
164
163
183
183
162
182
182
182
182
162
191
161
181
181
161
181
161
181
160
181
180
160
180
160
160
190
190
f~
155
155
155
154
154
154
154
153
153
153
153
153
188
232
288
288
313
323
333
340
347
354
382
352
276
227
202
189
180
174
169
185
131
189
158
154
153
151
148
148
147
147
146
145
144
143
142
141
141
140
140
138
138
138
138
13?
137
136
13«
135
135
135
134
134
134
133
133
132
132
132
131
131
131
131
F
541
540
543
542
541
542
542
544
545
547
548
549
709
1083
1155
1155
11SS
1155
1155
1155
1155
1185
1155
1148
1141
1051
873
•70
781
748
718
886
980
887
654
842
631
621
612
603
584
585
578
573
588
584
560
555
581
547
544
540
539
533
531
530
528
526
525
523
520
518
517
515
513
512
SOB
507
507
506
509
507
508
508
%
27
2.7
2.7
2.7
28
2,7
2?
2.6
2.5
2.4
24
2.4
2.4
2.4
30
3.0
3.0
3.0
30
30
3,0
3-0
3.0
3.0
30
3.0
so
3.0
30
2.9
2.5
2,1
1.8
1,5
1.3
1.2
1.1
1.0
0.8
0.8
09
0.8
0,8
0,8
0.8
0.8
08
0.8
0,8
0.9
09
0.8
0.8
1.0
1.0
0.8
0.8
0.9
0.8
0.8
0.9
09
0,8
0,9
0,8
08
0,8
0.8
0.8
09
08
09
0.8
09
COdb
ppm
856,2
840,8
833.8
828
882.8
888.4
821 1
•87,7
8486
Ml, 3
833
820
17282
2008.6
2007.8
2007.8
2008
2007.2
2007.8
2007.3
2008
2007.8
2008,3
20086
2005
2007.6
18883
1516.9
1207.2
957.5
714.7
848.8
548.6
467
404.3
355.5
321,1
285,9
2733
2837
255.5
258.1
257.2
252,6
246.4
246.7
244.3
246.9
245.1
245.8
245.1
249.2
252.1
249
247.2
24S.4
249.4
244.1
240.1
2371
2363
233.7
227.2
223.8
223.8
217.3
215,8
214
2098
2103
2095
213.2
2108
213.2
CO tow
ppm
5018.7
5017.1
5019.5
5018.3
5019.9
5018.3
5019.1
5018.7
5018.3
5018.1
5018.3
5016.7
5018.7
5019.5
50159
5016.7
5017.1
5018.7
5018.3
50187
6017.5
50187
50158
50175
5018,1
60183
5017.9
5017.5
50113
5018.7
50199
5017.8
5019.5
50179
5018.7
50151
5017.5
5017.8
5017.5
5019.9
50183
50158
5018.3
5018.3
5018.7
5018.3
5017.8
5018.7
5017.B
5019.1
50187
5016?
5018.7
5018.7
5019.1
5018.3
5015.9
5017.8
50187
5017.5
5018.3
50183
5018,3
5018.7
50171
5017.1
5018.7
50175
50178
50171
5018.7
50187
50178
50171
O2
%
888
8.92
10.01
10.18
10.82
10.33
10.08
10.04
10.18
10.18
10.06
10.15
9.68
598
3.25
1-49
088
087
1
1.15
1.37
1.51
1.48
1,58
2.85
5.71
7.14
781
833
908
8.35
8.82
8.88
873
897
10.24
10.12
10.2
10.54
10.63
10.48
1028
10.24
1008
1021
10.15
10.22
10.09
1001
884
10
1006
8.82
9.77
9.74
988
10.12
10.18
103
10.07
888
BBS
10.12
10.11
1002
8.88
101
1008
10,05
10.07
10.27
10.28
1024
10.44
Water
CO2 JUM-TMC balance catalyst actual flow rale neat out
%
11.36
11.29
1122
1103
10.87
1088
1105
11.09
10.9
10.81
11
1C1B3
11.49
13.87
1512
1705
1(03
18,27
18.28
182
17.8
17.73
17,73
1761
16.1
14.08
13.31
12.7
1198
11.06
10.74
10.49
10.43
10,4
10.19
9.89
10.13
10.06
9.75
9.72
9.85
10.07
10.13
10.28
1017
1026
10.22
10.36
10,48
10,59
10.54
10,51
10.7
10.85
1088
1083
10.52
10.48
10.34
10.58
10.74
10.64
10.46
10.49
10.SS
1068
10.48
10,51
10.55
10.54
1032
1035
1039
1011
pprfl
6696
6684
9693
8894
6698
9885
6885
6685
6894
8889
6983
888?
5132
9597
6888
6885
6695
6896
9482
9852
8373
5898
5453
5064
5853
6700
8888
8889
9817
5809
5053
4470
4132
3752
3435
3185
284?
2713
2541
2434
2360
2270
2185
2104
2077
2084
2120
2158
2140
2150
2124
2124
2324
2358
2300
2221
2180
2120
2058
2010
1994
1804
1871
1844
1613
1780
1780
1778
1748
1739
1734
1738
1718
1698
t*
38
38.5
38
37.5
36.5
36
3«
36
36
38
38
38
35.2
34.5
335
325
314
30.5
28.5
28.5
275
265
25.5
25
24.5
24.5
24
24
23.5
23.5
23.5
23,8
23
23
23
23
23
2S5
22.5
22
21.5
ZO.S
205
20.5
21
21
21
21
21
21
21
21
21
21
21
21.5
21.5
21
21
21
21
21
21
21
21
21
21
21
21
20.5
20.5
205
20.5
20
F
450
448
448
449
448
448
447
447
448
448
446
445
458
527
594
658
713
753
792
823
851
881
910
834
811
859
809
764
723
689
982
943
630
920
605
580
574
561
548
537
527
517
508
502
498
490
485
4(1
478
473
488
485
492
459
458
453
452
449
447
448
444
443
441
441
439
437
439
435
432
431
430
428
427
424
ppm Bt
7.2
7.2
7.2
7.2
72
7,2
7.2
72
7.2
7.2
7,2
7.2
72
7.2
72
72
7.2
7.2
7.2
7.2
72
72
7.2
7.2
7.2
7.2
7.2
7,2
7.2
7.2
7.2
7.2
72
7.2
72
7.2
72
72
7.2
72
7.2
7.2
7.2
7.2
72
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
72
7.2
7.2
7.2
72
7.2
7.2
7.2
7.2
7.2
72
7.2
7.2
7,2
7.2
7.2
72
7.2
7.2
uMnrv.1
548.9
5878
5878
5878
5878
5878
6498
949.8
5880
5880
588,0
589,0
947,0
6470
6498
6485
6493
704 8
845.7
704.4
7041
7038
703,7
656.5
7032
7032
703.2
703.2
7032
7032
703,2
703-2
703-2
6443
703.2
7032
703.2
703.2
6443
644.3
8448
8448
703.4
844.8
7037
945.0
602,0
645,0
7038
6452
845,2
704.1
845.5
845.5
6455
645.5
645-S
7044
704.4
645.7
845.7
645.7
6457
645.7
645.7
704.6
645-7
645.9
8458
8028
845.9
645.9
587.2
587.2
Density of Water meter
Draft cool water readng
On/Off
off
off
off
off
off
off
off
off
off
off
off
off
on
on
on
on
on
on
on
on
ort
on
on
on
on
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
ol!
off
off
off
off
off
off
off
of!
off
off
Hgel
8.16
8,18
8.18
8.16
8.18
8.16
8.17
8,17
8.17
817
8,1?
8.17
817
817
816
816
8,16
815
8.15
8. 15
8.15
6.14
814
814
8.14
8.14
8.14
8.14
8.14
« 14
814
814
8.14
8.14
8.14
8.14
8.14
814
814
8.14
8.14
8-14
814
8.14
8.14
814
8.15
8.15
8.15
8.15
8.15
(.15
8.15
815
8.15
8.15
8.15
8.15
8.15
8.15
8.18
8.18
8.15
816
615
8.18
8 16
816
816
816
8,18
•Pm
72
7,2
7.2
7.2
7.2
7.2
7.2
7,2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.1
7.2
7.2
72
7.2
7.2
7.2
7.2
7.2
7.2
7,2
7.2
7.2
72
7.2
7.2
7.2
72
7.2
7.2
7.2
72
7.2
72
7.2
7.2
72
7.2
7.2
7,2
7.2
72
72
72
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7,2
7,2
7.2
7,2
7-2
72
72
7.2
72
7.2
7.2
72
72
72
72
7.2
72
-------
FURNACE A WITH CATALYST-HIGH HEAT REMOVAL RATE
02-Apr-88
27-Od-H RunTTCD-2
time stack dlution amtt»m water-out water in stove axit fre-box CONpJi
sec "
18780
18840
16900
18860
17020
17080
17140
17200
17260
17320
17380
17440
17500
17580
17620
17680
17740
17800
17MO
17918
17078
18038
18086
18196
18218
18276
18338
18398
18456
18516
18S78
18838
l_,18698
WI87S6
C/H8818
•—"18876
18938
18696
180S6
19118
16178
19236
19292
19352
19412
t»472
19S32
19592
19652
19712
19772
10832
16892
18852
20012
20072
20132
20192
202S2
20312
20371
20432
204B2
20552
20812
20688
20728
20788
20848
20008
20968
21028
21388
21148
!-
103
104
104
104
103
103
102
103
102
102
101
100
99
98
89
99
98
97
»7
97
97
97
96
102
134
158
170
182
194
204
214
221
227
234
240
245
251
258
260
285
288
270
271
273
273
228
181
1St
147
140
135
132
128
124
121
119
117
115
112
110
108
106
105
104
104
104
103
102
102
101
101
100
88
97
f
77
77
77
77
78
75
75
75
75
75
75
74
74
74
74
74
74
73
73
74
73
74
73
75
84
88
91
94
98
100
101
102
104
105
108
107
108
110
111
112
112
113
113
113
113
93
84
81
80
79
78
78
77
76
78
76
76
75
75
75
75
75
78
77
78
78
78
77
77
77
76
76
75
75
r
70
71
71
71
71
71
71
71
71
71
71
71
70
70
70
70
70
70
70
70
70
70
70
69
88
69
70
70
70
70
71
71
71
71
71
71
70
70
70
70
70
70
70
70
70
70
70
70
70
70
70
m
69
•9
89
69
69
69
88
89
89 ,
89
69
89
70
70
71
71
71
71
71
71
71
71
c
170
170
170
189
170
180
169
189
189
168
188
188
188
187
187
187
167
187
187
187
187
188
168
188
188
188
185
185
188
188
187
188
168
168
170
170
171
172
173
173
174
174
175
178
177
177
17?
177
178
178
178
177
177
177
177
177
177
177
177
177
17?
177
177
176
178
17«
178
175
17*
175
174
174
174
174
h
180
180
180
158
158
159
158
158
158
158
158
157
157
157
157
157
157
15«
156
196
156
156
156
155
155
156
156
158
156
157
157
157
158
158
159
159
180
161
181
162
182
163
164
164
185
18S
185
165
165
165
185
185
185
185
185
185
165
185
185
185
18S
165
185
185
165
165
184
184
163
183
163
183
18J
163
F
132
132
131
131
131
130
130
130
129
128
128
128
127
127
127
126
125
126
128
128
126
125
124
137
196
220
239
248
263
276
287
294
301
308
315
320
326
331
335
339
342
344
345
346
345
289
230
201
184
175
169
164
159
156
153
150
147
145
142
140
139
137
138
135
134
134
133
132
132
131
130
129
128
128
F
506
505
503
503
S03
503
502
501
501
500
408
4B8
497
494
481
480
488
4M
48*
487
487
485
482
479
871
737
655
924
972
993
1003
1026
1082
1073
1054
1047
10S7
1084
1118
1122
1114
1079
1060
1044
1038
1043
993
858
863
743
702
878
860
645
833
822
612
601
582
563
575
568
581
553
546
939
533
528
523
520
518
512
509
904
%
0.9
1.0
1.0
1.0
0.9
0.9
0.9
0.9
0.9
0.9
0.9
0.9
0.9
0.8
08
0,6
0.8
0.8
0.8
0.8
08
08
0.8
0.8
0.8
1.1
1.3
1.4
1.3
1.1
1.0
1.0
1.0
1.1
1.2
1.3
13
1.3
1.3
1,3
1.2
1.2
1.2
1.2
1.0
0.9
2.1
3.0
3.0
3.0
3.0
2.8
2.6
2.4
2.1
1.8
1.5
1.3
1.1
1.0
O.f
0.9
0.9
0,8
0.8
0*
0,8
0,7
0.7
0.7
0.8
0.7
0.7
0.7
COdlu
npm
213.0
2153
2251
225.1
223.1
217.3
2155
2103
2065
203.3
202.1
203
194.S
187,3
1839
1813
178.4
178.3
175.5
173.7
1748
1751
176.6
2*5.7
1617.2
2007.8
20078
2008
1974
1550.3
1827
1787.8
1745,1
2004.2
20083
2008
2007.3
2007.8
2007.8
20085
19922
20081
20075
1846.8
1636
7082
17483
1738.4
13838
12243
1D388
917.8
812.7
708.2
803.8
492.5
384
3306
281.3
263.2
2428
227.7
208.7
1856
186.5
1631
182.3
175.1
171.4
1707
171 7
1885
168.8
1676
CO tow
ppm
5017.1
5018.3
5017.5
5017.1
9017.9
9017.1
5019.5
5018.7
5017.8
5017.8
9018.3
5017.9
$018,7
5017,5
50179
5016.3
5017.9
5018.1
5019.1
50156
501)3
50167
5018.7
50179
S017.S
5017.5
5017.5
50178
50175
5017.5
5016.3
9017.9
50179
9018.3
50175
50171
50159
5017.1
5018,7
5017.9
5018.3
5016.7
50175
5017.9
5016.7
8018.3
5017.9
5017.5
5018.3
6016.7
5015.1
5018.7
6020.3
6018.3
5017.8
5017.5
5018.3
5017.8
90178
50171
5018-3
5018.7
5017.1
50178
50171
5015.9
5018.7
5018.3
$019.1
5017.9
5017.1
5017.9
5017.8
50175
O2
%
1045
10.29
10.13
10.18
10.3
10.32
1027
1038
10.33
1024
10.07
10.15
10.34
10.52
10.63
10.30
10.4
10.45
10.S
104
10.26
10.29
10.46
10.85
10,74
11,87
11.54
10.69
9.3
8.18
a 35
620
8.17
7,»9
763
7.51
7.41
7.04
8.88
«.8
8.0
701
7.19
7.5
7.86
829
8.8
7.06
7.95
8.81
0.98
10.11
10,19
10.44
10.58
10.89
1084
10.86
10.57
10.85
10 M
10.98
11.17
11.17
11.27
11.25
11.26
11,37
1145
11.37
11.32
11.33
11.48
1182
Wain
CO2 JUM-THC balance Mini}* actual taw rate heatoul
%
1012
1027
1041
10.35
10.22
10.21
10.24
10.18
1021
10.31
1049
10.38
10.21
10.02
9.89
1016
10.12
10.07
10.01
10.12
10.28
10.2
10,02
9,84
9-89
8-58
8.9
9.73
11.1
1208
11,97
12,03
12.18
12,43
12.82
12.76
12.93
13.29
13.46
13.58
13.48
13.31
13.11
12.83
12.58
12.1
12,01
12,45
12,15
11,4
10.44
10.11
10.02
8.8
8.62
9.62
9.54
9,51
9.58
9,28
9-22
9,2
8.99
8.01
8.82
8,82
8.92
8.78
8,73
8,78
882
88
863
8.53
pom
1748
1780
1788
1738
1681
1843
1602
1574
1517
1513
1400
1402
1432
1355
1316
1290
1253
1225
1230
1241
1247
1244
1231
1252
861
658
686
705
715
731
803
870
892
926
1031
1228
1265
1296
1383
1378
1320
1308
1367
1362
1330
1488
5828
8700
6250
6509
6286
5888
5484
5009
4548
4089
3450
2827
2491
2137
1864
1875
1532
1410
1315
1244
1184
1097
1043
978
835
002
see
838
fcs
195
19
18.5
18.S
18.5
18
19
18
18
19.5
19.5
19.5
18.5
18.5
19.5
185
19.5
18.5
18.9
185
19.8
20
187
20
18,5
18
18.5
18
17
161
16
15.5
15
15
14.5
14.5
14
13.5
13.5
13
125
12
11.5
11.5
11
10.5
10.S
10.5
10.5
10.5
10,5
10,5
10.3
10.4
10
10
10
10
10
10
10
10
9.5
9
85
7.7
7.5
7.5
8
a
85
85
8.5
9
F
421
418
418
414
413
412
410
407
405
402
400
398
397
395
393
392
300
388
386
384
383
380
378
3?4
383
413
447
489
541
599
S47
875
888
711
727
748
773
793
811
626
842
652
858
862
883
824
772
731
697
668
844
824
804
588
573
558
544
531
821
512
504
485
488
481
475
469
462
456
449
444
438
431
425
418
tftjlli Bt
7.2
7.2
7.2
7,2
7.2
7.2
72
72
72
7.2
7.2
7-2
7.2
7.2
7.2
7.2
72
7.2
7.2
7.2
7.2
7.2
72
7,2
72
7.2
7.2
7.2
7.2
7.2
72
72
7.2
7.2
7.2
72
7.2
72
72
7.2
7.2
7.2
7.2
72
7.2
72
7.2
7.2
72
72
7.2
72
7.2
7.2
7.2
7.2
7.2
72
7.2
7.2
72
72
7.2
72
72
72
72
7.2
7.2
7.2
7.2
72
72
72
uMcrval
5872
587.2
587.2
5874
648.1
587.4
6463
6483
648.3
5878
S87.6
648,5
6485
5878
587.8
587.8
5878
846.8
6036
648.8
648.8
5880
588.0
847.0
6470
588.0
528.2
529.2
588.0
529.0
987.8
848.5
846.3
848.3
946.1
846.1
845.9
845.7
704.4
64S.5
704.1
802.2
645.0
703.7
703.4
703.4
7034
703.4
762.0
762.0
7620
7034
7034
703.4
7034
703.4
703.4
7034
703,4
7034
703.4
703.4
703.4
644.8
801.8
844.8
703.7
8450
7039
703.9
845.2
645.2
845.2
845.2
Draft
On/Olt
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
of!
off
off
off
off
off
off
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
Oft
on
on
on
on
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
Density of Water meter
cool water raadng
Ugal
8.18
6.16
8.18
8.16
8.16
8.18
8.16
8.18
816
818
8.16
8-16
8.18
8.16
8.16
8.18
8 16
8.17
8.17
817
817
8.17
817
817
817
8.17
817
6 17
8.17
818
818
8.16
816
818
818
8.18
8.16
8.19
8.15
8.15
8,15
815
814
8.14
8.14
8.14
8.14
8,14
8.14
8.14
814
8.14
8.14
814
8.14
8.14
6 14
614
8.14
8.14
8.14
8.14
814
8.14
8.14
814
814
814
815
815
8.15
815
8.15
8.19
0pm
72
7.2
72
7.2
7.2
72
72
72
72
7.2
72
72
72
7.2
72
72
7.2
7.2
72
72
7.2
72
72
72
72
72
72
72
72
72
7.2
7.2
7.2
72
72
72
7.2
7.2
72
72
72
7.2
72
72
7.2
7.2
72
72
7.2
72
72
7.2
72
7.2
7.2
7.2
72
72
7.2
7.2
7.2
7.2
72
72
72
72
7.2
7-2
7.2
72
7.2
7.2
7.2
72
-------
FURNACE A WITH CATALYST-HIGH HEAT REMOVAL RATS
27-Oct-BS Run TTCO-2
time sKaefc dlu&ion ambient w*1er-aut water in stove exit firft-hax CO hltf*
sec *" ~ - .. - _ _
21208
21218
21328
21388
2U48
J1508
2t5M
21828
21688
21748
21808
21888
21928
21988
23044
22104
22164
22224
22284
22344
22404
22404
22524
22584
22644
22704
22784
22824
22884
22944
23004
23084
(-C3124
^23184
^"23244
K>23304
23364
23420
23480
21540
23800
23860
23720
23780
23640
23800
23860
24020
24080
24140
24200
24260
24320
24380
24440
24900
24560
24820
24680
24740
24796
24856
24916
24976
25038
25096
25158
25218
25278
25338
25388
25456
25518
25578
r
87
87
88
88
85
85
84
83
83
83
81
81
82
82
81
82
82
82
82
82
82
82
81
80
80
89
89
88
89
89
68
88
88
88
89
89
89
89
99
130
148
155
1i1
1«4
169
172
178
17B
183
186
190
194
198
201
204
207
209
210
212
214
216
217
210
218
217
217
217
217
aie
218
218
217
217
217
r
75
75
75
74
74
74
74
74
74
74
74
73
74
75
76
76
77
78
75
75
74
74
74
74
74
74
74
73
73
73
73
73
74
75
75
76
75
75
76
83
88
88
88
89
88
80
81
82
92
94
95
97
97
87
88
97
98
98
88
88
99
88
99
88
99
99
99
99
89
B8
99
98
98
98
r
70
70
70
70
?0
70
70
68
68
69
68
68
69
69
69
70
70
70
70
70
70
70
70
70
70
70
88
69
89
69
69
69
69
68
69
69
70
70
70
70
70
70
69
69
69
69
89
69
88
66
69
89
69
70
70
70
70
70
70
69
89
69
89
69
88
88
68
88
68
87
87
87
67
67
r
173
173
173
173
172
172
172
172
172
172
172
171
171
171
171
171
170
170
170
170
170
189
168
168
166
168
168
168
188
188
188
187
187
187
167
187
168
166
166
166
166
165
165
165
165
166
166
168
186
187
186
187
167
187
168
168
168
168
168
189
169
169
169
169
170
170
170
170
171
171
171
171
171
171
r-
182
162
182
182
182
161
181
161
181
161
161
160
161
161
161
161
180
110
1S8
159
159
159
1S8
158
158
158
157
1S8
157
157
158
157
157
157
157
157
157
188
156
156
158
155
155
155
155
1S5
155
156
158
156
157
157
157
157
157
158
158
158
158
158
158
158
1S9
159
159
1S9
159
180
160
160
160
160
180
180
f
127
127
126
125
125
124
125
124
123
123
123
123
123
124
123
124
124
123
122
120
118
117
115
115
119
116
118
119
119
120
120
120
118
118
120
120
120
120
133
1«2
200
208
214
218
223
22S
232
235
240
243
247
251
254
258
281
263
265
266
287
270
271
272
271
271
271
271
271
271
270
270
270
269
269
269
f
499
494
480
466
484
483
482
481
479
479
479
478
476
474
470
466
463
461
459
458
4S6
456
45S
454
452
451
450
449
446
445
445
444
443
442
441
439
437
438
429
460
553
632
Ml
671
688
099
717
721
724
728
733
742
759
786
783
760
785
771
774
778
760
734
716
717
722
718
708
704
884
884
679
873
881
892
%
0,7
0-7
0.7
0-7
0.7
0.8
0.6
0.8
0.8
0.8
0,7
0,7
0.7
0.7
0.7
0.7
0.7
0.7
0.7
0.7
0.7
07
0.7
0.7
0.7
0.7
07
0,7
07
08
0.7
08
07
0.8
08
08
08
0.8
0.8
0.7
0.6
0.7
0.7
0.8
08
0.8
10
1.1
1.2
1.2
1.3
1.3
1.3
1,3
1.2
1.1
1.0
1.0
OB
08
0.7
0.7
0.7
0.7
0.8
0.8
08
06
06
08
0.8
06
0.6
0.8
COdkj
ppm
165.4
185,4
1646
183.7
188
16*5
1849
163,4
161,5
180
158.5
158.9
150.7
141.8
1405
136
1439
142.9
144.9
147
148.9
149.7
147.5
149.1
148.3
147.8
1456
148,5
147.S
148.4
141.6
152
141.4
138
1349
1349
143.7
144
2879
9992
1071,9
1083.7
1210.8
1314
1498.9
1630.5
1758
1887.5
2007.S
20083
2007.5
2008.3
2007.8
2008
19043
1704.9
1648 1
1478
1355.8
1241,4
11844
1088.1
1107.9
105S.5
1043,1
1018,3
1008.8
1019.S
1014,8
1024.8
1072.S
1085.3
1050
999.2
CO tow
Pf*"
5019.1
5018.8
5017.8
50175
5018.7
50183
50183
50199
50175
50187
50191
50163
50187
50179
50179
50179
50175
50163
5018.7
5016.7
50175
50183
50159
5017,9
50183
5017.9
5015.5
5016.3
50179
50183
50188
5017.5
50178
50175
50203
50179
50179
50199
50187
5017.5
50183
8018.7
5017.1
50179
5017.1
5015.9
5017.8
5016.7
5018.3
50191
5018.3
50158
50187
50179
50191
50187
50167
50179
50187
50159
50167
50181
5017.5
50183
5019.1
5017.9
5017.8
5018.3
5018,7
50163
5018-7
50179
5016.3
5017.1
O2
%
11.57
11.54
11.5
11.36
11-45
11 ,4S
1133
11 32
1128
11 16
1132
115
11,27
11,17
1104
1083
1097
11
11.03
10,92
1107
11,17
11,17
11,24
11-01
10-84
10,92
10-87
10,87
1081
1085
1085
1103
1082
1059
1018
10,14
10.4
10.7
11,56
14.94
14.73
14-45
14-19
14.1
13-95
13,75
13,46
13,34
1328
1318
13.08
1299
1288
1284
13.11
1311
1309
1313
1312
13.08
13.02
1312
13.17
13.27
13.27
13,31
13,39
1343
13,45
1349
1353
13.58
13-63
Pr
Wlt*r
CO2 JUM-THC bllancl cifilyst icM flow rat* MM out
%
(-57
8,8
882
8-77
8,88
8.88
8.8
8.77
8.85
8.94
876
8,65
8,85
192
906
8.14
9.1
8.05
902
911
8.98
8.88
8.87
8,83
• 09
8,2
8,13
9.2
9.12
1.27
9.13
828
8.07
834
8.54
8.92
99
9.85
9.31
8.35
5.81
5.83
804
8,25
833
8,46
8.85
69
7
7,03
7.1
7.19
7.28
7,38
728
7.17
7.16
7.19
7 .IS
7.22
7,34
7.37
7.28
7.23
7,14
7.18
714
7.08
704
702
8,88
8.95
8.88
8.87
PP***
823
812
839
839
844
851
841
828
821
816
811
809
786
771
767
768
753
734
719
896
681
879
665
683
887
681
885
678
891
701
713
727
728
752
788
774
785
749
728
482
348
344
347
348
388
384
39$
404
414
422
428
435
443
437
427
421
421
424
405
387
367
357
352
350
343
343
344
337
341
341
338
341
344
348
tit
3
9
9
95
95
8.5
95
95
95
95
95
95
95
9
9
8
7.8
7.5
7.7
8
82
85
65
as
9
9
9
9
9
9.5
95
95
9
9
85
6
75
75
a
a
82
8.5
8-5
85
8.5
8.5
8.5
8
8
75
7
65
5.5
55
55
55
5.5
5.5
55
5.5
5.5
5
5
5
4.5
4.5
45
45
45
4.5
4
4
4
4
F
413
407
402
398
391
388
381
376
372
388
364
361
357
354
351
348
348
' 343
341
339
337
335
333
332
330
328
327
326
324
323
322
322
320
319
318
317
316
315
313
317
333
347
361
374
367
400
415
429
443
457
471
485
489
512
521
530
536
540
544
548
549
550
550
552
554
554
555
555
557
557
556
556
585
554
Bun Bl
7.2
7,2
7,2
7-2
7,2
7,2
7,2
7,2
7,2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7,2
7.2
7.2
7.2
7,2
7,2
7,2
7.2
7.2
7.2
7.2
7,2
7.2
7.2
7.2
7.2
7.2
7.2
72
7.2
72
7,2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
72
7.2
72
7.2
7,2
72
7.2
7.2
7.2
7.2
72
7.2
7.2
72
7.2
72
7.2
7.2
7.2
7.2
72
72
7.2
7.2
7.2
7,2
7.2
7.2
uMeivit
645.5
645.5
645.5
645.5
588.8
8457
845.7
845.7
6457
845.7
845.7
6458
5870
547.8
5870
587.0
587.2
567.2
6481
846.1
848.1
587.4
587.4
8483
S87.8
648.3
6465
587.8
8465
846.5
5876
5878
5878
5878
5878
5878
4937
588.0
5680
588,0
588.0
5862
588.2
5882
588.2
847.0
8470
5880
588.0
6468
5280
5878
5878
5876
6465
587,6
5878
5878
5878
803.2
8463
6463
5874
5*74
848.1
848.1
6481
587,2
645,9
6459
845.9
8459
645.9
6459
irtedon
On*
OnFOf
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
off
0(1
off
off
off
off
off
off
off
off
off
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
on
00
on
on
on
on
on
on
on
on
on
on
02.A|*-90
Density of Water metw
cooi water readnfl
tvg»l
8.15
8.1S
8,15
8,15
8-15
8,15
8.18
8.15
8.15
8.15
8.15
818
8.15
8.15
815
8 15
816
8.16
818
8.18
8.18
8,18
818
8.16
818
818
8.16
8 16
8.18
8.18
8.16
8.18
8.16
816
816
6.16
8.16
•.17
817
6.17
8.17
817
817
8.17
8,17
8,17
8.17
8,17
817
8-17
6,18
8.16
8,18
818
816
818
8,18
8.16
8.16
8,18
8,18
6-18
816
816
8,18
818
8,16
8.18
8-18
8-18
8.18
8.16
818
8.18
gpm
7.2
7.2
7.2
7.2
72
72
7,2
7,2
7,2
72
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7,2
7.2
7,2
7,2
7,2
72
7.2
72
7.2
72
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
72
72
7,2
72
7.2
72
7.2
7.2
7.2
7,2
7,2
7.2
72
72
7.2
72
7.2
7.2
7,2
7.2
7.2
7,2
7,2
7,2
7,2
7-2
72
72
7.2
7.2
7.2
7.2
7.2
7.2
-------
FURNACE A WITH CATALYST-HIGH HEAT REMOVAL RATE
27-Oct-W RinTTCD-2
ttne ttack (Mutton m
we
25636
25696
25756
25816
25876
25936
25996
26056
26116
26172
26232
26292
2E352
26412
26472
26532
26592
26652
26712
26772
26832
26892
26952
27012
27072
27132
27192
27252
27312
.. 27372
O
LK) 8.6311111 test
r
217
217
217
217
217
217
217
217
217
216
217
217
217
217
217
216
214
214
214
213
212
211
211
210
210
210
209
209
208
208
145
hn
r
99
98
98
96
Si
99
100
100
101
100
100
99
99
99
99
98
98
98
98
98
97
98
97
97
97
97
97
97
96
98
83
nbhrt waler-oul wrtirln elovaml lk»bo» COMgti COdUton
F ~
67
67
67
67
67
67
67
67
66
68
68
69
69
69
69
68
88
66
66
68
67
67
67
67
67
67
67
67
67
67
69
f
171
172
172
172
172
172
172
173
173
173
173
173
173
174
174
174
174
174
174
174
174
175
175
175
175
175
175
175
175
175
172
f
160
160
161
161
161
161
162
162
162
162
162
162
162
1S3
162
163
163
163
163
163
163
163
163
163
163
164
164
164
164
164
161
r
269
269
268
268
269
268
267
267
267
266
267
267
267
266
265
265
263
264
263
262
261
260
259
259
259
258
258
257
257
258
183
p
709
724
731
734
732
723
715
708
669
677
677
668
661
656
656
667
669
666
665
664
665
665
663
661
660
654
658
658
653
647
596
%
0.8
0.6
06
0.6
0.6
0.6
0.6
0.6
0.6
0.6
0.6
0.5
0.5
0.5
0.5
06
0.6
0.6
0.8
0.6
0.6
0.6
0.6
0.6
0.7
0.7
0.7
0.7
0.7
0.6
1.37
ppm
964.2
978.4
983.2
966
931.8
912.1
956.1
1005.7
962.1
1022.1
906.9
859
858.6
691.3
925
918.9
905.6
940.1
969.7
960.1
993.8
993
1028.8
1068.1
1129.1
1140.8
1124.6
1103.2
1048.7
1032.1
CO low
ppm
50195
5017.1
5018.3
50187
50175
50195
50178
5019.1
5017.5
5018.7
50163
5016.3
5015.1
5006.9
5016.3
5016.7
5017.9
5016.7
50198
5016.7
5019.1
5018.7
5017.1
5017.5
5016.7
5015.9
50175
5019.9
50208
5017.1
O2
*
1366
1366
13.69
13.71
1373
1382
1391
1395
14.04
14.15
14.21
14.16
14.14
14.16
1429
1436
1435
1437
14.41
1446
1448
14.47
14.52
1452
14.55
1456
14.6
14.65
1472
148
1106
CO2 JUM-THC taatanc* cat*m
X
684
687
685
682
681
671
662
855
646
832
6.3
634
635
625
606
601 .
603
6
594
593
593
5.95
591
591
568
5.86
564
58
5.74
566
939
ppm
346
339
334
332
335
332
333
339
349
354
373
336
328
330
334
339
340
337
326
330
326
325
314
306
303
299
293
263
280
276
2533
tn
4
35
35
55
35
3
25
2
1.5
1
0.5
05
OS
OS
OS
05
05
OS
OS
0.5
0.5
0.5
0.5
0.5
OS
05
05
05
05
0
r
554
552
552
550
549
546
545
543
541
539
540
539
538
537
535
532
529
525
522
519
517
515
512
510
508
SOS
504
503
501
499
477
397.86667 test rrtn
06:38:52 hrm
rttc
flow rat*
Opm B
7.2
72
7.2
7.2
72
72
12
72
7.2
72
72
72
7.2
72
72
72
72
7.2
72
72
72
7.2
7.2
7.2
72
7.2
7.2
7.2
72
72
7.2
Tot* Btu out*
Total Btu h •
Efficiency •
Water Aowrate •
Bumrate'
WoodmoMure »
Burnt*™-
Dmtyof Water meter
heal out Draft cod water reacfno
tuMarval CrtOfT
6459 On
704.7 On
6457 On
6457 On
6457 On
6457 On
5866 On
645.5 On
8240 On
624.0 On
645.5 On
645.3 On
6455 On
6453 On
704.2 On
645.3 On
645.3 On
6453 On
645.3 On
6453 On
645.3 On
703.9 On
703.9 On
703.9 On
703.9 On
645.1 On
645.1 On
645.1 On
645.1 On
6451 On
6618
284,739 Btuout/hr.
556,757 BtukVhr*
47.55H
7.20 gpm
4.73 orykgfr
21.74%
683hr
Rwbal
8.16
8.16
8.15
8.15
8.15
8.15
8.15
8.15
8.15
6.15
8.15
6.15
8.15
8.15
8.15
6.15
815
6.15
8.15
6.15
8.15
6.15
8.15
8.18
8.15
8.14
8.14
8.14
6.14
8.14
6.15
39.924
83461
gpm
72
7.2
7.2
72
7.2
72
72
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
72
7.2
13
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
-------
FURNACE A WITH CATALYST- LOW HEAT REMOVAL RATE
Printed on 02-Apr-96
2&-Qei-e5 RunTTCCM
time smbi*nf dlution stacfc
SBC r C C
5772
5832
5882
5852
6012
6072
6132
6182
8252
8312
6372
8432
6492
8552
6612
6672
6732
6782
6852
6908
6BB8
7028
70S8
7148
7208
7268
7328
7388
7448
7508
7588
7828
O 7688
7748
tyi 7808
-L^, 7888
7928
7886
8048
8108
8168
8228
•284
8344
8404
8464
8524
8584
8844
8704
87B4
8824
88E4
8844
9004
9064
9124
9184
9244
9304
9364
9424
9484
9544
8604
9860
8720
9780
9840
9900
9860
10020
10080
10140
71
72
72
72
72
72
72
71
71
71
71
71
72
71
72
72
72
71
72
72
72
72
72
72
72
72
72
72
72
73
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
73
73
72
73
73
73
73
72
72
71
89
88
•7
67
66
66
38
84
84
85
86
87
88
92
86
99
101
103
104
105
106
108
111
115
120
123
128
128
128
102
90
85
82
81
80
78
78
77
77
77
77
77
77
78
78
78
78
78
76
78
76
76
78
76
77
77
77
77
77
77
77
77
77
77
77
77
77
77
77
77
78
75
74
73
73
72
72
72
73
74
141
141
143
147
153
159
165
178
189
196
204
208
213
216
220
228
240
257
271
279
285
289
282
248
208
186
173
166
158
165
151
148
145
144
143
141
140
139
137
137
137
137
137
136
135
135
135
135
135
136
136
136
136
138
139
139
136
138
138
138
138
138
138
138
139
140
139
141
140
140
141
140
138
140
stave fire-box water oul water (n CO Wrft CO dlu
p c c 1- „.
178
178
180
185
191
197
205
223
242
255
268
277
285
289
285
302
313
325
338
344
349
352
352
285
241
221
205
195
188
183
179
176
174
172
170
169
18?
166
184
163
163
162
162
181
161
161
180
160
160
181
181
181
161
181
162
162
162
163
163
163
183
163
163
163
183
183
163
164
164
164
164
164
164
165
191
214
287
361
410
452
485 ,
557
781
986
1103
1153
1153
1153
1153
1153
1153
1153
1153
1153
1154
1154
1154
1141
834
806
752
711
679
656
637
617
801
586
575
563
551
543
534
527
520
514
508
SOS
503
498
406
484
483
485
485
485
485
485
496
496
498
500
500
502
504
506
507
509
512
615
518
521
523
525
528
531
531
531
164
163
163
163
183
182
163
162
183
164
165
166
167
166
169
170
171
172
173
174
175
176
176
177
177
177
177
177
177
177
178
177
177
177
177
177
177
177
177
177
177
176
176
175
175
174
174
174
174
173
173
173
173
173
173
172
173
172
172
172
172
172
172
172
172
172
172
172
172
172
172
172
172
172
r
157
15?
157
158
156
156
156
158
156
157
156
159
160
161
161
182
163
164
185
186
167
167
169
168
170
170
170
170
170
170
169
169
170
170
170
189
170
169
169
169
169
168
166
168
18S
187
187
166
166
168
166
166
166
166
165
165
165
165
165
185
165
165
165
165
165
165
184
194
184
164
164
164
164
164
%
0.318
0283
0.436
0.537
0.588
0.645
0.947
0.928
0.783
2.05
2.708
2981
3013
3012
3.014
3.013
3012
3.012
3.013
3.013
3.013
3.013
3.013
3.013
3.013
2884
1.98
1247
0.966
0.873
0815
0.767
0.743
0726
0743
0.744
0.748
0.757
0.778
0.805
0.823
0.827
0.862
0.891
0.926
0.858
0876
1001
1.051
1.123
1.21
1.309
1.423
1.543
1648
1.754
1805
1875
1938
1-957
1.89
2.044
2.104
2.15
2.221
2.253
2.309
2364
2.471
2.531
2584
2U
2.687
2.727
484
718
W3
1091
1207
1253
1203
1252
186*
2007
2007
2008
2007
2007
2007
2007
2008
200?
2007
2007
2007
2007
2007
2008
1909
964
584
436
381
346
323
308
300
296
298
297
300
306
313
319
330
337
348
358
388
385
388
417
445
480
519
561
601
845
688
710
744
768
793
799
821
843
845
888
898
817
939
969
993
1030
1054
1073
1082
1104
CO tow
ppm
3177
2585
4331
5017
5017
5017
5017
5016
5017
5018
5016
5018
5016
5017
5017
5016
5015
5016
5017
6015
5018
5017
5016
5015
5017
5016
5016
5017
5017
5016
5017
5016
5017
5016
5019
5015
5017
5017
5017
5018
5016
5016
5015
5017
5018
5018
5014
5015
5016
5018
5017
5016
5015
5015
5017
5015
5017
5017
5016
5015
5017
5015
5015
5017
5016
5017
5015
5018
5015
5016
5018
5018
5014
5015
02
18.96
1978
1839
17.6
16.97
1635
15.85
14,77
11,88
792
6.75
62
5.77
5.4
5.11
474
4.55
4.31
394
3.66
355
345
3.38
375
7.34
10,73
12.14
12.55
1264
1287
1301
13.27
1345
1361
1363
1378
139
1396
1397
13.93
1391
14,07
1388
13.92
1384
13.81
1386
13.9
13.8
1363
1348
1339
13.24
1309
1307
1294
1294
1282
1284
1295
1285
12.9
12.77
12.71
12.58
1258
1248
1247
12.24
12.2
12.18
1207
12.14
1224
CO2 JUM-THC
2.13
1.43
2-88
3.58
4.25
4.82
5-32
646
8-33
1314
1412
14.66
1511
15.47
1578
1618
16.31
16.48
18.76
16-97
17.04
17.0»
17.09
16.74
14.31
1068
8.74
8.17
8.01
7.77
7.63
741
726
7.07
714
704
694
08
6.94
7.03
706
8.94
7.05
7.15
7.27
7.33
7.32
7.35
7.48
7-69
788
8.01
62
8.36
84
856
8.6
865
8.75
8.89
872
».7B
8.95
9.03
9.2
8.21
9.32
9.38
884
869
971
989
982
875
273
340
290
283
309
363
394
445
512
558
550
535
577
1429
2116
2858
3390
3758
3506
3274
3551
3884
3820
3683
3078
3251
3825
5022
0399
3023
1471
1322
1281
1246
1222
1301
2273
2597
2561
2851
2572
2559
2613
2689
2710
2770
2787
2926
3103
3360
3651
3985
4370
4496
4657
4754
4913
4664
4828
4888
8105
5459
5404
5371
5441
5420
5489
5840
5861
6158
6508
6670
6428
6458
baa no
t»
87.5
87.5
87.5
87.5
875
87
865
855
84.5
835
82
81
785
78.2
77
75.7
74.5
73.5
72
78.5
68
87.5
86
85
65
64.5
64.5
64.5
64
64
94
64
64
63.5
635
635
635
83.5
83
63
83
63
63
825
82.5
82.5
62
62
815
91.2
61
605
60.5
60S
60,5
60.5
60
59.5
59.5
59
59
58
58
58.5
58
58
58
58.5
59
SB
58
58
56.5
58
Waltr
catalyst actual flow rate heat out
F
252
254
260
270
283
289
317
382
416
486
546
581
623
645
664
6S1
898
717
739
754
768
775
783
771
730
692
658
631
609
591
580
574
566
552
537
524
512
501
491
483
475
489
463
458
453
449
446
442
438
435
431
428
425
423
422
421
421
418
419
418
418
418
417
418
417
417
417
417
417
418
418
418
420
420
Qpffi 8t
8.4
6.4
84
84
64
6.4
64
6.4
84
64
8.4
64
6,4
64
8.4
8.4
6.4
64
84
8.4
8.4
84
84
8.4
64
8.4
8.4
8.4
64
64
64
64
6.4
6,4
64
64
64
64
6.4
64
8.4
6.4
8.4
64
64
64
64
84
84
64
84
64
6,4
64
6.4
6.4
84
64
64
6.4
6.4
8.4
6.4
6.4
6.4
6.4
6-4
64
6.4
64
64
64
64
64
385-2
313,0
313,0
3653
365.3
313.1
3853
3131
3853
385.2
365 1
3649
3848
364.7
416.8
418.7
4185
4164
3885
418,1
415,8
487-9
3837
415,8
3836
3836
383.6
383.6
3636
363.6
467,6
415,6
363,6
3636
383,6
415.8
3636
415.6
415.6
415.8
415.8
339.4
415.8
363J
3838
3639
363.9
416.1
4161
3641
364,1
364 1
364 1
384,1
4162
364,2
416.2
384.2
364,2
364.2
364.2
364.2
384,2
384.2
338.9
384.2
416.4
418-4
418,4
418-4
418.4
419.4
4164
4164
Density of Watef meter
Draft coo) wwtef rwadng
OrfOff
Off
Off
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Oft
Off
OB
OB
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
on
Off
Off
Off
Off
Off
Off
8.16
818
8.18
8,17
4,17
8,17
817
8.17
8,17
8.16
8.16
8.16
8.18
815
8.15
8.15
8.15
8 14
814
814
814
8.14
8.13
8.13
813
813
8.13
8.13
8.13
8.13
813
8 13
8 13
813
813
813
8.13
8.13
8.13
813
8.13
813
813
813
813
8.14
814
8.14
814
814
8.14
814
8.14
8.14
814
814
814
814
8.14
8.14
8.14
8.14
8.14
8.14
814
814
8 14
814
814
814
9.14
8,14
8 14
8.14
8.3
8.3
8.3
8.3
8.3
8.3
8.3
6.3
6.3
63
8.3
8.3
6,3
63
8,3
8,3
6.3
83
83
8.3
83
63
83
83
8.3
8.3
8.3
63
83
83
83
63
6.3
6.3
6.3
63
6.3
8.3
83
8.3
63
8.S
63
8.3
6.3
6.3
83
fl.3
63
63
6,3
83
63
63
63
6.3
6.3
6.3
93
63
83
83
8.3
83
83
83
6.3
6.3
63
8.3
63
8.3
6 3
83
-------
FURNACE A WITH CATALYST- LOW HEAT REMOVAL RATE
2S~Qd-8S RunTTCO-1
time ambient dlution stack stove 1
sec
10200
10260
10320
10330
10440
10500
10560
10820
10680
10740
10300
10860
10920
10930
11036
11096
11156
11216
11278
11338
11396
11456
11516
11576
11636
11696
11756
11818
11876
11938
11998
12058
d2116
2176
UK 2236
17112296
12356
12412
12472
12532
12592
12652
12712
12772
12832
12892
12952
13012
13072
13132
13192
13252
13312
13372
13432
13492
13552
13612
13672
13732
13788
13848
13808
13888
14028
14088
14146
14206
1426B
1432B
14338
14448
14508
14568
r-
88
88
87
67
88
88
88
88
88
88
69
70
70
70
70
89
88
88
87
87
87
87
87
67
88
68
88
88
89
88
68
88
69
68
87
87
87
87
87
87
67
88
68
88
88
88
69
70
70
70
70
70
69
69
68
68
87
87
68
83
88
88
68
SB
88
68
88
68
87
87
87
87
87
88
r-
74
75
75
75
75
78
76
76
78
78
77
77
77
78
75
74
72
72
72
73
74
74
75
75
75
75
78
76
78
78
75
74
73
72
71
71
73
73
74
74
75
75
75
75
75
75
75
75
75
75
74
73
72
72
71
72
73
74
74
74
75
75
75
75
73
72
72
71
71
72
73
74
74
75
r
140
141
140
141
143
144
143
143
142
140
141
141
141
141
141
142
140
140
140
138
138
138
137
137
138
137
138
138
138
137
139
134
13*
134
133
134
U3
133
133
134
132
131
133
130
131
131
130
131
131
129
130
12B
128
129
127
126
126
126
12S
128
125
126
124
12S
123
123
123
124
123
121
121
121
122
118
r
135
185
165
186
166
166
166
188
188
188
189
185
165
165
165
164
166
165
185
184
183
183
182
162
162
162
182
182
161
161
180
180
180
160
180
180
180
159
198
198
189
188
158
158
167
157
157
196
166
166
158
155
195
155
154
153
152
151
151
151
150
150
150
149
149
150
150
150
149
148
148
148
148
148
re-box water out w
F
532
538
540
848
550
558
891
580
883
887
870
873
578
878
579
682
984
988
887
680
591
891
580
689
58B
9BO
839
5BO
589
639
982
594
585
98B
612
619
822
623
821
820
619
619
820
820
615
614
614
814
814
815
814
815
819
616
817
618
817
818
616
81 S
813
612
812
812
614
816
618
619
817
613
810
808
808
803
F
171
171
172
172
171
171
171
171
171
171
171
171
171
171
171
171
171
171
171
171
171
171
171
171
171
171
170
170
170
170
171
170
170
170
170
170
170
170
170
170
170
170
170
170
170
170
170
170
170
170
170
170
170
170
170
170
189
170
170
189
189
168
189
168
189
169
169
169
169
168
169
189
188
189
aterln CON0I COdki COkw
F
184
164
164
164
184
184
184
184
1*4
164
184
184
184
184
184
183
183
1*3
183
1*3
183
183
1*3
163
183
1*3
162
183
183
183
1*3
1*3
182
182
162
182
1*2
1*3
183
183
182
182
1*2
1*2
182
182
162
182
1*2
1*2
182
182
182
182
1*2
1*2
182
182
182
182
1*2
1*2
182
1*2
182
181
161
1*1
181
1*1
181
181
1*1
1*1
%
2729
2788
2857
2924
2982
3.012
3.013
3013
3.013
3.012
3.013
3012
3012
3013
3.013
3.013
3.013
S.012
3.014
3.013
3.012
3012
3012
3012
3013
3013
3.013
3.013
3.013
3.012
2.965
2.96
2995
3013
3014
2.994
2783
2.676
2.809
2.58
2513
2.513
2.516
2518
2459
2642
2.74
2.72
2.783
2.81
2.793
2.828
2.308
2.783
276
2627
2513
2458
2.405
2.35
2388
2.381
2342
2316
2.375
2.359
2296
2212
2.203
2.173
2.12
2.11
2.137
2.112
R***
1132
1166
1193
1208
1224
1251
1270
1279
1284
1288
1303
1308
1308
1308
1288
1313
1333
136S
1381
1393
1380
1398
1329
1309
1292
1278
1240
1221
1199
1181
1184
1187
1203
1220
1241
1083
1031
1033
1008
892
978
984
660
883
1001
1049
1084
1084
1087
10S8
1082
1050
1028
993
998
80S
831
389
852
838
33$
839
838
838
63S
811
778
788
798
747
7S4
784
757
747
ppm
5015
6018
5015
5015
5016
6015
5016
5016
9019
9016
5017
5017
6018
5016
5013
5016
5016
5018
6016
6015
8018
5018
5017
5016
5016
6015
8017
9016
5016
8017
8016
6015
6016
5018
6015
5015
5018
5017
5018
S018
6018
5017
5017
5018
5015
5018
5018
6018
5017
5017
5017
5015
601*
6016
9017
9018
5017
6016
5017
5017
5016
9017
6016
6016
901*
5018
5013
5016
5019
5017
5016
5017
5018
6017
O2
%
1241
12.35
12.24
1214
1201
11.71
116S
11 73
1171
1176
11.83
11.83
11.75
11.75
11 69
11.94
1132
11.38
11 27
11.28
11.8
12.02
12.09
12.03
11.92
11.8
11 98
11.B
11.75
11.72
11.6
11. 88
11.68
11.42
11,5
11 39
11.3
11.82
11.71
11.78
11.66
118*
11.88
11.88
11.87
11.78
11.72
1191
11 75
11.88
117
1183
11.81
11.38
11.2
11.3
11 4
11.44
11.51
11,87
1137
1133
11.47
11.88
11,32
11.22
11 07
11.09
10.B3
1101
11.34
11.52
1164
11.53
Water
CO2 JUM-THC balance cutaljtt actual How rate heat out
%
9.59
9.71
8.82
983
1006
10.38
10.41
10.31
10.31
10.25
10.17
10.17
10.26
10.25
1035
10.47
10.7
10.«3
10.73
10.71
10.37
9.98
983
10.01
10.14
10.28
10.09
1016
10.31
10.S1
10.11
10.09
1033
1049
10.37
1044
1061
10.43
10.21
10.14
10,34
10.2
10.21
10.28
993
1005
10.03
884
10,02
1008
10-04
10.18
10.17
10,21
10,38
10.18
10.04
9.98
9.91
9.*7
10.07
10.09
993
9.a*
10.13
10.2
1035
1035
10.46
10.35
10
98
9.14
9.83
PpfR
8874
8896
8884
8688
6697
689S
8883
8888
8888
8899
8695
8884
8895
8884
8893
8898
8884
8884
889$
6694
6683
6884
6688
8694
88S9
8879
8882
8884
8860
8872
8484
6552
8493
6320
8153
8082
8901
5750
9872
5703
S728
5602
5481
558B
5732
5857
5887
5849
6384
8808
5888
5823
5777
6S7B
5371
5083
4898
4833
4341
4098
4009
3827
3760
3883
3345
3184
3024
3008
2974
2824
2827
2547
fc»
57.9
97.4
57
58.5
58
555
55
94.5
54
94
53.8
53
53
52.5
52.5
S3
63.5
93.6
53.5
53
52.8
52.5
52
51
51
90.9
50
60
489
49.5
49
49
49.5
497
50
SO
49.5
48
43.5
43
48
47.5
47
47
485
46
496
45.9
45
44.5
44
44.5
49
49.9
45.5
45
45
44
44
43.5
43
43
43
42.1
42.5
42.5
43
435
43.5
43
425
42
41.5
41
F
420
421
421
421
422
422
422
421
420
420
420
419
418
417
417
416
416
418
418
418
418
416
416
415
415
414
415
414
414
413
41S
413
413
413
415
417
418
418
418
418
417
417
416
418
414
414
413
413
4t3
413
414
414
414
414
414
413
413
412
413
412
412
412
412
412
412
412
411
412
412
411
412
411
410
409
gpm Bt
6.4
8.4
6.4
64
84
8.4
64
8.4
84
94
6.4
84
84
8.4
84
64
8.4
6.4
• 4
6.4
8.4
8.4
64
6.4
6.4
6.4
6.4
*,4
84
84
6.4
8.4
84
6.4
6.4
64
6.4
8.4
84
8,4
84
64
6,4
8.4
84
8.4
64
64
84
8,4
8-4
6-4
8.4
6,4
64
64
6.4
64
*.4
84
6.4
6.4
8.4
84
64
6.4
64
6.4
6
8.
6
8
8
8.
uMarval
364.3
3643
4164
416.4
364.3
384.3
384.3
384.3
3B4.3
384.3
384.3
364.3
364.3
3400
384.3
416.5
418.5
4185
416.5
418.5
418.5
416.8
416.5
418.5
416.6
418.5
4187
384.5
384.5
384.5
418.5
384.5
418,7
418,7
416-7
416.7
388.9
384.5
384.5
394.8
4187
4167
4167
416.7
416.7
4187
4167
416.7
416.7
416.7
418.7
418.7
416.7
418.7
418.7
416.7
3848
4187
418.7
340.3
3848
384.8
364.8
384.6
3848
4188
4188
418.6
416.8
416.8
4188
4188
41B3
416.8
Draft
On/Off
Off
on
Off
Off
on
Off
ow
Off
on
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
on
Off
Off
on
on
on
on
Off
Off
OB
OB
on
Off
Off
Off
on
on
Off
Off
Off
Off
on
on
on
on
Off
Off
on
Off
Off
Off
Off
Off
on
Off
Off
Off
on
Off
OB
Off
Off
Off
Off
Off
on
on
on
on
Off
Off
OH
on
Demit? of Water meter
eool water reasing
i^oal
8.14
8.14
8.14
8 14
8.14
8.14
814
8.14
8.14
8.14
3.14
3.14
8.14
8.14
8.14
8.15
8.15
8.15
8.18
8.15
81$
8.15
8.15
8.15
815
8.15
815
8.15
8.15
8.15
815
8.19
8.15
8-15
8.15
815
815
815
8.19
8.19
8.15
8.15
3.15
8.15
8.15
8.15
8.15
B.1S
8 15
8.15
815
8.15
8.15
815
815
a is
815
8.16
8.15
8,15
8.15
S.15
8.15
8.15
8.16
8.15
815
8 15
3.15
8.15
8.15
8.18
8.15
3-15
pm
6.3
6.3
8.3
6.3
63
63
8.3
*,3
8.3
8.3
8.3
8.3
*.3
6.3
63
83
6.3
83
8.J
e.j
83
8.3
63
83
8,3
6.3
8.3
8.3
8.3
6.3
8.3
83
8.3
8.3
83
6.3
83
83
8.3
e.a
6.3
6.3
8.3
8.3
83
83
63
6.3
0,3
83
83
83
83
83
8,3
6.3
6.3
83
8.3
8.3
8.3
83
63
8.3
6.3
63
6.3
83
8.3
83
8.3
6.3
6.3
6.3
-------
FURNACE A WITH CATALYST- LOW HEAT REMOVAL RATE
PrtiMon 02-Apf-M
2S-Oct-95 RunTTCO-1
tim« ambient dkltion Made stove fire-box water di* walerln COhitfi COdki CO tow
SAC
14828
4868
4748
4808
4868
4828
14988
15048
15108
15184
15224
15284
15344
15404
15484
15524
15584
15844
15704
15784
15824
15884
19844
19004
16004
18124
181B4
18244
14304
18364
18424
184S4
,_jl«540
W6800
(_fti8960
(3x18720
18780
18840
18900
18980
17020
17080
17140
17200
17280
17320
17380
17440
17500
17580
17820
17880
17740
17800
17860
179H
17978
18038
18098
18156
18216
18276
18336
18388
18498
18516
1857B
18630
18698
18798
16818
18878
18938
18968
r
68
69
69
69
68
68
67
66
66
66
66
66
86
67
68
68
88
69
69
69
70
69
68
68
88
67
67
66
66
68
67
67
87
68
68
69
89
89
89
68
68
67
87
67
67
87
67
68
88
89
89
88
69
69
69
88
88
87
87
87
68
68
69
68
89
89
70
89
89
88
68
87
67
88
r
75
75
74
73
72
71
70
70
71
72
73
73
74
74
74
74
75
75
75
75
74
73
72
71
70
70
70
71
72
73
73
73
74
74
74
74
74
73
n
71
70
70
71
72
73
73
73
77
91
95
99
95
104
107
107
10S
108
103
85
81
79
78
78
77
77
76
75
73
73
71
71
72
73
74
r
123
124
122
122
121
121
119
120
117
118
117
116
116
117
117
118
lie
117
115
115
112
111
112
111
112
112
111
110
111
112
111
111
112
111
112
111
110
108
110
109
108
108
107
107
107
110
108
118
152
172
190
181
208
231
243
250
255
252
191
168
150
144
140
137
133
130
128
124
123
11)
118
118
115
11S
r
148
148
148
148
148
147
146
146
145
144
144
143
143
143
143
141
141
141
140
139
139
139
138
139
138
137
137
138
137
1M
137
137
136
137
138
138
136
135
135
135
135
134
134
134
134
135
13S
155
229
2S3
267
2S7
288
312
323
331
338
331
257
211
188
177
171
187
183
180
157
154
152
150
148
147
145
144
1-
604
603
802
602
600
599
600
603
608
808
806
603
601
598
596
595
59<
592
589
586
586
587
587
588
591
593
592
592
590
887
584
S82
582
582
580
579
57«
578
S78
578
575
575
574
572
570
569
568
589
1014
1155
1155
1155
1155
1155
1155
1155
1158
1158
1156
1110
1014
836
863
815
784
780
745
730
718
707
894
680
869
859
f
189
168
169
169
189
169
186
16B
169
169
16»
169
168
168
188
169
188
168
188
168
168
188
188
188
188
168
168
168
1«8
188
168
187
16S
167
1«7
197
167
168
188
167
187
187
1»7
187
167
187
167
167
197
108
138
170
171
172
173
174
176
177
178
178
179
179
178
178
178
178
179
179
179
17»
179
179
179
179
f
181
161
181
181
181
181
181
141
160
HI
181
161
181
161
161
161
181
161
HI
160
181
180
190
180
160
180
180
180
160
180
160
160
160
160
180
160
180
160
180
160
159
159
160
160
160
160
160
160
15*
160
181
182
163
184
165
166
167
168
168
170
170
171
171
171
171
171
170
170
170
171
170
170
170
170
%
2-085
2-166
2.191
2,175
2.183
2.161
2.126
2.072
2.048
2
1.984
1.836
188
1819
1.787
1.728
1.877
1.812
1.504
1.534
1.512
1.501
1.486
1.488
1.476
1.5
1,5
1485
1 485
1,528
1 515
1498
1.46
1 488
1.452
1.441
1.417
1.368
1302
1.427
1.413
1417
1.384
1312
1.398
1.412
1.432
1.4Z1
1.488
2.688
3.011
3.013
3014
3.012
3011
3-013
3.014
2.978
2865
3.013
3013
3.012
3-012
3,013
2.929
2.811
2.408
2.233
2017
1.77T
1514
1.31S
1.175
1-076
ppm
736
739
741
741
732
719
704
88S
674
600
652
628
907
573
946
527
514
504
490
477
479
474
471
465
462
462
490
448
448
448
441
440
431
427
423
415
420
418
417
424
425
421
409
408
408
412
413
853
2007
2007
2007
2007
2007
2007
2007
2007
2007
1981
1841
2007
1828
1575
1290
1099
957
858
788
707
614
523
438
368
334
307
tpra
5017
5017
5017
5017
5016
5016
5018
5015
5016
5017
5017
5015
5017
5017
5016
5018
M16
5017
5015
5018
5015
5018
5018
5017
5017
5017
5018
5016
5017
S017
5017
5016
5017
5017
5017
5018
5018
5017
5016
5015
5017
5018
5015
5017
5018
5017
5017
5018
5018
S017
5015
5018
S017
5015
5017
5017
501S
5015
5018
5018
5015
5016
5016
5017
5017
5018
5018
5018
5016
5018
5018
5017
5017
5015
O2
%
11.58
11 17
11.04
11.05
11.02
11,02
10.87
11.02
10.03
11.1
11.28
11.28
1134
1132
11.18
11.08
11.04
11 16
11.17
1125
11.23
11.21
11.22
1108
11.11
10.93
10.83
11.03
1108
10.88
10.89
10.83
1109
10.93
10.95
10.9
10.88
11.2
11
1078
1095
10.95
11.13
11 18
11.08
11,02
1088
1088
9.4
S.S9
4.49
4.17
4.74
3.76
348
3.51
3.SS
385
4.82
7.82
8.88
9.32
9.53
8.58
10.1
10.58
10.72
10.72
10.76
10.71
10.78
10.8
10.86
10.98
Water
CO2 JUM-THC befenee catalytt actual (tow rate heat out
%
9.88
1028
10.38
10.35
10.38
10.36
1037
10,2*
10.33
10.13
9.84
8.9
8.8
8.77
9.9
998
9.97
986
9.85
9.76
877
8.78
8.77
9.87
984
10
10
988
8.87
10.07
10.05
1002
989
1009
10.03
1008
10.02
9.8
8.88
10.19
10
10.02
984
9,81
8.81
887
1009
886
1158
14.13
14-13
14.11
13.73
15.12
1588
18.28
18.39
1638
15.17
12.93
1211
11.53
11.08
10.74
10.17
8.72
8.6
881
864
973
8.72
8.75
875
8.85
ppm
2625
2697
2823
2516
2509
2583
2461
2210
2210
2328
2509
2338
2283
2306
2481
2550
2240
2128
2329
2438
2187
2019
1991
2007
1851
1895
1707
1783
1777
1681
1543
1563
1540
1535
1438
1482
1538
1561
1516
1437
1452
1432
1357
1314
1296
1324
1344
1318
1314
1333
1364
1300
1339
1381
1403
1318
1255
1235
1283
1791
2255
2537
2812
2918
2617
2288
2144
2116
2118
3191
4808
4355
3203
2477
fc«
41
40
40
40.5
41
418
42
42.5
42
41 .8
41.1
41
40.5
40.5
40
395
39.5
38
38
385
38
3)
30.5
395
40
405
40.5
40
38.5
38.5
39
39
39
385
385
383
38
38
38.5
39
395
40
395
38
38.5
38
37.5
37.5
36
35
34
33
32.5
32
31.5
31
30.5
28
28
27
265
28.5
28
28
28.5
25.5
25.5
26
27
27.5
27.5
27
26.5
28
F
409
410
409
409
409
409
408
408
408
408
407
408
407
408
406
405
40S
404
404
403
402
402
402
401
401
401
401
401
401
401
401
400
400
400
400
388
399
398
398
398
398
398
388
388
398
388
397
397
463
552
617
648
978
719
784
795
824
848
831
791
746
712
87»
849
824
900
580
562
547
534
823
510
498
488
flpm Btuflrtervil
«4 416.8
6.4
64
8.4
64
6.4
6.4
6.4
8.4
6.4
6.4
84
6.4
94
6.4
8.4
64
64
64
64
84
9.4
6.4
6.4
84
6.4
64
6.4
94
8.4
84
8.4
64
8.4
8.4
64
8.4
64
6,4
84
84
6.4
64
64
8.4
8.4
84
6.4
6.4
8,4
8.4
8.4
64
6.4
6.4
64
8.4
6.4
84
9.4
84
84
8.4
8.4
8.4
64
8.4
6.4
6.4
6.4
84
6.4
64
8.4
418.8
418.8
418.8
416.8
4168
418.8
4188
437.8
4168
4188
418.8
3847
3847
364.7
418.8
394.7
3647
364.7
4169
384.7
418.9
416.9
416.8
416.9
416.8
4189
416.9
418,8
418,8
416,9
3405
416.9
3948
364.8
384.8
394.8
418.9
4198
3948
417.1
417.1
3648
3948
384.8
3848
384.8
384.8
417.1
416.8
4188
419.7
4185
4164
3885
416.1
467.8
4878
467.8
415,5
4874
415,3
4153
415,3
41S3
415,3
467,4
487,4
467.4
415.3
497.4
4674
4974
4874
Density of Water meter
Draff cool water rearing
OVOff
Off
on
C4I
on
on
OR
on
CHI
Off
OR
Off
Off
on
Off
Off
Off
Off
Off
Off
Off
Off
on
Off
Off
Off
Off
Off
on
Off
on
Off
wr
Off
Off
Off
Off
Off
Off
Of
Off
Off
Off
Off
Off
Off
Off
Off
Off
On
On
On
On
On
On
On
On
On
On
On
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
on
Off
Off
tygal
8.15
815
815
8.15
8. 15
815
8.15
815
8.16
8 15
8 IS
8 15
815
815
8.15
8.14
8.15
8 15
8.15
818
815
818
e 16
816
8.16
816
816
8.16
818
818
818
818
8 18
816
8.16
8.16
818
8.18
8.18
8.18
818
816
8.18
8.16
8.16
8.16
816
8.16
818
8.16
8.1S
815
815
8.14
8.14
8.14
8.14
8.13
813
8.13
813
6.12
8.12
8.12
812
812
8.13
8 13
813
812
813
813
813
8.13
6.3
63
63
63
63
83
83
93
93
93
8.3
93
9.3
8.3
83
83
93
83
93
63
8.3
83
6.3
63
6.3
8.3
63
6.3
S3
63
93
83
83
93
9.3
93
93
83
83
63
93
6.3
63
83
63
63
63
63
83
93
83
83
63
63
63
63
83
83
63
83
83
63
63
83
83
8.3
6.3
6.3
6.3
6-3
83
6.3
83
63
-------
FURNACE A WITH CATALYST- LOW HEAT REMOVAL RATE
Printed on 02-Apr-98
25-OCI-95 Run TTCD-1
time ambient dlution stack stove fire-box water out water in CO higft CO dlu CO low
sec "~ "~ "
19056
19116
19176
19236
19292
19352
19412
19472
19532
19592
19652
19712
19772
19832
19892
19952
20012
20072
20132
20192
20252
20312
20372
20432
20492
20552
20612
20688
20728
20788
20848
20908
l_,20968
O2102S
U121088
•^121148
21203
21268
21328
21388
21448
21508
21568
21628
21688
21748
21808
21868
21928
21988
22044
22104
22164
22224
22284
22344
22404
22464
22524
22584
22644
22704
22764
22824
22884
22944
23004
23064
23124
23184
23244
23304
23384
23420
r
68
68
68
69
69
70
70
70
69
69
68
67
87
67
67
67
67
67
67
68
68
69
69
70
70
70
70
70
69
88
68
67
67
67
67
67
67
68
68
68
69
69
70
69
68
68
67
68
68
68
86
88
68
67
68
88
68
89
69
88
88
67
67
67
67
67
67
68
68
67
67
68
68
66
r
74
75
75
75
75
75
75
74
73
72
71
71
70
70
72
72
73
73
74
74
74
74
74
74
74
74
72
71
71
70
69
69
70
72
73
73
74
73
74
74
74
74
73
72
71
70
69
89
70
71
72
72
73
73
74
74
74
73
72
71
70
89
70
71
72
73
73
73
72
71
70
70
70
71
r
115
115
114
113
112
110
109
109
108
106
106
105
103
102
101
101
102
102
101
101
101
101
100
100
99
98
98
98
97
98
96
95
94
94
94
94
94
94
93
93
93
93
93
93
92
92
92
91
90
89
90
90
91
91
91
91
91
91
91
91
90
90
89
90
90
90
91
90
90
89
90
89
88
88
r
143
143
142
141
140
140
139
137
136
135
134
134
134
133
133
133
132
132
132
132
132
132
131
131
131
130
129
129
128
127
127
126
126
127
127
127
127
127
126
126
127
126
126
124
124
124
123
123
123
123
124
124
124
123
122
123
124
124
124
123
122
122
122
122
122
123
122
123
123
122
122
121
121
121
i-
648
640
631
623
616
609
601
595
591
587
583
578
574
571
566
562
558
554
549
544
540
536
533
532
533
531
530
529
526
524
523
520
518
515
512
509
507
505
504
501
500
499
498
497
496
497
496
495
495
494
491
490
488
485
484
481
481
479
479
480
482
483
483
480
480
479
476
474
473
474
473
474
474
474
r
179
179
178
178
178
178
178
178
178
177
177
177
177
177
177
176
176
176
176
176
176
176
176
176
176
176
176
176
175
175
175
175
175
175
175
175
175
175
175
175
175
174
174
174
174
174
174
174
174
174
174
174
174
173
173
173
173
173
173
173
173
173
173
172
172
172
172
172
172
172
172
172
171
171
F
170
170
170
170
170
170
170
170
170
169
169
169
188
188
168
168
168
188
188
168
168
168
168
188
168
168
167
187
187
167
167
167
167
167
167
167
187
167
166
167
167
166
166
166
166
166
165
165
185
166
166
166
166
165
165
165
165
165
165
165
164
164
165
184
164
164
164
164
184
164
164
164
163
163
%
1023
0.981
0932
089
0.858
081
0.771
074
0.73
0.708
069
0684
0667
0653
0.63
0816
0613
0603
0587
0.587
0.575
0558
0548
0539
0529
0.521
0523
0548
0.56
0558
0553
0549
0533
0529
0524
0513
0.5
0502
0.501
0.49
0495
0.498
049
0491
0503
0507
0.52
0.514
0514
0506
051
052
0517
0521
0.516
0508
0512
0505
0509
0509
0511
0514
0524
0528
0549
0548
0.55
0554
0548
0535
0.527
0538
0.54
0537
ppm
286
268
250
236
220
209
201
194
187
181
176
172
166
160
151
147
142
139
132
129
127
124
119
118
115
124
126
129
125
125
123
120
111
108
106
106
104
101
103
100
101
106
105
108
106
109
109
109
106
101
101
99
99
100
97
97
101
103
104
105
105
108
104
102
102
102
101
106
106
110
109
111
111
105
ppm
5018
5017
5017
5017
5015
5016
5017
5017
5016
5015
5015
5017
5018
5017
5019
5016
5016
5018
5016
5017
5018
5015
5017
5015
5017
5014
5017
5016
5018
5018
5017
5018
5015
5017
5016
5017
5014
5017
5017
4960
5002
5008
4959
4987
5017
5017
5015
5016
5017
5018
5018
5018
5016
5016
5015
5018
5017
5017
5018
5015
5018
5015
5016
5015
5016
5018
5017
5017
5017
5016
5017
5018
5016
5017
O2
%
1088
1074
107
1069
1062
1068
1073
1078
10.58
1063
1071
1056
1063
1068
1088
1089
10.75
1089
10.78
1059
1056
107
1074
10.77
10.81
11.08
11.51
11.37
11.24
11.22
1125
11.25
11.4
11.42
11.3
11.39
1157
11.54
11.51
11 72
1165
1159
1173
1186
1173
11.78
1156
1172
11 75
11 93
1182
1163
11.58
1149
1155
1166
1161
1166
1166
11 74
1183
1191
1192
1198
11.67
11.61
11.54
1141
11.52
11.74
1201
119
12.01
12.12
Water
CO2 JUM-THC balance catalyst actual (low rate heat out
%
9.77
99
991
993
999
992
987
983
998
995
989
10
993
969
969
9.68
984
9.87
979
997
996
986
981
978
972
942
9
91
921
922
9.2
921
905
908
9.17
9.1
892
896
8.97
879
886
892
877
868
878
876
896
881
8.8
8.64
8.75
895
897
906
902
891
897
89
891
882
875
868
866
863
894
895
9.08
916
906
8.82
86
87
861
8.48
ppm
2109
1858
1636
1538
1579
1523
1502
1436
1348
1326
1273
1222
1183
1150
1216
1202
1175
1152
1137
1U99
1058
1027
1039
1030
1006
984
973
958
935
919
901
865
868
656
854
856
856
857
851
848
646
840
834
822
809
801
785
766
748
743
740
743
745
749
748
745
750
757
756
740
729
726
729
728
723
720
718
726
726
722
715
711
712
710
tx
255
255
25
25
25
25
245
24.5
25
26
285
27
27
27
264
255
25
25
25
245
245
245
24
24
24
24
245
25
25.5
26
26
26
255
255
25
24.5
24
24
235
235
235
23
23.5
24
24.5
25
255
255
25.5
25
24.5
24
24
235
235
23
23
23
235
24
24.5
245
245
24
235
23.5
23
23
23
235
24
245
245
242
F
482
475
468
463
459
455
451
448
446
444
442
441
439
438
437
436
437
437
437
436
436
437
437
436
437
437
436
437
436
437
436
435
433
429
424
417
411
403
397
391
385
379
374
369
364
360
356
353
350
346
343
341
339
337
334
333
331
330
328
326
325
324
323
323
321
320
319
318
317
317
316
316
315
314
Qpm Bt
84
64
64
64
64
64
64
64
64
64
64
64
64
64
64
6.4
84
84
84
82
82
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
6.2
62
62
62
62
62
62
62
62
62
62
82
62
82
62
8.2
82
62
62
62
62
62
62
62
62
62
62
6.2
62
62
62
62
62
62
62
62
62
62
uflnlerval
4674
4674
4155
3878
4155
4155
4155
415.5
4155
4156
4156
415.6
4678
4678
4878
415.8
4158
4158
4158
4041
4041
4041
4041
4041
4041
404 1
424.4
454.8
404.2
4042
4042
4042
4042
4042
4042
4042
4042
4042
4549
4042
4042
4044
4044
404.4
4044
4044
4551
4551
4551
3774
4044
404.4
404.4
404.5
404.5
404.5
404.5
4045
4045
404.5
4552
4552
404.5
4046
404.6
4046
4046
4046
4046
4046
4046
404.6
3778
404.8
Density of Water meter
Draft cool water readng
OrVOff
Off
Off
Off
Off
Off
Off
on
on
on
on
on
on
on
on
on
on
on
on
on
on
Off
Off
Off
Off
Off
Off
Off
Off
Off
on
on
on
on
Off
Off
Off
Off
Off
on
on
on
on
on
on
on
on
on
on
Off
Off
on
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
on
Off
on
on
on
on
on
on
on
on
on
tVgll
813
813
8.13
813
813
813
813
813
613
813
813
813
813
813
813
813
613
813
8.13
813
813
813
813
813
613
813
814
814
8.14
8.14
8.14
814
814
814
814
8.14
814
814
814
8.14
614
814
814
8.14
814
814
814
814
614
814
814
814
8.14
814
614
614
814
814
814
814
814
8.14
6 14
814
814
814
814
814
814
814
814
814
815
815
cpm
63
63
63
63
63
63
63
63
63
63
63
63
63
63
63
6.3
63
63
63
61
61
61
6.1
61
61
6.1
6.1
6.1
61
61
61
61
61
61
6.1
6.1
6.1
61
61
61
61
6.1
6.1
6.1
61
61
61
61
61
61
81
61
81
81
61
61
61
61
61
61
61
6.1
61
81
6.1
6.1
61
61
6 1
6.1
61
6 1
6.1
61
-------
FURNACE A WITH CATALYST- LOW HEAT REMOVAL RATE
2S-Oct-95 Run TTCO-t
time ambient dluttor; stack stove fire-box watar out w
sec ~
23480
23540
23600
23630
23720
23780
23140
23900
23960
24020
24080
24140
24200
24260
24320
24380
24440
24SOO
24S60
24620
24680
24740
24798
24IS6
24918
14976
25036
25096
251 S6
25218
25278
25338
25398
(.325456
(JfiMS
O025578
25838
25898
2S7S8
25816
2S878
25038
29888
28058
26116
28172
26232
26292
283S2
26412
28472
28532
28592
28852
28712
28772
28832
28892
28952
27012
27072
27132
27102
272S2
27312
27372
2T432
27482
2T548
27«0»
27688
27728
27788
27848
r
86
66
87
87
88
88
88
87
87
87
87
87
87
87
88
88
88
89
89
89
88
87
88
88
88
88
87
87
88
88
88
88
88
88
87
88
68
67
67
67
67
68
88
69
88
89
88
88
87
87
87
87
67
67
68
88
68
68
SB
87
87
87
87
87
87
88
88
88
69
68
68
68
87
S7
t-
72
72
73
73
73
72
71
70
70
70
71
72
72
72
73
73
73
73
72
71
71
70
70
70
71
72
73
73
73
73
73
71
71
70
70
70
71
72
73
73
73
73
74
73
73
74
81
83
64
86
89
92
93
95
97
98
99
99
100
100
101
101
103
104
103
88
81
79
77
76
74
73
73
72
r
89
89
go
90
90
90
89
88
89
89
88
89
90
89
90
90
91
90
90
90
19
89
88
88
88
89
88
80
86
90
90
88
89
BO
89
88
89
90
90
90
91
91
B1
91
90
95
125
148
180
171
17»
188
197
205
212
218
224
230
23S
241
245
248
260
252
2S3
208
170
151
HI
134
129
124
121
117
f-
122
122
122
122
122
122
121
121
121
121
121
121
122
122
122
123
122
122
122
123
122
121
120
121
121
122
121
121
121
121
121
121
121
121
120
120
121
121
122
122
122
123
123
122
122
132
185
208
223
235
247
258
289
277
285
281
298
308
312
318
321
324
328
327
324
286
218
190
178
188
160
155
152
149
I-
473
471
470
470
488
487
4«7
489
489
489
489
489
488
488
463
462
480
458
458
457
457
4S7
458
458
457
458
459
455
454
454
453
454
4S5
455
458
456
458
458
490
480
458
455
4S3
450
448
447
542
873
792
870
927
985
983
978
984
992
1007
1029
1026
1021
1019
1024
1917
1009
1001
948
8S6
788
744
709
884
884
647
8J1
f
171
171
171
171
171
171
170
170
170
170
170
170
170
170
170
170
170
199
189
189
189
169
189
189
189
188
199
188
188
168
188
188
188
188
168
188
187
167
167
167
197
187
187
187
197
197
169
199
188
197
167
168
188
189
170
170
171
172
172
173
174
175
175
178
177
177
177
177
178
178
178
178
178
178
rtarln COH01 CO<*u COkjw
F
183
183
163
183
163
183
193
182
182
182
182
182
162
182
182
162
482
182
162
161
161
161
161
161
181
161
181
161
181
161
161
160
180
180
160
160
160
180
160
160
190
190
180
158
158
156
158
159
159
159
180
180
181
161
162
163
163
164
184
185
199
166
197
198
1M
169
168
170
170
170
170
168
189
170
%
0558
0,573
OS78
0,574
0-58
0558
0,563
0,553
0.551
0-572
0578
0598
0.613
0811
0611
0.807
0.812
0812
0-994
0,601
0593
0.583
0.594
0.809
0.812
0832
0.641
0.851
0.8S
0.644
0657
0.649
0841
0883
0.981
0.981
0984
0999
0.709
0.703
0.983
0.88
0.989
0.988
0.881
0.957
0.892
1.028
1.408
1.3S1
1.187
1.184
1.19
1 108
0923
0.834
0983
0938
0.978
1.034
108
1,106
1.027
o.n
0.944
0.023
1.51
2.418
2-529
2.387
2.187
2.02
1 836
1.651
PP"
103
105
106
104
114
109
112
117
115
112
108
112
115
112
113
110
111
115
117
118
122
124
123
120
120
121
121
122
123
125
132
132
133
135
137
134
128
130
132
133
130
128
128
134
136
265
1507
2008
2008
2007
2007
2007
1885
1545
1555
1717
1938
1658
1858
1888
2007
1839
1747
1646
1943
578
943
992
814
783
687
624
547
488
PUB!
5018
5015
5017
5018
5015
5015
5018
5015
5015
5018
5018
5016
5016
5016
5017
5017
5017
5018
5016
5017
5017
5018
5017
5018
5016
5018
5018
S018
5017
5015
5018
5016
5017
5016
5017
5016
5018
5016
5017
5018
5017
5017
5017
5015
5018
5018
5015
5015
5017
5016
5016
5018
5018
5018
5018
5019
5015
5018
5017
5016
5017
5018
5016
5017
5015
5018
5018
5016
5017
5018
5018
5018
5017
5018
O2
%
11.89
11.92
11,48
11.48
11.67
11.74
11.88
11.91
12.1
11.85
1186
1169
1146
11 48
11.5
11.55
11.48
11,45
11.73
1197
11.87
1204
12.18
12.13
12.2
11.99
11-83
11.88
11.65
11-79
1167
11.66
1204
1188
11 72
1182
1181
11.73
11.58
11.56
11.88
11.79
11.85
11.7
12.03
12-14
12,3
13.48
12.73
11.84
11.48
11.02
10.45
10.22
102
888
875
8.18
8.72
8,75
8.85
896
8.12
8.22
9.49
10.15
10.52
10.08
10.4
1076
11.01
11,04
11-23
11.31
Pr
Water
CO2 JUM-THC Mince catalyst actual How raw neat out
%
8.7S
9
811
811
(.83
888
893
8.7
8.58
878
8.78
886
817
9.14
9.13
909
9.15
9 18
891
8.88
8.78
8.82
849
8J7
8.52
8.75
8.89
803
908
8.93
9.05
887
888
889
9
691
8.85
903
8.17
8.17
806
8.B8
9.07
903
8.88
8.83
8.39
7.43
8.32
621
9.57
9.92
10.38
10.58
10.54
10.68
1088
11.47
11.78
11.73
11.87
11,58
11.48
11.31
11.14
10.41
10.28
10.48
8.98
9.5
8.25
8.24
9.1
9.05
pptn
718
719
718
715
718
724
733
728
718
711
700
688
891
889
688
686
885
681
700
704
685
684
684
683
873
882
681
672
675
671
872
878
880
676
993
986
899
989
964
8S3
859
658
655
655
868
873
675
878
673
665
895
870
855
838
619
589
496
495
492
479
482
489
525
548
542
534
52?
527
531
544
569
584
591
572
t*
24
235
23,5
23
23
235
24
245
24.5
245
24
24
235
235
235
235
23.5
23
23
23
235
24
24
24
23.5
235
23.5
23
23
225
22.5
23
235
24
24
24
235
235
23.5
23
23
225
22.5
22
22.5
23
23.5
24
24
23
225
21.5
21
205
195
18.5
185
19
195
195
19
18.5
18
17
185
15.5
15.5
15.1
15
15.5
16
16.5
185
18.5
F
313
313
312
312
312
311
311
311
311
S11
311
310
310
310
310
310
, • 309
309
308
310
308
308
310
310
310
310
310
310
310
311
311
311
311
311
312
312
313
314
314
314
314
314
315
315
315
318
326
351
383
425
47»
535
591
840
973
899
724
748
765
783
798
808
809
810
808
782
744
715
688
642
839
618
597
577
SP**5 Bt
8.2
8.2
6.2
82
6.2
62
8.2
6.2
8.2
6.2
6.2
8.2
62
6.2
6.2
8.2
8.2
8.2
62
82
9.2
8.2
8.2
6-2
62
62
6.2
82
6.2
8.2
8.2
6.2
62
82
62
62
8.2
6.2
8.2
8,2
8.2
8.2
9.2
92
8.2
9.2
8.2
8.2
6.2
6.2
8,2
8.2
62
82
82
9.2
9.2
92
9.2
9.2
9.2
92
8.2
6.2
8.2
8.2
8.2
6.2
8.2
6.2
8.2
8.2
62
8.2
urintefval
404.8
404.8
4048
404.8
404.8
404.8
3542
404.9
404.8
404.8
4048
4049
4048
404.8
404.8
4049
404.9
354.3
354.3
405.1
405.1
378.1
405.1
405.1
4051
354.4
405.1
3544
354.4
3544
3544
405.2
405.2
405.2
405.2
405.2
3546
3548
3546
3546
3549
3548
3546
405-3
378-3
4053
354.7
354.7
3547
405.3
3546
4052
354.4
4051
4049
3542
4048
4048
4046
404.5
404.4
454.9
4042
404.1
403.9
4039
403.8
329.8
403.8
403.8
4038
454 4
454.4
403.8
Intocfon Q2~Apr-9e
Density of Water meter
Draft cool water read no
On/Off
Off
Off
off
Off
Off
Off
Off
Off
on
otr
on
OR
on
Off
Off
Off
Off
Off
Off
Off
OB
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
t>'ull
8.15
815
815
815
8.15
8.1S
8.19
8.15
815
815
615
815
815
8.15
815
8.15
819
8.15
8.15
1.15
8,15
8-15
8,1»
8.15
8.15
8.1S
8.15
8.15
8.15
8.15
8.15
816
8.18
816
8.16
8.18
8 18
8.18
8.16
818
8 18
816
816
816
8.18
818
8,18
8,18
8 18
6,18
8.19
8.16
8.15
8.15
8.15
8 15
8.15
8.14
8,14
8.14
8 14
8.14
8-14
8.13
8.13
8.13
8,13
8,13
8.13
8 13
8.13
8.13
8 13
8.13
gpm
6,1
81
8,1
6,1
81
8.1
6.1
8.1
6.1
81
61
61
61
61
8.1
6.1
8.1
8.1
91
61
81
81
at
81
8.1
81
61
61
81
8.1
81
81
8.1
81
81
81
8.1
81
8.1
8.1
91
8.1
81
81
61
61
61
81
8.1
81
61
6.1
61
81
61
61
61
6.1
6.1
8.1
81
6.1
81
8.1
8.1
6.1
6 1
61
8.1
81
6.1
8 1
91
61
-------
FURNACE A WITH CATALYST- LOW HEAT RBMOVAL RATE
25-C*t-95 Run TTCO-1
time amUent dlutton stack stove fir*-box water out water In CO Ho/i CO dkj CO low
sec *" " " " ~ ~ ~
27808
27888
28028
28088
28146
28208
28288
28328
28388
28448
28508
28588
28828
28888
28748
28808
28868
28924
28984
29044
29104
29184
29224
29284
29344
29404
29484
29524
29584
29644
29704
29784
O 29824
29884
LA 29944
^530004
30094
30124
30184
30244
30300
30360
30420
30480
30540
30600
30880
30720
30780
30840
30900
30960
31020
31080
31140
31200
31260
31320
31380
31440
31500
31SBO
31620
31678
31738
317B6
31856
31818
31978
32038
32088
32158
32216
32276
r
87
67
67
68
68
68
69
69
69
89
68
88
88
87
87
67
67
88
68
88
68
88
88
67
67
66
88
86
87
67
87
68
68
69
89
69
66
88
68
67
88
88
66
68
67
67
67
68
68
59
69
69
88
69
68
69
68
67
88
66
66
86
66
67
87
67
68
68
68
68
69
69
69
70
r
73
74
75
74
75
75
75
75
74
73
72
71
71
71
72
73
73
74
74
74
73
72
71
71
70
71
72
72
73
73
73
74
74
74
74
73
72
70
70
69
89
71
71
72
73
73
73
73
73
?3
73
73
73
73
71
70
70
89
69
70
71
72
72
72
72
73
73
73
73
73
73
73
73
73
r
115
114
113
112
111
108
106
107
108
104
103
102
101
88
100
100
99
100
99
99
88
87
88
85
94
94
93
93
83
94
84
84
93
84
93
93
83
82
82
80
90
90
80
90
80
80
90
80
90
88
80
81
80
90
89
89
88
87
87
86
87
87
87
87
87
87
88
88
88 '
88
88
88
88
88
r
148
144
142
141
141
138
138
137
138
138
134
133
133
133
132
132
131
131
131
130
128
128
127
128
128
129
128
124
124
122
121
120
120
119
118
118
118
118
117
119
115
114
114
114
114
114
114
114
115
114
114
114
113
114
114
112
112
112
112
112
111
111
111
112
111
112
111
111
111
111
111
111
111
111
r
817
604
992
581
570
561
550
542
535
527
521
515
510
505
500
495
490
485
482
478
474
471
488
486
464
481
457
455
453
450
446
447
445
442
439
437
437
438
436
435
434
433
431
428
426
424
424
423
422
421
420
419
417
416
415
415
415
414
414
414
413
412
410
409
407
406
408
405
404
403
402
402
401
401
f
178
178
178
178
178
178
178
178
178
178
178
178
178
178
177
177
177
177
177
177
177
177
177
178
176
178
178
176
178
178
176
175
175
175
175
175
175
175
175
175
174
174
174
174
174
174
174
174
174
174
174
174
173
173
173
173
173
173
172
173
173
173
172
172
172
172
172
172
172
172
171
171
171
171
p
170
170
170
170
189
170
170
170
170
170
168
188
189
169
169
169
189
169
169
189
188
189
1(8
168
168
168
168
181
188
188
188
188
168
167
1«8
187
167
187
167
187
166
187
186
187
186
186
186
189
188
188
106
188
189
188
165
165
185
166
185
165
165
165
185
165
185
165
165
1*5
164
164
184
164
164
184
%
1.433
1.276
1.157
1.062
0.978
0.912
0.866
0846
0.82S
0804
0.793
0.778
0.783
0.74
0.728
0.731
0.71
0.888
0685
0887
0.883
0.847
0.838
0.618
0.614
0803
0597
0597
D.SS2
0.582
0.574
0.571
0.562
0-557
0.554
0.548
0538
0533
0.526
0532
0.523
0.515
0528
0.529
0.519
0.508
0.504
0.497
0.49
0.492
0.482
0.504
0.497
0.491
0489
0.48
0.478
0481
0.479
0.48
0494
0.48
0.49
0481
0.475
0.478
0.478
0.488
0.484
0.477
0.474
0.469
0.465
0.494"
Pprn
388
351
312
283
259
242
230
223
212
207
202
197
191
178
171
169
184
160
155
154
150
147
145
142
139
133
127
128
123
123
120
117
115
111
112
114
113
114
112
111
108
101
89
87
97
95
86
95
87
84
93
93
81
93
95
84
95
97
82
88
87
86
87
87
88
85
84
83
84
82
84
83
84
83
ppm
5015
5016
5017
5018
5018
sow
5018
5014
5015
5015
5016
5017
5018
5017
5019
5017
5017
5015
5015
5017
5018
5017
5017
5016
5017
5016
5013
5017
5018
5018
5016
5017
5017
5016
5017
5015
5017
5018
5017
5017
5017
5018
5018
501S
SDK
5017
5017
5002
4854
4866
4962
5015
5002
4964
4910
4838
4812
4846
4430
4838
4972
4928
4838
4839
4781
4783
4805
4900
4888
4813
4778
4723
4690
4574
02
%
11.57
1187
11.88
11,74
1191
12,09
12.21
12.12
12.12
1217
12.16
12.19
12.27
12.42
12.43
1226
1235
12,4*
12.43
12.5
12.44
12.51
12.S
12.84
12.67
12.71
12.71
12.61
12.88
1258
12.54
12.51
12.53
12,51
12-46
12.46
12.56
12.83
12.71
1262
12.72
12.78
12.47
12.29
12.37
12.45
12,48
12.52
12.58
12.57
12.54
12.34
12.32
12.39
12.43
12.55
12.88
12.64
12.7
12.72
12.43
12.38
12.27
12.35
12.44
12-4
1235
12.2
12.18
12.28
12.29
1236
12.36
12.58
R
Water
CO2 JUM-THC Mam c«tjly«t actual few rat* heat out
^
883
8.77
8.75
6.7
6.54
8.42
831
8.38
8.38
8.33
8.38
834
8.27
8.1$
8.17
833
8.24
8.13
8.17
8.08
8.14
8.08
8.07
7.92
7.82
789
788
7.97
7.9
8
8.02
8-05
804
807
808
1-09
7.97
7.82
7,16
7.94
7.82
7.81
6.08
8.24
8.16
8.1
8.08
802
797
7.98
7.99
82
8.2
8.15
8.1
798
7.8
7.91
788
7.88
8.13
8.15
8.28
8.17
8.12
8.14
a. 19
834
8.35
8.26
8.23
8.17
814
7.97
com
544
532
531
564
928
1414
1620
1571
1467
1412
1326
1206
1075
1005
840
867
802
772
743
•12
675
657
955
938
624
621
827
619
611
804
613
811
811
811
618
825
597
575
555
552
949
S84
567
568
588
985
S64
S82
583
583
872
570
589
571
566
582
561
556
547
539
542
538
529
525
821
S23
523
523
524
523
518
514
506
508
bs
18
15.5
15
15
15
14.5
14.5
14.5
14.5
15
1S.5
18
16
18
U.6
1S.5
15,4
15
15
14,8
14.5
15
15.5
18
16
16
15.5
15.5
1S.5
15
15
15
19
15
18
14.5
15
IS
15.5
16
16
18
155
199
15.5
15
1$
1$
15
15
15
15
IS
16
15
15
1S.S
18
18
18
1S.5
15.5
15.5
155
15.5
155
1S.S
15.S
19.5
15.5
19
18
18
18
F
559
545
532
519
510
501
493
484
477
472
486
459
453
448
442
436
431
426
421
418
411
407
403
388
394
390
386
382
378
374
370
387
364
361
158
J55
353
350
348
345
343
341
339
338
334
332
330
329
327
328
324
322
321
320
319
318
317
316
315
314
313
312
311
310
309
308
307
307
308
305
30S
304
303
303
gpm &
6.2
6.2
9.2
6.2
82
8.2
6.2
6.2
9.2
6.2
82
82
62
6.2
8.2
6.2
8.2
6.2
6.2
82
82
6.2
8.2
62
62
8.2
62
62
6.2
6.2
62
8.2
6.2
62
62
8.2
62
6.2
62
8.2
82
9.2
6.2
8,2
6.2
8.2
8.2
8.2
6.2
9.2
6.2
62
8.2
62
6.2
9.2
6.2
6.2
6.2
62
6.2
8.2
82
8.2
6.2
82
8.2
8.2
82
6.2
82
62
82
8.2
uHntervat
4038
403.8
403.8
403.8
454.4
403.8
403.8
403.8
403.8
4038
454.4
454.4
4544
454.4
403.9
4039
377.0
403.8
403.9
4039
4039
4039
4548
404.1
404.1
4041
404.1
4041
4041
404.1
404.1
353.8
3538
4042
3538
404.2
4042
404.2
404.2
377.3
404.4
3S3.7
404.4
353.7
4044
4044
4044
404.4
404.4
404.4
4044
4044
353.8
353.8
404.5
404.5
404.5
4045
353.9
404.5
404.5
404.5
3303
353.9
3839
353.9
353.9
353.9
404.6
4046
354.1
354.1
354.1
354.1
interJon 02-A|»-9O
Density oT Water meter
Draft cod water rearing
OnK>B
Off
Off
OB
OB
Off
Off
Off
Off
OB
Off
Off
Off
Off
OB
Off
OB
Off
Off
OB
Off
Off
Off
Off
Off
Off
OB
Off
Off
Off
Off
off
off
Off
Off
Off
Off
Off
Off
Off
Off
OB
OB
Off
Off
Off
Off
OB
Off
Off
Off
Off
Off
off
off
Off
Off
Off
Off
Off
off
Off
Off
OB
OB
OB
Off
OB
OB
Off
OB
Off
Off
Off
Off
fcftttl
813
8.13
813
8.13
813
813
8.13
813
8.13
8.13
813
1.13
813
8.13
8.13
8.13
8.13
813
8.13
813
8.13
813
813
813
813
813
1.13
813
813
8.13
8.13
813
1.13
8.14
813
8.14
8.14
8.14
8.14
8.14
8.14
8.14
8.14
8.14
814
814
8.14
8.14
8.14
a 14
8.14
8.14
8.14
6.14
8,14
S.14
8.14
8.14
6.14
8.14
8.14
8.14
8.14
8.14
8.14
8.14
6.14
8.14
8.14
8.14
814
8.14
814
S.14
cdft
8.1
8.1
8.1
6.1
81
6.1
61
8-1
8.1
8.1
8.1
8.1
8.1
8.1
8.1
9.1
81
8,1
8.1
9.1
8.1
81
61
6.1
61
8.1
8.1
8.1
9,1
6.1
6.1
6.1
6.1
6.1
6.1
9.1
9.1
6.1
81
8.1
61
6.1
6.1
9.1
8.1
91
91
6.1
81
8.1
8.1
8.1
8.1
6.1
81
6.1
8,1
61
6,1
61
6.1
61
61
8.1
9.1
9.1
91
91
81
61
6.1
9.1
91
-------
FURNACE A WITH CATALYST- LOW HEAT REMOVAL RATE
25-Oct-95 Run TTCD-1
time ambient dlution stack stove fire-box water out water in CO Nort CO dkj CO tow
sec -------
32336
32398
32456
32516
32576
32636
32696
32756
32S16
32876
32930
32996
33052
33112
33172
33232
33292
33352
33412
33472
33532
33592
33652
33712
33772
33632
33892
33952
34012
34072
34132
34192
_ 34252
O 34312
O\ 34372
O 34428
34488
34548
34608
34668
34728
34788
34848
34908
34968
35028
35088
35148
35208
35268
35328
35388
35448
35508
35588
35628
35688
35748
35804
35864
35924
35984
36044
36104
36164
36224
36284
36344
36404
36464
36524
36584
36644
36704
f-
70
70
70
70
70
70
71
71
71
71
71
71
71
71
71
71
71
71
71
71
71
71
71
71
72
71
71
71
71
71
71
71
71
71
71
71
71
71
71
71
71
71
72
71
72
73
72
72
71
70
70
69
68
68
87
67
67
87
67
88
68
68
69
68
88
67
66
66
67
66
67
67
68
68
r
73
73
73
73
73
73
73
73
72
73
72
73
73
72
72
72
72
72
72
72
72
72
72
72
71
72
72
71
72
71
71
71
71
71
71
71
71
71
72
72
72
72
73
77
83
84
84
85
65
85
85
85
86
86
87
89
91
92
93
93
94
94
92
91
91
90
90
92
93
94
94
95
95
96
I-
86
88
86
88
88
88
88
88
87
87
88
87
88
88
88
87
67
87
87
87
87
87
87
86
86
86
86
86
86
87
86
88
86
86
85
88
86
86
66
86
88
88
86
101
132
147
155
161
168
170
175
178
183
186
189
193
196
199
201
202
204
205
204
205
204
205
205
206
208
209
209
210
210
211
t-
111
111
111
110
110
111
111
110
110
110
110
110
110
110
110
110
110
109
109
109
109
109
109
109
108
109
110
109
109
109
108
109
109
109
109
109
108
108
106
108
109
109
109
141
185
200
208
215
221
226
231
236
240
243
248
249
251
253
254
255
256
258
256
257
258
257
257
258
259
259
259
259
259
280
i-
400
399
399
398
398
397
396
398
395
394
394
393
393
393
393
392
392
391
391
390
388
385
384
383
382
382
382
381
381
381
380
380
380
379
379
379
379
379
378
378
378
377
376
362
381
466
534
584
615
847
870
682
890
696
700
701
704
686
873
670
669
666
666
689
679
681
678
687
693
675
668
688
669
669
F
171
171
171
171
171
170
170
170
170
170
170
170
170
170
170
189
169
189
188
169
188
168
188
168
188
188
188
188
188
188
188
168
188
187
167
167
167
167
167
167
167
167
166
166
186
166
166
166
166
186
166
167
167
168
168
188
168
168
188
168
168
188
170
170
170
170
171
171
171
171
171
171
172
172
F
164
183
163
163
183
163
183
163
163
183
183
162
182
182
162
161
162
162
161
161
181
161
161
181
181
161
161
160
160
180
160
160
180
160
158
158
159
159
158
159
158
158
159
158
158
158
158
158
158
158
158
158
158
158
160
180
161
161
161
161
161
161
161
161
182
162
162
183
163
183
163
163
163
164
%
0.455
0456
0462
0464
0.481
0464
0486
0459
0.458
0456
0.46
0457
0454
0455
0461
0453
0.454
0455
0457
0459
0453
0.453
0.452
0455
0.456
0455
0458
0458
0469
0472
0.475
0463
0468
0.464
0458
0.462
0465
0.453
0.48
0.464
0.483
0456
0.463
0.462
0.472
0.671
0821
0822
0969
0.941
0888
0832
0806
0.751
0.69
0637
0602
0578
0.586
0.605
0613
0.602
0.585
0573
0572
0568
0558
0.541
0.55
0547
0569
0577
0576
0.57
ppn
82
83
81
83
80
80
79
80
79
79
79
80
80
78
79
77
78
77
78
78
78
77
79
80
80
80
82
81
61
81
79
80
78
80
78
79
79
78
77
74
78
71
70
392
888
1348
1553
1660
1628
1526
1407
1373
1280
1189
1081
1028
871
889
1022
1035
1025
881
873
978
886
854
822
926
917
852
870
975
967
945
ppm
4583
4589
4663
4683
4643
4683
4676
4840
4622
4599
4838
4601
4577
4576
4644
4580
4584
4587
4591
4612
4560
4560
4581
4581
4588
4587
4604
4807
4722
4747
4785
4887
4705
4673
4820
4655
4691
4581
4838
4665
4664
4585
4878
4654
4896
5016
5016
5016
5015
5018
5017
5017
5017
5018
5017
5016
5016
5018
5016
5018
5018
5015
5018
5018
5016
5018
5018
5015
5017
5018
5018
5016
5016
5017
02
%
1256
1258
12.41
1237
1242
1235
1234
12.45
1248
1254
1245
1249
1253
1253
12.4
1252
1256
12.46
12.48
1243
1253
1254
1258
1266
1279
12.84
1289
1289
1273
1265
1257
1274
12.68
12.72
1281
1274
1282
12.83
1276
1287
1262
1272
125
1245
1391
1585
1557
153
151
15.06
14.89
14.72
1465
1458
1453
1455
1449
14.48
1462
1472
14.75
14.8
1486
149
1469
1487
14.9
14.91
1482
1485
149
14.91
1494
1496
Water
CO2 JUM-THC balance catilyM actual flow rate neat out
%
797
798
811
817
611
819
818
808
804
8
808
803
799
8
812
a
797
8.06
8.07
808
8
799
794
786
776
7.71
768
788
783
79
799
7.81
7.9
783
7.75
782
792
772
783
78
7.94
787
608
8.1
658
5.13
551
568
581
578
585
6.1
6.13
622
624
621
628
628
613
6.04
6
597
5.68
586
588
5.92
591
5.91
6
597
568
589
587
584
ppm
504
501
493
494
467
464
479
477
475
470
462
461
458
452
451
445
443
441
435
436
439
442
444
443
443
440
437
438
443
452
458
458
464
467
467
468
466
470
472
475
490
503
517
525
542
556
498
441
444
445
441
438
443
437
431
429
422
413
404
401
387
378
367
363
354
350
354
356
358
354
351
349
352
345
IDS
16
16
16
16
16
16
16
16
161
165
165
165
165
165
16.5
165
165
165
165
165
165
185
165
165
185
185
165
165
17
17
17
17
17
17
175
175
17.5
175
175
175
165
16
155
155
15
14
135
135
135
14
14
14.5
145
14.5
15
15
155
155
155
155
15
14
135
135
135
14
14
14.5
15
15
15
148
15
145
F
302
302
301
301
300
300
299
299
298
286
297
297
286
288
285
295
204
294
283
283
283
282
282
291
291
280
280
289
288
288
289
268
269
288
287
287
287
286
286
288
286
285
285
284
289
304
322
342
381
383
407
427
444
461
473
481
489
488
504
508
510
511
512
513
514
511
509
509
510
510
511
512
513
513
gpm Bt
62
82
62
82
6.2
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
82
82
62
62
62
62
62
62
62
62
82
82
82
6.2
62
62
62
82
6.2
62
82
6.2
62
62
62
82
62
62
82
6.2
62
6.2
6.2
62
6.2
6.2
82
82
62
62
62
62
62
62
62
62
62
u/tnterval
3541
4048
4048
404.8
4048
3542
3542
3542
3542
3542
3542
3779
4049
4049
4049
4051
3543
354.3
4051
405.1
405.1
4051
4051
4051
3544
3544
3544
4052
4052
4052
4052
4052
4052
3546
3783
4053
4053
4053
4053
4053
4053
4053
3547
3547
3547
3547
3547
3547
3547
3547
354.7
405.3
4053
4560
4052
4052
3544
3308
4051
4051
4051
4051
4557
4557
4049
4049
455.5
404.8
4048
4048
4048
4048
4554
4048
Density of Water meter
Draft cool water readng
On/Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
on
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
IVgil
814
615
815
8.15
615
615
615
815
615
815
615
815
815
815
815
815
815
615
815
8.15
815
615
615
815
815
615
815
816
816
816
816
816
816
816
816
8.16
816
816
8 16
818
816
8 18
816
816
816
8.18
8.16
816
8.16
8.16
8 18
818
816
8.16
816
8 16
815
8.15
815
8.15
815
815
815
615
8.15
8.15
815
8 15
815
815
815
815
815
8.14
oxn
61
61
61
61
6.1
61
6.1
81
61
61
61
6.1
8.1
8.1
81
61
8.1
81
81
61
61
81
61
61
81
61
61
81
6 1
61
81
81
61
61
61
81
61
61
81
81
61
61
61
6.1
81
61
61
61
61
6.1
81
61
8.1
61
61
61
61
6.1
81
81
61
6.1
6.1
61
81
81
61
61
61
61
61
8.1
81
61
-------
FURNACE A WITH CATALYST- LOW HEAT REMOVAL RATE
Printed on 02-Apr-96
25-Oct-95 RunTTCD-1
time ambient dlution stack
36764
36824
36884
36844
37004
37064
37124
37180
37240
37300
37360
37420
37480
37540
37600
37660
37720
37780
37640
37900
37960
38020
38080
38140
38200
38260
38320
38380
38440
38500
38556
38616
. .36676
O38736
ON38786
I— '38856
38918
38976
39038
38086
38156
39216
39278
39336
39396
39456
39518
39576
39636
39696
39756
39816
39876
39932
39892
40052
40112
40172
40232
40282
40352
40412
40472
40532
40582
40652
40712
40772
40832
40882
40952
41012
41072
41132
69
69
70
69
ee
69
68
67
67
67
67
67
68
68
68
69
70
70
70
69
69
68
67
67
66
67
67
67
68
88
68
68
69
69
70
70
70
70
69
68
67
66
66
66
66
66
67
67
67
67
68
88
68
68
68
68
70
70
70
70
70
70
71
71
71
71
70
70
70
70
69
69
68
69
86
86
88
84
83
92
91
91
92
93
94
95
95
95
96
96
96
96
95
93
80
73
71
71
72
73
73
73
73
73
73
74
74
74
74
73
72
70
69
88
67
68
68
70
71
71
71
71
72
72
72
72
72
72
72
72
72
72
72
72
72
72
72
71
71
70
70
68
69
69
68
68
68
69
211
212
211
211
209
209
208
207
207
208
208
210
210
210
211
211
211
211
210
209
184
154
138
128
121
117
114
111
108
107
105
103
102
101
100
100
88
98
95
94
93
81
90
90
90
88
89
89
89
90
90
90
90
90
90
90
90
90
90
90
90
90
90
90
90
89
89
89
89
88
87
87
67
87
stove fire-box water out water In CO Noji CO dlu
260
260
260
260
260
260
259
258
258
257
258
258
258
258
258
259
259
259
258
258
227
190
168
158
150
146
142
139
136
135
134
132
131
130
129
127
124
123
122
121
118
116
115
115
115
114
115
115
115
115
116
116
116
115
115
114
114
114
115
116
115
115
114
113
113
113
112
112
111
111
111
111
111
111
667
663
661
658
657
654
653
655
659
661
862
661
657
660
668
669
671
675
672
672
687
634
602
577
557
540
527
515
504
494
487
478
472
465
459
453
448
443
439
435
431
428
425
421
417
413
408
405
402
398
396
393
390
387
365
382
360
377
375
373
372
370
368
386
365
364
363
362
361
360
359
358
357
356
172
172
173
173
173
173
173
173
174
174
174
174
175
175
175
175
175
175
176
176
176
176
176
176
176
176
176
176
176
176
176
176
178
176
176
178
176
176
176
176
176
176
176
176
175
175
175
175
175
175
175
174
174
174
174
174
174
174
174
173
173
173
173
173
173
173
173
173
172
172
172
172
171
172
r
164
164
164
164
165
165
165
165
165
166
166
166
167
166
168
167
167
167
167
187
187
187
168
168
168
167
166
168
168
168
168
166
188
188
187
167
167
167
167
167
167
167
167
167
167
167
166
166
166
166
166
166
166
165
166
166
165
165
185
185
165
165
165
164
164
164
164
164
163
163
163
163
163
163
T»
0562
0554
0552
0532
0532
0533
0.54
0549
0.551
0554
0.549
0545
0552
0562
0563
0571
0574
0566
0.58
0583
0577
0526
0631
0982
0917
0824
0.72
0643
0.576
053
0.49
0.456
0.428
0.408
0.39
0379
0376
0372
0361
0.36
0356
0.356
0347
0344
0349
0343
0342
0.337
033
0331
0328
0324
0324
0317
0.321
0.32
0318
0315
0.314
0311
0.313
0315
0316
0317
0.315
0312
0.312
0315
0318
0315
0312
0.315
0.313
0316
ppm
942
933
909
687
906
911
833
827
941
928
918
918
956
940
968
961
980
1001
1004
1003
428
214
320
292
253
212
177
153
135
120
109
100
93
86
84
81
81
80
80
80
79
76
72
70
68
66
65
64
84
63
63
63
63
61
63
81
61
61
61
60
61
59
62
63
64
63
63
83
63
82
62
82
61
62
CO low
ppm
5017
5018
5018
5015
5018
5017
5016
5017
5018
5017
5015
5018
5015
5018
5015
5016
5015
5018
5017
5015
5016
4956
5016
5015
5017
5018
5016
5017
5018
5016
4928
4570
4303
4104
3910
3802
3781
3734
3602
3599
3545
3569
3462
3438
3481
3420
3412
3371
3293
3303
3263
3230
3229
3169
3209
3190
3162
3131
3128
3110
3122
3141
3158
3159
3147
3114
3112
3141
3180
3136
3102
3146
3114
3143
O2
15.03
1509
15.13
15.16
1519
15.23
1524
1526
1531
1527
1526
1527
1532
1532
1531
15.27
1524
1523
1522
1524
1538
15.99
14.07
13.3
1337
13.32
13.39
1338
134
1333
1334
1342
13.44
134
1346
1345
1333
1326
1347
1347
1359
13.55
1375
13.73
13.54
1357
1351
1348
1356
1353
136
1368
13.71
1382
13.75
13.75
13.83
139
1392
1398
1397
1398
1396
1399
1403
1414
14.2
1419
14.18
1426
1433
14,21
14.27
14.2
Water
CO2 JUM-THC balance catalyst actual (low rate heat out
576
572
568
565
5.61
5.57
5.57
555
553
554
556
554
551
55
55
554
558
558
558
555
536
486
652
69
6.71
669
657
657
654
661
661
655
656
661
659
661
8.76
68
666
674
667
672
658
683
662
679
688
6.9
682
887
6.79
6.74
6.72
662
6.7
6.87
6.6
655
653
8.48
6.5
6.51
6.5
648
645
834
632
6.33
637
626
623
8.35
63
6.37
341
340
339
338
341
346
342
335
323
315
313
310
304
305
301
300
300
297
299
303
302
303
288
304
304
303
308
322
331
325
313
408
520
506
466
415
375
348
320
302
288
279
266
258
251
245
241
237
236
235
235
236
243
247
251
253
255
262
265
272
281
291
293
294
294
297
301
302
305
309
313
315
322
325
fcs
145
14
13
125
125
125
125
125
13
13.5
13.5
135
14
13.5
135
135
135
125
11.5
11.5
11.5
11.5
11.5
12
12
125
125
125
13
13
13
13
13
13
13
13
12.5
12.5
12.5
13
13
13.5
14
14.5
145
14.5
14.5
14.5
15
145
14,5
14.5
14.5
14.5
14.5
14.5
14.5
14.5
145
145
145
145
145
15
15
15
15
15
145
145
14.5
14.5
14.5
145
F
515
516
515
515
513
511
508
506
504
503
501
500
499
499
498
497
496
495
494
493
491
479
487
455
446
437
430
424
419
415
410
406
402
397
393
388
384
378
375
371
366
382
356
354
348
345
342
338
335
332
329
327
324
322
319
317
315
313
310
308
306
305
303
302
300
299
297
296
294
293
292
291
289
288
flpm Btu/Interval
6.2 4048
62 4046
6.2 4552
62 4552
62 4045
6.2 4045
6.2
62
62
62
62
62
6.2
6.2
62
62
62
62
62
62
62
82
62
62
6.2
82
82
62
62
62
62
62
62
62
62
6.2
6.2
62
62
6.2
62
6.2
6.2
62
82
62
62
62
62
6.2
6.2
62
62
62
62
62
6.2
62
62
62
8.2
62
62
62
62
6.2
6.2
6.2
62
62
6.2
62
62
6.2
377.5
404.5
455.1
404.4
4044
4044
404 2
454.9
4549
404.2
4042
4042
4548
4548
4548
4548
404.1
4041
4041
4548
4041
4041
404 1
377.1
404 1
404 1
404 1
404.1
4548
4548
4548
4548
4548
4548
4548
4548
4548
4548
404.2
4042
4549
4549
4549
4549
4549
404.4
3774
4551
4044
4044
4551
4551
4551
4045
404.5
404.5
4045
4552
4552
455.2
4552
4552
4554
4554
455.4
455.4
4048
455.4
Density of Water meter
Draft coot water readng
On/Off
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
tVgal
814
814
614
8 14
814
8.14
814
814
8.14
8.14
814
6 14
6.14
6 14
8.14
8.14
814
814
6.14
6.14
814
8.14
8.13
813
8.13
8.14
813
8.13
8.13
813
8.13
813
813
813
8.14
814
8 14
8.14
814
814
8.14
814
814
8.14
8.14
8.14
8.14
814
6.14
8.14
814
8.14
8.14
8.14
814
8.14
8.14
814
8.14
814
814
814
614
814
814
814
8.14
8.14
815
8 15
815
815
815
815
6.1
6.1
81
6.1
61
6.1
6.1
61
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
61
6.1
61
8.1
6.1
61
6 1
6.1
61
6.1
8.1
61
61
6.1
61
6.1
6.1
6.1
6.1
81
6.1
6.1
6.1
8.1
6.1
6.1
8.1
61
6.1
61
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
61
61
6.1
6.1
6.1
8.1
61
6.1
6.1
6.1
6.1
6.1
61
6 1
6.1
-------
FURNACE A WITH CATALYST- LOW HEAT REMOVAL RATE
25-OO-85 RunTTCCM
tirnt inaaanl dButior, stack ttovi Urt-bw r
C02 JUMTHC bahre* only* actual How rate twit out
842
835
637
638
6.54
8.48
8.36
8.37
837
8.39
6.38
6.37
8.38
84
8,31
8.34
643
8.47
848
8.44
838
838
8.48
6.4
6.41
8.35
832
6.34
633
836
638
8.44
655
6.6
651
3.85
3.14
3.26
3.48
3.61
3.67
3.72
382
381
3.87
4.05
413
416
4.17
4.15
4.15
4.11
4.08
408
4.07
4.1
4.14
4.15
418
4.14
4.15
411
4.08
399
398
3.81
3.88
3.86
3.13
3.8
3.77
376
3.74
368
331
335
340
341
348
351
359
385
372
378
385
382
403
414
423
438
457
473
488
502
521
545
585
648
715
750
787
837
881
881
884
881
865
346
817
717
778
780
738
708
667
627
585
563
522
485
481
484
452
435
423
413
399
391
383
376
383
355
347
340
335
331
328
314
311
308
301
295
292
261
283
251
258
257
14.5
145
145
18.7
15
15
15
18
15
15
15
15
15
15
15
15
15
15
15
15
IS
IS
15
14.5
15
15
IS
15
15
IS
15
15
15
15.1
16
18
16
16
15.5
15.5
18.5
15.S
155
15.S
15.5
15.8
15.5
15.5
15
15
15
14.5
14.5
145
145
145
14,5
14
14
14
14
14
14
14
14
14
14
14
14
14
14
14
14
14
f
287
288
285
284
283
282
281
280
279
278
277
276
275
274
273
272
271
271
270
269
288
288
288
287
288
286
265
284
264
264
263
263
262
262
256
257
282
269
275
280
284
288
285
302
309
317
325
332
338
343
348
353
358
361
364
387
388
372
374
376
377
378
379
379
378
378
377
376
374
373
372
371
370
368
6.2
6.2
6.2
6.2
8.2
6.2
8.2
8.2
62
6.2
62
6.2
8.2
6.2
8.2
6.2
6.2
6.2
6,2
6.2
6,2
82
62
8.2
62
82
6.2
62
6.2
6.2
62
6.2
6.2
62
62
62
6.2
6.2
6.2
6.2
8.2
82
9.2
8.2
8.2
8.2
62
6.2
8.2
8.2
9.2
9.2
62
9.2
6.2
6,2
6,2
62
8,2
8.2
8.2
8.2
6.2
62
6.2
6.2
62
6.2
62
62
62
62
82
6.2
u^Mfffval
404.8
377.8
404.8
455.5
455.5
4555
45S.5
404 9
404.9
404.9
4049
4049
455.7
405.1
405.1
405.1
4051
4051
455.8
455.8
405.2
405.2
405.2
4052
4256
453.0
4560
4053
405.3
456.2
4053
458.2
453,2
458.2
405.5
405.5
405,5
405-5
458.3
456.3
4055
4S8.3
456,3
456.3
456.3
458.3
458.3
378.4
405.5
405.5
405.5
405.5
405.5
456.2
458.2
4582
458.2
456.2
4053
405.3
4053
4053
405.3
405.3
40S.3
458.0
456.0
456.0
4560
4560
425.6
4560
4560
456.0
Inted on 02-Apr 96
Density of Witar meter
Draft cod Wller ntadng
On/Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
on
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
8.15
8.15
8-15
8.15
815
8.15
8 15
8 15
8.15
8.15
1.15
8 15
8.15
8.15
8.15
8.15
815
815
818
616
8.18
818
8.16
8.16
8.16
8.16
8.16
816
6.18
8.16
8.18
816
816
8.16
818
816
8 18
816
8 18
816
6.18
8.18
8.18
8.13
8.18
616
818
118
616
816
8 18
818
8 16
818
818
818
116
116
818
8.16
1.18
8.18
6.18
8,18
8.16
8.16
8-16
8-18
819
8.18
8 18
8.19
8.16
1.16
8.1
61
8.1
8,1
61
8.1
81
61
6.1
61
6.1
61
3,1
61
8,1
6,1
6,1
8,1
6.1
6.1
8-1
6.1
8.1
6.1
61
61
6,1
61
61
61
6.1
8.1
8.1
61
61
61
6.1
81
61
6.1
81
6.1
8.1
8.1
81
81
61
81
8 1
61
8 1
61
61
61
6,1
81
8,1
6,1
9,1
6,1
81
61
61
61
8-1
8,1
8-1
8-1
8.1
61
81
81
81
8.1
-------
FURNACE A WITH CATALYST- LOW HEAT REMOVAL RATE
Printed on 02-Apr-86
25-Oc(-9S Run TTCO-1
Urnffi ambient dkjtion stick
see "
4SB18
4S678
48736
48798
468S8
48819
4SB7B
46038
48089
43156
48218
46276
48338
48398
48456
46518
46576
48639
46686
46758
48812
40872
46932
46962
47052
47112
47172
47232
4729S
47352
47412
47472
d7S32
7582
O*7852
U»7712
47772
47832
47882
47852
48012
41072
48132
481B8
4(248
48308
48368
48428
48499
48548
41608
48688
48728
487B8
48848
4BBOB
4S968
49028
4008ft
49148
49208
49288
40328
4838$
49448
48506
49584
49624
49884
48744
49804
40884
49924
49884
r
65
65
85
66
es
88
«s
85
65
85
65
65
65
65
65
65
65
65
85
85
65
85
65
64
85
64
84
84
64
84
64
64
84
64
84
84
64
64
64
64
84
64
64
84
84
84
84
84
84
84
64
64
64
63
84
84
63
64
«3
84
B4
63
83
83
83
83
63
64
63
84
64
64
64
65
t-
84
85
as
85
84
84
84
84
84
84
84
84
84
84
84
84
83
84
83
83
83
83
83
83
53
83
83
83
83
83
83
83
83
83
83
83
83
83
82
82
82
82
82
82
81
81
81
81
81
81
81
81
81
81
81
80
80
80
80
SO
80
80
80
80
81
82
$1
80
81
81
81
81
81
81
t-
181
180
180
179
179
179
178
178
178
177
177
176
178
178
178
175
175
175
175
174
174
174
174
174
174
173
173
173
17S
173
173
173
172
172
172
171
171
171
171
170
170
170
169
168
187
167
187
188
189
185
16S
164
184
164
183
183
163
162
161
161
181
180
160
160
161
161
182
181
182
182
161
1«1
162
161
stove fi
F
221
221
220
218
219
218
218
218
217
216
216
215
215
214
214
214
214
213
213
212
212
212
212
212
212
212
212
211
211
211
211
211
210
210
210
209
209
208
207
207
206
205
20S
204
203
203
202
202
201
200
200
199
199
198
198
187
197
188
195
195
184
184
1M
193
184
194
194
1S3
184
193
193
193
183
183
re-box water out water In CO Ntfi CO dfu CO low
f
488
485
482
482
480
478
478
471
488
482
457
454
452
448
448
448
447
445
443
441
441
444
445
444
443
442
441
440
440
438
438
436
433
431
431
428
427
422
418
415
412
408
406
403
403
401
401
401
400
398
400
400
388
397
395
382
390
388
386
384
383
382
380
372
357
356
3S?
358
358
383
364
364
360
354
F
188
188
188
168
168
168
168
188
168
168
168
168
168
168
168
168
168
188
168
168
168
168
168
168
188
188
168
188
168
169
188
168
189
188
189
168
169
188
188
136
169
169
188
188
188
198
169
169
188
169
198
198
168
169
168
168
168
168
168
168
189
168
168
198
168
168
188
188
198
198
168
168
168
188
F
159
160
180
1S9
159
159
180
159
190
160
159
180
159
159
160
160
160
160
160
160
160
160
160
160
160
160
160
180
160
160
180
180
161
181
160
160
180
180
160
180
160
161
180
180
190
180
161
161
181
181
191
161
160
191
ISO
181
160
160
160
1*0
180
160
160
160
160
160
180
190
161
161
161
181
16t
1«1
%
0391
0386
D.383
0.376
0.373
0.369
0364
0358
0.349
0.344
0.338
0.334
0.335
0333
0.334
0.335
0.334
0.337
0.342
0.342
0.342
0.345
0.352
0.3S8
0.382
0.346
0.338
0.333
0.333
0.333
0.33
0.326
0.32
0.321
0.32
0.313
0.313
0.304
0.288
0.282
0287
0.27B
0.275
0.27
0.2M
0.2T9
0.287
0.288
0.285
0283
0.289
0.284
0.282
0.288
0.285
0.277
0-272
0.288
0.268
0.27
0.271
0.27
0.272
0.273
0282
O.S14
0.33
0.336
0.338
0,333
OS31
0328
032S
0 332
pptn
837
83«
828
814
808
809
592
S78
585
559
549
551
547
544
547
546
544
557
558
554
sei
566
589
578
588
558
543
541
541
537
534
521
517
521
510
506
495
482
469
490
446
440
433
427
439
457
458
454
449
4S4
471
494
455
459
449
432
426
427
427
428
430
428
434
445
538
881
594
597
594
569
580
580
549
903
ppm
3895
3844
3822
3747
3703
3672
3921
3556
3488
3413
3358
3334
3337
3310
3313
3321
3317
3343
3386
3398
3405
3437
3487
3563
3*01
3438
3353
3309
3285
3290
3267
3228
3171
3174
3165
3101
3083
3008
2933
2870
2821
2747
2705
2860
2940
2740
2828
2820
2789
2790
2836
2898
2861
2837
2792
2736
2672
2632
2842
2846
2657
2961
2675
2676
2761
3079
3247
3322
3329
3277
3281
3237
3221
3285
O2
%
17,27
17.28
17.32
17,37
17.39
17.4
17,42
1745
17.S2
17.54
1758
17,61
17.63
17.84
17,65
17,84
17.66
1766
17.65
17.96
17.86
17.64
17.85
17-88
17.7
17.7
1771
17,71
17.74
17.78
17.78
17.77
17.8
17.84
17.87
179
17.91
17,86
18.03
18.07
18.09
18.13
1117
18,21
1824
1828
18.24
18.28
1*27
1828
18.28
18.28
18.3
18,34
18,37
1841
18.45
18,5
1849
1151
18,83
1859
18,57
18.6
1883
18,83
18.58
18.57
11.58
18.58
18.54
18.53
1853
18.58
CO2 JW-THC balance c
%
3.84
3,81
3.58
3.56
3.S8
3.S4
3.51
3.48
3,44
341
3,37
3.S5
3.34
3.31
331
3.31
3.28
3.3
3.3
3.28
3.29
3.31
3.3
3.28
3.28
3.26
3,28
3-25
3.22
3.21
3.19
3.18
3.15
3.12
3.08
3.05
3,08
2,99
2.85
2.9
2 as
284
2.81
2.78
2.75
2.73
2.74
2.71
2.7
2.68
288
268
2.68
2.83
2.81
2.57
2.52
2,5
2.48
2.47
2.4S
2.42
241
2.38
2.34
2.35
2.38
2.4
2.38
2.39
2.43
2.43
2.42
2.38
pjxn
280
243
237
234
230
222
219
217
214
213
207
207
208
203
200
198
187
187
184
183
184
181
189
190
188
189
180
189
1KB
181
180
188
188
186
187
188
186
18S
187
187
189
188
185
182
181
177
179
175
177
176
17?
181
180
179
177
177
173
177
177
175
172
172
173
170
168
1SS
168
188
188
173
177
183
189
198
IDS
135
138
13.5
14
14
14
14
13.5
13.5
135
135
13.5
13.5
135
13.5
13
13
13.2
13
13.4
13
13
13
13
13
13
13
13
13
13
13
125
13
125
125
12.5
12.5
12.5
12.5
12.5
12.5
12.5
125
125
12.5
12
12.9
12.5
12
12
12
12
12
12
12
12.5
122
125
12.5
12.5
12.5
12.5
12
12.5
12.5
12.5
12.1
12
11.5
10.5
10
95
9
9
Water
alalyst actual flow rale heat out
F
367
365
384
383
361
360
358
357
355
354
352
350
348
348
347
345
344
343
342
342
341
341
340
340
338
339
338
337
336
335
335
334
333
332
331
331
330
329
327
325
323
321
310
317
315
314
312
110
309
30?
306
304
303
302
300
288
297
296
294
292
291
288
268
286
284
283
283
282
282
281
281
281
280
278
9pm Btufinterval
62 4560
62
8.2
8.2
6.2
62
8.2
8.2
8.2
6.:
6.2
6.2
8.2
8.2
6.2
6.2
6.2
6.2
9.2
9.2
82
6,2
62
82
9.2
9.2
8.2
8.2
8.2
82
9.2
8.2
6.2
8,2
8.2
6.2
6.2
6.2
8.2
8.2
6.2
6,2
6.2
6.2
6.2
6.2
*.2
«.2
6.2
6.2
62
62
8.2
8.2
62
62
8.2
62
8.2
6.2
6.2
62
6.2
8.2
62
6.2
6.2
6.2
62
6.2
6.2
6.2
8.2
6.2
405.2
4052
458.0
459.0
459.0
4052
4560
4580
4052
456.0
405.2
458.0
456.0
405.2
4052
4052
405.2
4052
3782
4052
405.2
405.2
405.2
409.2
4082
4052
4052
405.2
405.2
405.2
405.2
405.1
3544
4559
4052
455.8
4052
405.2
4559
4559
405.1
378.2
4052
455.9
455.9
405.1
405.1
4051
405.1
405.1
405.1
4SS.9
4051
405.2
3544
4052
4052
4052
405.2
4559
405.2
405.2
405.2
4052
3782
4052
4052
3544
354.4
3544
3544
354.4
3544
Otalt
OnfOff
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
Density of Water meter
cool water reatina
(Kgal
8.18
8.16
8.16
8.16
8.18
5.18
a ia
8.18
8.18
8.16
816
8.16
8.18
8.18
8.16
8 16
8.16
8.18
816
8.16
8 16
818
8.16
8.16
8.16
8.16
816
816
8.16
8.16
8.16
816
8,15
6.15
8.19
8.18
816
618
818
8.16
8.16
8.15
816
816
816
816
8.1S
8.1»
8.15
8.1S
8.15
8.15
8.18
8.15
816
818
816
816
8,18
8,16
8.18
6.16
8.16
816
8.16
8.16
116
616
815
8,15
815
815
818
8 15
8.1
8.1
9.1
6-1
8.1
81
8.1
91
6.1
6.1
8.1
8.1
81
8.1
6.1
61
8.1
61
6.1
8.1
8.1
8,1
6.1
8.1
8.1
6.1
8.1
8-1
6-1
6-1
6.1
6.1
6.1
8.1
61
61
8.1
8.1
6.1
6.1
8.1
8.1
8.1
9.1
81
8.1
81
81
8,1
61
61
6.1
81
81
6.1
6.1
8.1
61
8.1
8.1
61
61
61
6.1
6.1
6.1
8.1
6.1
6.1
6.1
6.1
81
6.1
6.1
-------
FURNACE A WITH CATALYST- LOW HEAT REMOVAL RATE
Printed on 02-Apr-M
25-OCI-95 Run TTCD-1
time ambient dlution slack stove tlre-box water out water In CO Noh CO dlu CO tow
SBC prccrrr-.--.
50044
50104
50164
50224
50284
50344
50404
50464
50524
50584
50644
50704
50764
50824
50884
50940
51000
51060
51120
51180
51240
51300
51360
51420
51480
51540
51800
51660
51720
51780
51840
51900
.51960
^52020
(^52080
^.52140
52200
52260
52316
52376
52436
52496
52556
52616
52676
52738
52796
52856
52916
52976
53036
53096
53156
53216
53276
53338
53398
53456
53516
53578
53838
53692
53752
53812
53872
53932
53992
54052
54112
54172
54232
54292
AVERAGE
1346111 hrsruntii
65
65
68
66
67
67
67
87
68
68
68
68
69
69
69
69
69
70
70
70
70
70
70
70
70
71
71
71
71
71
71
70
89
88
67
66
66
86
66
67
67
67
67
68
88
88
69
69
89
70
70
70
69
68
68
67
67
66
66
65
65
64
64
64
64
64
64
65
65
66
66
68
ne
82
81
82
82
82
82
82
82
82
82
82
82
82
82
82
83
83
82
82
82
82
82
82
82
82
82
82
83
82
82
80
79
78
77
77
78
78
79
79
80
80
80
80
80
80
81
81
81
81
81
81
79
78
77
78
78
76
76
76
75
75
75
75
76
77
78
78
79
79
80
80
78
161
161
161
161
160
180
160
159
159
159
158
158
158
158
158
157
157
157
156
156
156
156
155
155
155
155
154
154
154
153
153
152
151
150
150
149
149
149
149
149
149
149
148
148
148
148
148
148
148
148
148
148
147
148
145
145
144
144
143
143
142
142
142
142
142
142
142
142
142
142
142
132
193
193
192
192
192
192
191
190
190
190
189
189
189
168
188
187
186
186
186
185
185
185
184
184
183
183
183
182
182
182
181
180
179
179
178
178
177
177
177
177
177
176
176
178
178
176
176
176
175
175
175
175
174
173
172
172
172
171
171
170
170
189
169
169
169
169
169
168
168
169
168
165
350
348
347
348
347
346
342
336
335
332
330
327
325
323
320
316
314
311
309
306
304
303
302
301
287
296
297
296
295
293
289
288
287
285
284
283
284
283
282
282
280
278
277
278
278
276
276
274
272
271
289
266
284
284
283
261
260
257
255
254
251
250
249
250
249
248
248
247
246
246
246
517
168
188
168
188
168
168
168
168
168
168
166
168
188
168
168
188
187
188
168
168
167
167
167
167
167
167
167
167
167
167
187
167
167
187
186
188
167
166
186
166
166
166
166
166
166
166
166
166
166
168
166
168
188
185
168
185
165
165
185
165
185
185
165
185
165
164
164
164
164
164
164
171
r
181
161
161
161
161
161
161
161
161
161
161
181
161
161
161
161
181
161
161
181
161
161
161
161
181
161
161
161
181
161
160
160
160
160
160
160
180
160
160
180
160
160
160
160
160
160
160
180
160
160
180
159
159
159
158
158
158
158
158
158
158
158
158
158
158
158
158
158
158
158
158
163
•*
0347
0.338
0325
0317
0305
0.295
0.29
0284
0274
0.264
0.26
0258
0254
0.248
0.243
0.239
0234
0233
0231
0.228
0.228
0225
0215
0.211
0.207
0204
0.21
0208
0203
0.196
0.195
0.194
0.195
0.19
0191
0191
0.189
0187
0.183
0.179
0178
0176
0.174
0172
0172
0169
0168
0.167
0166
0162
0183
0.162
0157
0.158
0154
0.154
015
0148
0144
0142
0139
0136
0133
0.129
0129
0129
0127
0.129
013
0.13
0128
095
ppm
588
564
538
523
506
489
486
468
450
438
433
428
422
406
404
383
389
386
374
381
377
361
349
342
336
345
344
337
327
321
322
325
319
316
315
312
307
288
289
286
286
283
277
277
273
273
286
269
262
264
264
256
251
253
247
243
234
229
226
221
213
211
205
200
200
196
199
204
204
202
200
ppm
3436
3355
3230
3125
3019
2914
2852
2789
2899
2815
2563
2531
2500
2445
2396
2382
2312
2299
2269
2221
2262
2222
2125
2073
2030
2026
2075
2045
2004
1944
1927
1914
1917
1882
1872
1870
1859
1829
1792
1756
1740
1731
1710
1684
1676
1666
1648
1636
1629
1587
1611
1803
1552
1535
1521
1501
1477
1448
1418
1397
1351
1318
1292
1264
1242
1249
1240
1260
1269
1267
1251
O2
1867
187
1689
1871
1871
1873
1876
1878
1884
1886
189
1892
1894
1898
18.99
19.01
1904
1805
1808
1907
1809
181
1813
1817
1818
1918
1917
19.18
1821
1824
19.25
1928
1933
1934
1935
1935
1936
1937
1937
1939
194
1941
1943
1944
1843
1844
185
18.5
1851
18.49
19.48
1948
1852
1955
1957
1958
1958
1959
196
1961
1963
1986
1967
1967
1968
1968
1966
1969
1968
1971
1971
1352
Water
CO2 JUM-THC balance catalyst actual flow rate heat out
23
228
226
225
224
222
2.17
215
2.11
206
205
204
2.02
199
197
1.95
193
191
191
189
188
186
1.82
18
1 78
178
1.8
179
175
173
172
1.69
1.64
1.63
1.63
163
1.62
1.61
1.6
1.59
158
158
1.55
1.54
156
158
155
154
152
1.51
1.51
1.5
146
1.44
1.42
1.42
1.41
1.41
1.39
138
135
1 34
133
132
132
131
131
1.31
1.3
1 29
128
732
Ppm
201
207
208
208
209
218
229
232
232
234
233
231
236
235
233
232
233
235
237
236
235
236
237
240
241
243
246
244
245
244
244
241
237
231
228
225
221
224
223
226
226
228
230
230
232
233
233
236
237
238
238
237
238
232
230
228
227
224
222
217
214
208
207
204
204
206
206
208
207
209
210
1358
IDS
85
8
75
72
7
65
65
6
6
55
55
5
5
5
4.5
45
4
4
4
3.5
35
35
3
3
3
25
2.5
25
2
15
1.5
25
3
3
35
35
3
25
25
2
2
1.5
15
15
1.5
1
1
1
05
05
05
0
0.5
1
1
1
1
1
1.5
2
2
25
25
25
2
1.5
1.5
1
0.5
02
0
F
278
278
277
276
275
274
273
271
270
288
267
265
284
262
281
280
258
257
256
255
254
252
250
249
248
246
246
244
243
242
240
238
237
235
234
233
232
230
230
229
228
227
226
226
225
224
224
223
222
222
222
221
220
219
217
217
216
215
214
213
212
211
210
210
209
209
208
208
207
207
206
385
gpm Btu/mterval
62 3544
62 3544
62 3544
62 3544
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
6.2
6.2
62
62
6.2
62
62
62
6.2
62
6.2
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
6.2
62
8.2
62
62
62
82
62
82
82
62
62
62
62
62
62
62
62
62
62
62
62
62
62
6.3
3544
354.4
3544
3544
3544
3544
3544
3544
3544
3544
3308
3544
3038
3544
3544
3544
3038
3038
3038
3038
3038
3038
3038
3038
3038
3038
3546
3546
3546
3546
3039
3038
3546
2838
3039
3039
3039
3039
3039
3039
3039
3039
3039
3039
3038
3038
3038
3547
3547
3040
3547
3040
3548
3548
3548
3548
331 1
3548
3548
3548
3548
3041
304 1
304.1
3041
3041
3041
3962
Density of Water meter
Draft cool water readng
cm/on
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
On
tVgal
815
815
815
8 15
8.15
815
6 15
815
815
815
6 15
815
6 15
8.15
8 15
815
8.15
8 15
8 15
6.15
8 15
815
8 15
815
8.15
815
8.15
815
815
815
816
816
816
816
816
8.16
8 16
816
8.16
816
816
816
816
816
8 16
818
816
818
8 16
8 16
6 16
6.18
816
816
816
816
816
816
816
816
816
8 16
816
816
816
816
816
818
816
818
816
8 15
gpm
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
61
6.1
6.1
61
81
61
61
6.1
61
6.1
61
6.1
61
6.1
61
61
61
61
61
61
61
6.1
61
6.1
61
6.1
61
8.1
6.1
61
61
6 1
6.1
61
61
6.1
61
6.1
6.1
61
61
61
81
6.1
6.1
61
61
6.1
81
61
81
6.1
61
61
-------
Printed on 02-Apr-M
FURNACE A WITH CATALYST- LOW HEAT REMOVAL HATE
25-Oet-85 Rim TTCD-1 Water Density of Water meter
time »tr*i«nl dlutian stick *ov» Urn-box Wlterout wtttrin CONtfi COdlu CXllcM O2 CO2 JUM-THC bounce c»l«/»« ictual Ifew nt* heitoul On* coolwlter repdng
secFFF F FFF« ppm «m % % ppm In F a»n Btuflnt«v»l On/Of
-------
iFui-nace 1 OEM teat datiT
Elapsed
time, min.
0
10
20
30
40
50
60
70
80
90
100
110
120
130
140
150
160
170
180
190
200
210
220
230
240
250
260
270
280
290
O 300
O\ 310
CT> 320
330
340
350
360
370
380
390
400
410
420
430
440
450
460
470
480
490
SOO
510
520
530
540
550
560
570
580
590
600
610
620
630
640
650
Test #1
O2, % CO2, % CO, % Elapsed min. Elapsed min.
18 3.61 1.63
17.87 2.76 0.89
17.73 2.67 0.75
17.3 2.83 0.71 46
18.12 2.24 0.61 55
17.93 3.96 1.81
18.12 2 0.4
17.82 2.31 0.37
17.41 2.68 0.48
17.3 2.82 0.53
17.12 3.03 0.58 111 119
S.3 3.48 7.01
17.95 2.86 0.71
17.63 2.53 0.43
17.71 2.47 0.37
17.26 2.81 0.42
17.17 2.92 0.45
16.91 3.12 0.5 189
16.65 3.35 0.54 198
1 1 .84 8.73 6.65
17.43 3.58 1
17.33 2.97 0.64
17.22 2.89 0.51
17.1 2.8 0.42
16.71 3.22 0.42
16.59 3.34 0.44
16.33 3.58 0.5 273
18.02 2.66 0.54 286
16.56 5.43 3.76
17.27 3.34 0.9
17.18 2.87 0.51
17.25 2.69 0.4
16.86 2.99 0.4
16.79 3.07 0.38
16.5 3.25 ' 0.42
16.43 3.42 0.46 36S
14,24 6.07 1.07 374
16.42 4.13 1.92
16.94 3.27 0.77
16.86 3 0.47
16.31 3.4 0.44
16.27 3.41 0.41
16.01 3.67 0.45
15.77 4.04 0.5
15.05 4.3 0.52 457
15.61 4.95 0.71 483
16.28 4.17 1.96
16.41 3.75 0.95
16.29 3.7 0.69
15.87 4.03 0.64
15.88 3.95 0.59
15.3 4.41 0.68
15.32 4.4 0.68 535
14.06 6.14 1.02 543
16.19 4.45 2.02
16.58 3.59 0.87
16.28 3.45 0.56
16.01 3.73 0.17
15.33 4.09 0.55
15.58 4.18 0.61
14.69 4.72 0.75
11.82 8.03 0.75 623
16.13 3.91 1.35 631
16 3.95 0.75
15.6 4.06 0.59
Test #2
O2, % CO2, % CO, % Eteosedmin. Elapsed min.
lefoe all o3T 3 —
16.42 3.41 1.23 18
15.26 8 3.35
17.85 2.21 0.6
1763 2.09 0.44
12.14 6.42 1.05 44
17.82 4.05 1.58 57
17.8 1.83 0.38
17.68 17.92 0.39 88
14.78 3.08 0.92
4.01 4.73 9.92 100
17.92 3.43 1.16
17.95 2.06 0.48
17.89 1.94 0.39 131
6.07 12.79 3.27 141
17.52 4.92 2.15
17.5 2.91 0.73
17.44 2.55 0.545 176
14.61 4.99 1.2 185
16.77 5.14 3.32
16.93 3.38 0.92
16.72 3.1 0.55
16.35 3.31 0.53 223
9.39 10.22 0,7 232
16.51 3.91 0.06
16.2 3.65 0.61
15.68 3.94 0.88 261
9.54 9.98 0.93 271
16.6 3.91 1.23
16.18 3.81 0.67
15.69 4.03 0.57 302
10.74 9 0.89 311
16.56 4.01 1.38
15.91 4.22 0.81
15.72 4.09 0.59 343
12.71 7.23 0.81 354
16.18 4.14 141
15.91 4.06 0.77
15.45 4.2 0.58 383
13.43 6.38 1.15 395
16.29 4.29 1.68
15.77 4.15 1.1
15.76 3.97 0.7 428
16.81 3.48 0.53
12.44 7.17 1.57 442
16.28 4.45 1.74
15.94 3.89 0,93
15.55 4.11 0.69 474
14.94 4.89 1.08 489
11.79 5.66 0.86
16.43 4.57 1.76
1608 4.05 1.1
15.75 3.92 0.73 527
16.65 3.48 0.71
1096 8.78 1.53 541
16.66 4.32 1.75
16.48 3.73 1,07
16.1 3.52 0.72 576
1655 3.87 0.69 589
12.02 7.49 1.14
15.88 3.93 1.17
15.67 3.91 0.72
15.31 4.01 0.6 621
13.5 6.06 1.3 637
16.05 4.11 1.6
18.21 3.82 1.02
Test #3
brail on Draft oft
O2, % CO2.% CO. % Elapsed min. Elapsed rnln.
17.56 2.1 tofg"' 75
10.67 9.19 3.1 17
17.43 4.1 2.06
18.42 2 0.4
18.19 2.28 0.43 48
15.52 4.21 0.91 56
17.63 4.56 2.26
18.34 2.01 0.43
18.27 2.06 0.29
17.81 2.51 0.35
17.54 2.81 0.46
17.35 2.94 0.51 118
15.2 3.88 0.76 128
4.83 13.27 8.29
18.22 2.69 0.92
18.52 1.71 0.33
18.23 1.95 0.29 164
11.99 775 1.21 173
17.6S 4.54 2.22
18.37 2.31 0.6
18.27 1.95 0.37
18.15 2.13 0.35
17.3 2.76 0.45
17.08 3.01 0.54
16.92 3.19 0.63 240
15.6 5.98 4.7 247
17.67 3.32 1.27
17.84 2.41 0.56
17.7 2.32 0.4
17.16 2.64 0.41
17.11 2.78 0.42
16.57 3.27 0.49 311 318
14.98 5.28 2.41
17.14 3.3 1.01
17.3 2.81 0.57
16.73 3.05 0.55
16.35 3.38 0.56
16.39 3.35 0.56 378
16.02 3.32 0.6 387
15.95 5.08 3.21
16.88 3.69 1.26
16.93 3.26 0.75
16.61 3.41 0.63
15.89 3.78 0.59
15.57 4.03 0.6
15.11 4.41 0.63 455
14.64 5.26 1.29 465
16.91 4.54 2.47
17.02 3.39 1
16.55 3.29 0.65
16.59 3.15 0.51
16.15 3.56 0.51
16.2 3.47 0.51 529
14.3 5.81 0.82 538
14.71 5.77 3.8
16.97 4.02 1.59
17.12 3.21 0.95
16.76 3 0.64
16.29 3.25 0.55
16.01 3.45 0.54 596
13.89 5.76 1.22 604
16.12 4.25 2.34
16.57 3.63 1.15
16.23 3.56 0.83
16.06 3.52 0.72
15.48 3.96 0.71
Test #4
Draft on DraN oH
' "IS" -3-85 i45 0 8
10.05 9.85 3.26
16.93 2.95 1.02
16.6 3 0.86 32
4.23 14.3 7.68 42
17.66 3.01 1.18
17.42 2.41 053 63
7.55 11.61 2.33 72
17.55 3.95 1.79
17.53 2.38 0.57
1741 2.39 0.54 100 108
12.69 8.71 9.25
17.35 3.87 1.63
17.42 2.76 0,78 138
18.18 2.19 047 146
16.61 5.57 3.57
17.48 3.36 1.17
17.2 2.96 0.74 172
16.18 4.06 1.04 182
16.03 4.75 2.79
16.83 3.63 1.22 205
16.54 3.41 0.8 215
14.48 5.63 1.3
16.35 4.54 2.12
16.68 381 1.13
16.25 3.67 0.82 253
17.08 7.44 1.3 263
16.38 4.64 2.13
16.43 4.06 1.22
16.04 4.04 0.88 292
7.38 11.43 1.6 300
16.22 4.31 1.37
16.17 3.98 0.86 328
12.56 6.69 1.23 338
14.5 5.37 1.44
16.5 4.2 1.27
15.9 4.11 0.85 368
15.51 3.87 0.65 378
15.12 5.2 2.13
16.53 4.2S 1.47
16.18 3.95 0.93 409
14.54 5.93 1.04
12.09 7.67 1.49 421
16.25 4.45 1.63
16.16 3.83 09
15.68 4,03 0.67 455
14.76 5.27 1.15 467
15.8 4.73 1.56
16.01 4.36 t.22
15,78 4.14 0.8
15.28 4.43 0.68 SOS
14.5 5.69 0.8 519
13.7 6.33 1.51
18.05 4.73 1.5
16 4.08 0.9
15.22 4.35 0.75 555
15.53 4.61 1.1
11.78 8.25 1.24 571
16.51 4.94 2.08
16.51 3.78 1.05
15.48 4 0.78
15.25 4.11 0.63 610
13.93 5.74 1.45 624
16.09 4.75 2.27
16.07 4.29 1 .24
15.41 4.11 0.78
-------
[Furnace B OEM test data.
Elapsed
time, min.
660
670
680
690
700
710
720
730
740
750
760
770
780
790
800
810
820
830
840
850
860
870
880
890
900
910
920
930
940
950
O 960
2 970
980
990
1000
1010
1020
1030
1040
1050
1060
1070
1080
1090
1100
1110
1120
1130
1140
1150
1160
1170
1180
1190
1200
1210
1220
1230
1240
1250
1260
1270
1280
1290
1300
1310
Test #1
O2, % CO2, % CO, % Elapsed rnin. Elapsed min.
15.24 4.46 0.67
15.41 4.46 0.7
15.24 4.62 0.76 690 698
16.17 3.99 1.46
16.1 3.88 1.01
15.9 3.79 0.62
15.57 4.09 0.57
15.16 4.35 0.6
15.08 4.41 0.67
15.22 4.35 0.69 761
13.06 6.52 0.95 778
16.01 3.8? 1,08
16,06 3.62 0.62
15.89 3.76 0.57
15.78 3.8 0.57
15.75 3.89 O.S9
15.63 4.05 0.62 831
11.48 7.51 0.94 841
16.48 3.45 0.92
16.19 3.48 0.61
15.91 3.59 0.55
15.92 3.66 0.55
15.68 3.81 0.6
15.72 3.85 0.83 903
14.66 5.03 1.24 915
16.37 3.84 1.44
16.26 3.58 0.84
16.24 3.23 0.58
18.17 3.41 0.59
15.96 0.6 0.59
15.44 4.02 0.7 976
16.52 3.74 0.85 989
15.44 3.84 0.8
16.66 3.63 1.15
16.48 3.32 0.76
16.56 3.16 0.69
16.64 3.17 0.68 1034
16.74 3.19 0.7 1046
16.83 3.18 0.68
16.93 3.19 0.68
16.17 4.36 1.72
16.79 3.33 0.99
16.66 3.12 0.64
16.12 3.47 0.63
16.09 3.47 0.61
15.45 3.93 0.71
15.39 4.04 0.71
16.78 3.37 0.61 1140 1147
16.51 3.72 1.24
16.75 3.32 0.86
16.42 3.35 0.64
18.02 3.64 0.61
15.94 3.64 0.8
16.04 3.57 0.6 1208
15.08 4.24 0.71
15.23 3.57 0.6
12.16 7.7 0.54 1230
16.42 3.85 1.24
16.25 3.63 0.84
16 3.74 0.72
15.6 3.91 0.74
15.63 3.91 0.69
15.68 3.88 0.68 1298
16.94 2.7 0.58 1308
14.72 4.04 0.43
Test #2
02,% CO2, % CO, % Elapsed min. Elapsed min.
15.54 3.8 072
15.74 3.68 0.56 670
13.81 5.8 1.32 687
16.4 3.81 1.27
16.26 3.71 1.1
15.92 3.69 0.73
15.46 3.98 0.59 721
14.46 5.33 1.01 738
16.64 3.65 1.05
16.16 3.82 1.16
15.66 3.85 0.7 768
17.37 2.83 0.45
14.1? 5.58 0.93 785
16.01 3.93 1.28
15.88 3.89 0.8
15.67 3.79 0.6 816
16.53 3.67 0.61
13.95 5.73 0.92 834
18.39 3.7 1.08
15.98 3.67 0.68
15.82 3.68 0.54 864
16.1 3.93 0.72
15-47 4.48 0.7
15.38 4.63 1.10 averages
Test #3
O2, % CO2. % CO, % Elapsed min. Elapsed min.
15.73 . 3.83 0.66 663
15.2 6.47 0.81 672
15.89 4.32 1.9
15.85 3.95 1.04
15.9 3.75 0.66
15.61 3.83 0.58
14.9 4.33 0.62 729
14.78 5.41 0.73
11.14 8.44 1.14 740
15.93 4.08 1.57
15.64 3.95 1
15.7 3.76 0.75
15.21 4.16 0.71
14.51 4.65 0.77 797
15.7 4.43 0.76 807
16.25 4.27 1.83
16.13 3.76 0.97
16.22 ' 3.4 0.65
15.92 3.6 0.54
15.16 4.18 0.6
15.14 4.13 0.57 863
14.15 5.38 1.06 876
16.01 4.2 1.71
16.1 1 3.76 1
15.76 3.59 0.68
15.79 3.54 0.5
15.32 3.82 0.51
14.96 4.17 0.56 934
15.72 4.1 0.89 949
16.05 4.2 1.76
16.12 3.85 1.17
15.93 3.63 0.87
15.58 3.73 0.77
15.23 3.93 0.76
15.03 4.19 0.79
14.63 4.45 0.82 1016
15.85 4.4 0.81 1024
16.11 4.3 1.96
16.13 3.86 1.17
15.79 3.84 0.78
15.68 3.8 0.63
15.48 4.01 0.63
15.1 4.28 0.64
13.61 6.46 0.86 1090 1098
15.96 4.22 1.74
16.24 4.09 1.36
16.14 3.72 0.81
15.53 3.97 0.65
15.16 4,09 0.59
14.92 4.38 0.59
14.58 4.69 0.62 1164
15.18 5.04 0.62 1175
16.17 4.19 1.87
18.28 3.73 1,15
15.82 3.63 0.76
15.83 3.58 0.61
15.22 3.95 0.64
14.94 4.21 0.66 1238
16.08 3.06 0.51 1248
16.54 , 3.67 0.92
15.93 4.03 1.25
15,47 3.92 0.77
14.75 4.46 0.68
14.83 4.39 059
14.49 4.69 0.81
14.57 4.61 0.6 1311
Test #4
Draft on Draft off
O2, % C02,% CO, % Elapsed min. Elapsed min.
14.98 4'!23 0.59 6*4
15.14 4.77 1.09 680
11.29 8.51 1.21
15.96 4.92 1.77
15.92 4.01 0.87
15.47 4.06 0.62
14.81 4.48 0.57 721
14.04 5.88 1.05 736
15.84 4.52 1.71
16.03 4.16 1.02
15.49 4.08 0.65
14.88 4.37 0.55
16.57 3.56 0.68 788
13.24 6.52 1.29 793
16.1 4.35 1.82
15.85 4.12 1.04
15.41 3.93 0.63
15.03 4.11 0.54 837
16.27 3.23 0.39
13.87 5.94 1.14 856
15.87 4.36 1.85
15.9 4.03 1
15.62 3.84 0.67
15.31 3.88 0.56 897
17.49 2.72 0.52
13.86 5.8? 1.06 916
15.78 4.26 1.47
15.97 3.94 0.95
15.62 3.76 0.63
15.49 3.79 0.55 951
15.05 4.85 0.97 962
13.96 5.81 1.05
16.07 4.05 1.26
15.7 3.9 0.79
15.88 3.51 0.56 1005
16.56 3.B3 0,64
14.24 5.6 0.88 1022
16.39 3.8 1.09
16.18 3.63 0.78
16.2 3.32 0.54 1057
17.66 2.7 0.47
16.15 3.94 0.72
15.40 4.68 1.27 averaqes
-------
[Furnace B CEM test datlT"
Elapsed
time, min.
1320
1330
1340
1350
1360
1370
1380
1390
MOO
1410
1420
1430
1440
1450
1460
1470
1480
1490
1500
1510
1520
1530
1540
1550
1560
1570
1580
1590
1600
1610
O 1620
<£ 1630
00 1640
1650
1660
1670
1680
1690
1700
1710
1720
1730
1740
1750
1760
1770
1780
1790
1800
1810
1820
1830
Test #1
Draft on Braft off
O2, % CO2. % CO, % Elapsed min. Elapsed min.
15.96 3.91 0.78
15.6 4.02 0.66
15.68 3.89 0.57
14.87 4.42 0.62
14.94 4.37 0.6 1374
17.14 3.05 0.48 1389
13.26 6.44 0.65
16.13 3.83 1.07
16.18 3.69 0.68
15.41 4.08 0.63
15.59 3.93 0.56
15.17 4.28 0.58
15.18 4.4 0.56 1458
17.02 2.75 0.42
15.86 4.19 0.57 1474
16.55 3.79 1.14
16.59 3.55 0.96
16.47 3.38 0.69
16.19 3.47 0.6
15.85 3.74 0.61
1555 398 0.64
15.31 4.17 0.69 1540
16.48 3.54 0.59 1558
17.33 2.4 0.44
16.09 3.84 0.97
15.8T 3.67 0.89
15.89 3.55 0.57
15.81 3.73 0.57
15.46 4 0.61
15.86 3.74 0.58 1624
17.59 2.63 0.51
16.01 3.85 0.71 1646
16.7 3.31 0.74
16.22 3.47 0.65
16,43 3.17 0.47
16.47 3.14 0.47
16.18 3.4 0.51
16.37 3.3 0.49 1705
18.84 1.55 0.28
17.32 2.75 0.5
16.73 3.21 0.7 1738
16.95 2.6 0.57
16.37 3.36 0.57
16.42 3.11 0.46
16.68 2.94 0.43
16.33 3.31 0.49
16.55 3.17 0.49
16.18 3.52 0.59 1804
17.28 3.14 0.23
16.09 3.71 0.78 averages
Test #2
Draft on Draft off
02,% CO2,% CO, % Elapsed min. Elapsed min.
Test #3
Draft on Draft on
O2, % CO2, % CO. % Elapsed min. Elapsed rnin.
14.58 -tig" 6"76"" ™ -a! 1324"
15.96 4.19 1.65
16.05 3.8 1
15.61 3.76 0.73
15.3 3.96 0.61
15.01 4.22 0.6
14.66 4.47 0.82
14.08 4.92 0.7 1392
15.99 3.94 0.83 1409
15.92 4.31 1.58
15.73 4.01 1.11
15.84 3.54 0.65
15.44 3.7 0.56
14.8 4.23 0.6
1506 4.12 0.56
14.51 4.69 0.64
16.31 3.87 0.73
13.07 6.53 0.85
16 3.89 1.19
15.56 3.72 0.74
15.34 3.83 0.58
15.18 4.02 0.53
14.56 4.38 0.6
14.34 4.66 0.66
14.18 4.87 0.68 1560
14.46 5.23 0.71 1574
16.09 3.72 1.22
15.88 3.64 0.8
15.69 3.57 0.56
15,16 3.98 0.52
14.85 4.21 0.54
14.87 4.29 0.58
14.67 4.47 0.61 1643
16.02 3.88 0.72 16S8
17.88 2.37 0.28
15.84 3.82 0.93
15.83 3.62 0.65
15.59 3.63 0.54
15.41 3.81 0.56
15.35 3.91 0.59
14.97 4.14 0.65 1725
17.99 2.18 0.46 1738
14.82 4.76 0.89
15.9 3.89 1.09
15.69 3.7 0.75
15.32 3.76 0.6
15 3.84 0.58
15.01 4.04 0.64
12.54 4.13 0.67 1802
16.16 5.4 0.92
15.82 3.55 0.8S
15.57 3.9 0.86
15.76 4.01 0.93 averaqes
Test #4
Draft on Draft off
-------
Appendix E - Method 5G Meter Box Data
El
-------
Method 5G Sample Box Data
TIME
NAME: Russell Logan and Joey Valenti
DATE: 15-Jun-95
TEST No.: TD-MM5G-2A Fumac
DATA TAKFNI FVPRY-
! Tfift DP DH METER
14:38
15:08
15:38
16:08
16:38
17:08
17:38
18:08
18:38
19:08
19:38
20:08
20:38
21:08
21:38
21:42
07:04
77
70
70
71
70
70
70
69
69
68
67
66
66
66
66
end of run
run time
0.140
0.140
0.140
0.135
0.135
0.135
0.135
0.135
0.137
0.138
0.138
0.139
0.139
0.139
0.139
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
115.001
119.1
121.7
124.4
127.1
129.9
132.5
135.2
138.0
140.8
143.6
146.5
149.2
152.0
154.8
155.288
WOODSTOVE TEST DATA
00:30 hrmin
Tcond Tin Tout
55 73 77 86
56 79 95 88
46 83 98 87
50 85 100 88
44 85 100 87
47 85 100 85
51 85 99 86
54 85 100 83
56 85 99 82
56 85 100 80
56 85 99 79
56 84 99 78
57 84 98 76
57 83 98 76
57 85 98 76
Tdil WATER FLOW
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
NAME: Russell Logan and Joey Valenti
DATE: 19-Jun-95
TESTNo.:TD-MM5G-2B
DATA TAKEN EVERY:
TIME
WOODSTOVE TEST DATA
Furnace A, scoping test 2.
00:30 hrmin
Tfilt DP DH METER Tcond Tin
14:15
14:45
15:15
15:45
16:15
16:45
17:15
17:45
18:15
18:45
19:15
19:45
20:15
20:45
21:15
21:45
21:02
70
70
70
70
71
70
70
70
70
70
70
70
70
70
70
70
end of run
0.138
0.136
0.140
0.137
0.128
0.128
0.130
0.128
0.128
0.130
0.130
0.130
0.125
0.130
0.135
0.133
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
0.050
164.002
166.1
167.9
169.7
171.7
173.6
175.8
177.9
179.9
182.3
184.1
186.2
188.3
190.4
192.4
194.5
195.300
36
32
32
32
32
32
32
32
32
31
31
32
33
33
34
35
Tout Tdil
97
100
86
86
86
86
85
85
87
87
86
86
87
88
89
87
81
85
100
100
100
100
100
100
102
102
100
100
100
103
103
102
WATER FLOW
72
83
86
80
84
84
79
80
80
77
79
78
79
77
76
79
6.5
6.6
6.6
6.6
6.5
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
E2
-------
Method 5G Sample Box Data
WOODSTOVE TEST DATA
NAME: Russell Logan and Joey Valenti
DATE: 34877
TEST No.: TD-MM5G-2C Furnace A, high heat removal.
DATA TAKEN EVERY: 00:10 hnmin
TIME
; Tfilt DP DH METER Tcond Tin
11:50
12:00
12:10
12:20
12:30
12:40
12:50
13:00
13:10
13:20
13:30
13:40
13:50
14:00
14:10
14:20
14:30
14:40
14:50
15:00
15:10
15:20
15:30
15:40
15:50
16:00
16:10
16:20
16:30
16:40
16:50
17:00
17:10
17:19
79
79
79
80
80
80
80
81
82
83
84
84
85
84
84
84
84
84
84
84
83
83
83
83
83
83
83
80
80
77
76
76
76
end of run
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.14
0.135
0.135
0.136
0.14
0.138
0.138
0.14
0.14
0.141
0.141
0.141
0.141
0.02
0.03
0.025
0.025
0.03
0.025
0.04
0.03
0,03
0.03
0.03
0.03
0.03
0.04
0.03
0.03
0.04
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
201.501
201.9
202
202.8
203.3
203.8
204.2
204.7
205.2
205.7
206.2
206.6
207.1
207.6
208.1
208.6
209.1
209,5
210
210.5
211
211.4
211.9
212.3
212.8
213.3
213.8
214.2
214.7
215.2
215.6
216.3
216.7
217.1
28
30
32
33
35
36
36
36
39
40
38
38
41
46
46
50
49
49
48
51
55
56
56
58
59
58
58
56
55
55
55
58
59
Tout Tdil WATER FLOW
84
85
87
88
89
89
90
91
91
91
91
92
92
93
93
93
93
93
93
93
94
94
94
94
95
95
95
94
94
94
94
93
93
94
97
100
101
102
103
104
105
105
106
106
106
106
106
106
107
107
107
107
107
107
108
108
108
109
109
109
107
107
107
107
106
106
90
90
88
90
90
95
97
100
104
109
110
109
108
107
107
105
105
98
95
91
88
91
92
93
93
92
89
85
84
86
88
88
87
7.6
7.4
6.8
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
E3
-------
Method 5G Sample Box Data
WOODSTOVE TEST DATA
NAME: Russell Logan and Joey Valenti
DATE: 34880
TEST No.: TD-MM5G-2D Furnace A, high heat removal.
DATA TAKEN EVER' 00:10 hr:min
TIME Tfilt
10:20
10:30
10:40
10:50
11:00
11:10
11:20
11:30
11:40
11:50
12:00
12:10
12:20
12:30
12:40
12:50
13:00
13:10
13:20
13:30
13:40
13:50
14:00
14:10
14:20
14:30
14:40
14:50
15:00
15:10
15:20
15:30
15:40
15:50
16:00
16:10
16:20
16:30
16:40
16:50
17:00
17:10
17:20
17:30
17:38 end
DP DH METER Tcond Tin
76
76
75
75
75
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
75
75
75
76
76
76
76
76
76
76
76
76
76
76
76
76
76
of run
0.13
0.135
0.135
0.133
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0,135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.03
0.025
0.025
0.025
0.025
0.028
0.028
0.028
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.025
0.03
0.025
0.025
0.03
0.03
0.03
0.025
0.03
0.025
0.025
0.025
0.025
0.025
0.03
0.025
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
289.001
290.3
290.9
291.5
292
292.5
293
293.5
294
294.5
295
295.6
296.1
296.6
297.1
297.6
298.1
298.6
299.1
299.6
300.1
300.7
301.2
301.7
302.2
302.7
302.2
303.7
304.2
304.7
305.2
305.7
306.2
306.7
307.2
307.9
308.5
309.1
309.6
310.3
310.8
311.5
312
312.5
313.145
32
31
31
31
33
35
40
42
42
45
48
48
44
50
51
52
52
52
53
53
53
30
31
33
35
36
40
44
43
46
46
46
46
46
46
46
46
49
52
53
52
53
54
54
Tout Tdil WATER Fl
75
77
79
81
83
84
85
86
86
87
87
87
87
87
87
87
87
87
87
87
87
87
87
87
87
87
87
87
87
87
88
88
88
87
87
87
87
87
87
87
87
87
87
87
79
86
91
95
98
99
100
100
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
102
101
101
100
101
107
100
100
101
101
101
101
101
100
92
86
85
85
90
86
89
89
89
85
86
86
88
87
87
87
88
84
85
86
83
83
83
85
82
85
81
85
83
82
82
84
84
82
85
84
83
85
83
85
84
84
84
84
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.8
6.7
6.7
6.7
6.7
6.7
6.7
6.7
6.7
E4
-------
Method 5G Sample Box Data
WOODSTOVE TEST DATA
NAME: Russell Logan and Joey Valenti
DATE: 34878
TEST No,:TD-MM5G-1A Furnace A, low heat removal
DATA TAKEN EVERY; 00:10 hrmin.
TIME Tfilt DP DH METER Tcond Tin
12:20
12:30
12:40
12:50
13:00
13:10
13:20
13:30
13:40
13:50
14:00
14:10
14:20
14:30
14:40
14:50
15:00
15:10
15:20
15:30
15:40
15:50
16:00
16:10
16:20
16:30
16:40
16:50
17:00
17:10
17:20
17:30
17:40
17:50
18:00
18:10
18:20
18:30
18:40
18:50
19:00
19:10
19:20
19:30
19:40
19:50
20:00
79
79
78
78
78
78
78
79
78
78
78
78
78
78
78
78
78
78
76
77
77
77
78
76
76
76
76
77
76
76
77
77
77
77
77
77
77
76
75
74
74
74
74
75
75
75
75
0.12
0.125
0.124
0.122
0.122
0.124
0.123
0.123
0.123
0.123
0.123
0.123
0.123
0.123
0.123
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.04
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
217.203
218.1
218.7
219.3
220
220.5
221
221.4
221.8
222.5
223.1
223.6
223.9
224.6
225.2
225.7
226.2
226.7
227.3
227.8
228.1
228.8
229.4
229.9
230.5
231
231.5
232
232.5
232.9
233.4
233.9
234.6
335.2
235.7
236.2
236.7
237.3
237.8
238.3
238.9
239.4
239.9
240.5
241.1
241.5
242
33
32
33
34
35
36
37
39
39
40
43
39
43
44
47
46
45
48
43
46
46
43
43
46
46
43
43
44
42
44
46
44
46
46
48
48
45
46
46
46
41
42
46
43
43
46
45
Tout Tdil WATER FLOW
77
78
81
83
86
87
88
89
90
90
90
90
90
90
90
90
90
90
90
90
90
91
90
91
91
91
91
91
91
91
91
91
91
91
91
91
92
91
91
90
90
90
91
91
90
90
91
81
86
94
97
99
100
101
102
103
103
103
102
102
103
103
103
103
103
103
103
103
103
103
103
103
104
104
104
104
104
104
105
106
105
105
105
104
104
103
102
102
103
104
104
104
104
104
84
80
83
85
86
86
90
91
91
90
88
89
88
86
87
80
78
76
80
76
77
79
78
76
76
78
81
84
85
84
81
84
81
83
82
82
74
72
75
72
79
78
74
76
76
76
79
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
E5
-------
Method 5G Sample Box Data
WOODSTOVE TEST DATA
NAME: Russell Logan and Joey Valenti
DATE: 34878
TEST No.: TD-MM5Q-1A Furnace A, low heat removal
DATA TAKEN EVERY: 00:10 hrmin.
TIME
20:10
20:20
20:30
20:40
20:50
21:00
21:10
21:20
21:30
21:40
21:50
22:00
22:10
22:20
22:30
22:40
22:50
23:00
23:10
23:20
23:30
23:40
23:50
00:00
00:10
00:20
00:30
00:38
Tfilt DP DH METER Tcond Tin
75
75
75
75
75
75
75
76
76
75
76
76
76
76
75
74
74
74
74
74
73
73
74
73
74
73
74
end of run
0,125
0.125
0.124
0.124
0.124
0.124
0.12
0.122
0.124
0.12
0.122
0.122
0.122
0.125
0.125
0.125
0.125
0.125
0,125
0.123
0.123
0.123
0.122
0,123
0.123
0.122
0.122
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
242.5
243.1
243.6
244.1
244.6
245.1
245.6
246.2
246.7
247.2
247.8
248.3
248.8
249.4
249.9
250.4
250.9
251.4
252
252.5
253.1
253.6
254.1
254.6
255.2
255.7
256.2
256.651
47
43
43
46
48
44
47
47
23
30
30
31
31
33
35
36
34
35
43
43
41
43
48
45
46
49
51
Tout Tdil WATER FLOW
91
91
91
91
91
90
91
91
90
91
91
91
91
90
90
89
88
88
88
88
87
87
87
87
87
87
87
104
103
104
104
104
103
103
104
104
104
104
104
104
104
103
102
102
102
101
101
101
100
100
100
100
100
100
76
79
81
81
81
85
86
85
82
83
79
77
79
77
75
77
77
77
77
80
81
80
81
83
81
81
81
6.1
6.1
6.1
6.1
6,1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.1
6.2
6.2
6.2
6.2
E6
-------
Method 5G Sample Box Data
WOODSTOVE TEST DATA
NAME: Russell Logan and Joey Valenti
DATE: 34879
TEST No.: TD-MM5G-1B Furnace A, low heat removal,
DATA TAKEN EVER1 00:10 hnmin
TIME Tfilt DP DH METER Tcond Tin
11:50
12:00
12:10
12:20
12:30
12:40
12:50
13:00
13:10
13:20
13:30
13:40
13:50
14:00
14:10
14:20
14:30
14:40
14:50
15:00
15:10
15:20
15:30
15:40
15:50
16:00
16:10
16:20
16:30
16:40
16:50
17:00
17:10
17:20
17:30
17:40
17:50
18:00
18:10
18:20
18:30
18:40
18:50
19:00
19:10
19:20
74
74
75
74
75
74
75
75
75
75
75
75
75
75
74
74
75
74
74
74
74
74
74
74
74
73
73
73
72
72
72
72
73
73
73
73
73
73
73
73
73
73
73
73
73
73
0.13
0.13
0.13
0.13
0.13
0.13
0.13
0.13
0.13
0.13
0.135
0.135
0.135
0.135
0.134
0.133
0.133
0.133
0.135
0.135
0.133
0.13
0.13
0.13
0.134
0.134
0.131
0.131
0.132
0.13
0.134
0.131
0.131
0.131
0.131
0.131
0.131
0.131
0.13
0.13
0.131
0.131
0.131
0.131
0.131
0.131
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
256.727
257.7
258.3
258.8
259.3
259.8
260.3
260.7
261.2
261.7
262.2
262.7
263.2
263.7
264.1
264.6
265.1
265.6
266.1
266.6
267.1
267.5
268
268.5
269.1
269.5
270
270.5
270.9
271.3
271.9
272.4
272.8
273.3
273.8
274.3
274.8
275.3
275.8
276.2
276.7
277.2
277.7
278.2
278.7
279.2
35
33
33
34
34
34
35
35
35
36
40
43
50
50
46
47
52
49
52
50
52
53
53
54
54
53
40
40
41
40
40
42
45
45
45
44
46
45
48
47
47
50
50
52
52
50
Tout Tdil WATER FLOW
75
75
77
80
81
84
85
85
86
86
86
86
87
87
87
87
87
87
87
87
87
87
87
86
87
87
87
87
82
80
80
76
77
87
87
87
84
84
85
84
84
87
86
87
87
86
78
83
90
95
97
98
99
99
99
100
100
100
100
100
100
100
100
101
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
90
88
83
85
86
90
92
92
89
88
77
75
75
74
77
78
76
78
77
82
87
88
75
77
77
80
80
80
76
87
86
87
81
81
80
85
87
87
87
87
87
80
86
82
82
86
6,2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.3
6.3
6.3
6.3
6.3
E7
-------
Method 5G Sample Box Data
WOODSTOVE TEST DATA
NAME: Russell Logan and Joey Valenti
DATE: 34879
TEST No.: TD-MM5G-1B Furnace A, low heat removal.
DATA TAKEN EVER' 00:10 hr:min
TIME
19:30
19:40
19:50
20:00
20:10
20:20
20:30
20:40
20:50
21:00
21:10
21:20
21:30
21:40
. 21:50
22:00
22:10
22:20
22:30
22:40
22:45
Tfilt DP DH METER Tcond Tin
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
74
end of run
0.131
0.131
0.131
0.131
0.131
0.132
0.134
0.131
0.131
0.131
0.13
0.131
0.131
0.131
0.131
0.131
0.131
0.13
0.13
0.13
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
279.7
280.2
280.6
281.1
281.6
282.1
282.5
283
283.5
284
284.5
285
285.5
285.9
286.5
286.9
287.4
288
288.5
289.3
289.423
50
53
35
36
39
40
42
41
44
45
48
45
49
49
49
49
49
49
49
50
Tout Tdil WATER F
86
86
86
86
86
86
86
86
86
86
87
87
87
86
86
86
86
86
86
87
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
101
86
77
79
76
80
77
75
80
74
74
79
81
78
83
80
85
86
87
87
88
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
6.2
E8
-------
Method 5G Sample Box Data
WOODSTOVE TEST DATA
NAME: Russell Logan and Joey Valenti
DATE: 34996
TEST No.: TD-MM5G-2 Furnace A with catalyst, high heat output
DATA TAKEN EVERY; 00:10 hr.min
TIME
11:55
12:05
12:15
12:25
12:35
12:45
12:55
13:05
13:15
13:25
13:35
13:45
13:55
14:05
14:15
14:25
14:35
14:45
14:55
15:05
15:15
15:25
15:35
15:45
15:55
16:05
16:15
16:25
16:35
16:45
16:55
17:05
17:15
17:25
17:35
17:45
17:55
18:05
18:15
18:25
18:35
18:36
Tfilt DP DH METER Tcond Tin
70
69
69
69
68
68
68
70
71
71
70
70
70
70
70
70
70
70
70
70
70
70
70
70
70
70
71
71
70
69
69
69
70
70
70
70
70
70
70
70
70
end of run
0.13
0.132
0.132
0.132
0.132
0.132
0.132
0.125
0.122
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.127
0.125
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.125
0.125
0.125
0.125
0.125
0.13
0.13
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
313.381
314.1
314.9
315.8
316.4
317.2
317.9
318.6
319.2
319.5
320
320.5
321.3
321.5
322.5
322.9
323.4
324.1
324.5
325
325.6
325.9
326.2
327
327.6
328.1
328.7
329.2
329.8
330.3
330.8
331.4
331.9
332.2
333
333.6
334
334.7
335.2
335.8
336.3
336.351
30
29
31
31
31
33
33
35
36
38
38
40
40
30
30
32
38
39
40
42
42
42
43
44
46
48
47
47
48
49
48
49
49
49
49
50
50
50
50
50
51
Tout Tdil WATER FLOW
70
70
74
74
79
80
80
81
82
82
79
78
77
77
77
80
85
82
79
79
77
76
79
77
76
76
86
86
86
86
86
86
86
86
86
87
86
86
86
86
86
78
85
95
100
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
101
75
79
76
77
73
73
77
102
124
80
79
78
77
77
77
80
109
85
85
86
86
86
86
86
86
101
112
79
77
78
76
79
75
85
92
98
99
99
100
98
97
6.6
6.8
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7,2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
E9
-------
Method 5G Sample Box Data
WOODSTOVE TEST DATA
NAME: Russell Logan and Joey Valenti
DATE: 34997
TESTNo.:TD-MM5G-1
DATA TAKEN EVERY:
Furnace A with catalyst, low heat removal.
00:10 hnmin
TIME Tfilt DP DH
10:45
10:55
11:05
11:15
11:25
11:35
11:45
11:55
12:05
12:15
12:25
12:35
12:45
12:55
13:05
13:15
13:25
13:35
13:45
13:55
14:05
14:15
14:25
14:35
14:45
14:55
15:05
15:15
15:25
15:35
15:45
15:55
16:05
16:15
16:25
16:35
16:45
16:55
17:05
17:15
17:25
17:35
17:45
17:55
18:05
18:15
18:25
18:35
70
70
75
74
71
71
71
70
69
70
69
69
68
67
68
69
69
70
69
70
70
71
69
70
70
70
70
70
70
70
70
70
70
70
70
70
70
70
70
70
69
69
70
69
70
69
69
69
0.12
0.12
0.13
0.13
0.13
0.13
0.13
0.13
0.13
0.132
0.13
0,13
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.13
0.133
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.128
0.128
0.134
0.134
0.134
0.134
0.134
0.134
0.134
0.134
0.134
0.134
0.13
METER Tcond Tin
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
336.551
337.4
338.3
339.3
340.3
341.1
341.6
342.1
342.8
343.3
343.9
344.5
345.2
345.8
346.4
347
347.6
348.2
348.9
349.5
350.1
350.7
351.3
352
352.6
353.1
353.9
354.1
354.9
355.6
356.2
356.8
357.5
358.1
358.7
359.3
359.9
360.5
361.1
361.8
362.4
363
363.6
364.2
364.8
365.5
366.1
366.7
40
33
33
33
33
34
34
36
37
40
39
40
40
42
42
42
41
43
42
42
42
34
35
36
36
36
38
38
38
39
39
37
39
39
40
41
40
40
40
40
40
40
40
40
40
40
40
41
E10
Tout Tdil WATER FLOW
68
70
74
77
80
81
83
83
82
83
83
83
84
84
84
84
84
85
85
85
85
85
86
86
86
86
85
85
85
85
85
85
85
85
85
85
85
85
85
85
84
84
84
84
84
84
84
84
72
78
86
91
94
97
97
98
97
97
97
97
97
98
98
98
98
99
98
98
99
99
99
100
99
99
99
99
99
99
99
99
99
98
98
99
98
99
98
98
98
98
98
98
98
98
98
98
83
98
120
79
78
78
79
75
78
78
78
75
77
74
76
77
75
75
76
76
98
80
74
74
76
76
77
77
77
73
75
75
75
72
80
99
88
76
73
74
76
75
75
74
75
75
75
74
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6,3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6,1
6.1
6.1
6.1
6.1
6.1
-------
Method 5G Sample Box Data
WOODSTOVE TEST DATA
NAME: Russell Logan and Joey Valenti
DATE: 34997
TEST No.;TD-MM5G-1 Furnace A with catalyst, low heat removal.
DATA TAKEN EVERY: 00:10 hnmin
TIME Tfilt
18:45
18:55
19:05
19:15
19:25
19:35
19:45
19:55
20:05
20:15
20:25
20:35
20:45
20:55
21:05
21:15
21:25
21:35
21:45
21:55
22:05
22:15
22:25
22:35
22:45
22:55
23:05
23:15
23:25
23:35
23:45
23:55
00:05
00:11 end
DP DH
69
69
70
69
69
69
69
69
67
67
67
66
66
65
65
65
65
64
64
64
63
63
63
62
62
62
63
66
67
68
69
69
68
of run
0.134
0.134
0.126
0.126
0.126
0.126
0.13
0.132
0.132
0.13
0.133
0.135
0.135
0.135
0.135
0.13
0.13
0.128
0.128
0.13
0.13
0.13
0.13
0.13
0.13
0.135
0.135
0.131
0.131
0.135
0.135
0.135
0.135
METER Tcond Tin
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
0.03
367.4
368.2
368.6
369.2
369.8
370.4
371
371.6
372.3
372.8
373.4
374.1
374.7
375.3
375.9
376.5
377.1
377.8
378.4
379
379.7
380.2
380.8
381.5
382.1
382.7
383.3
384
384.5
385.2
385.8
386.4
387
387.44
32
32
34
34
35
34
35
35
35
35
35
36
36
36
36
36
36
36
40
40
40
40
41
40
40
38
39
41
41
42
42
45
42
Tout Tdil WATER F
84
84
85
84
84
84
84
84
83
83
84
84
83
83
81
82
82
81
81
81
80
80
79
79
79
79
80
81
82
83
82
84
84
98
98
99
98
98
97
98
98
97
98
98
98
97
97
97
96
96
96
96
95
95
94
94
93
92
93
94
96
97
98
98
98
98
74
74
95
95
93
98
75
76
74
75
72
71
70
70
69
83
86
81
87
86
86
85
85
83
79
79
84
84
82
81
83
78
81
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
Ell
10
-------
Furnace B Modified Method SO Meter Box Data for Run I
m
*__*
to
Elasped Weight Hue Tunnel DGM #1 ROTO 1
Time Remain Gas Temp Read Read
Min. Lb Temp °F ft*
0
10
20
30
40
50
60
70
80
90
100
110
120
130
140
150
160
170
180
190
200
210
220
230
240
250
260
270
280
290
300
310
320
330
340
350
360
370
380
390
400
410
125.34
118.00
117.50
117.00
1 16.5
115.5
104.5
10.3.5
103.0
102.5
102.0
101.5
94.0
92.0
91.5
91.0
90.5
90.0
90.0
89.5
82.5
81.0
80.5
80.0
79.5
79.5
79.0
79.0
78.5
72.0
71.5
71.0
70.5
70.5
70.0
70.0
69.5
68.5
64.5
64.5
64.0
63.5
,p
115.
150.
125
119
116
179
154
133
124
119
117
115
290
138
129
122
119
116
115
134
149
135
128
121
117
114
112
111
170
159
130
123
118
114
111
110
109
223
137
123
117
113
88
94
90
90
88
99
94
91
82
90
89
81
81
91
90
90
90
90
90
94
99
91
91
90
90
89
89
89
97
94
90
89
89
89
88
88
87
104
90
88
87
87
567.5
568.0
568.5
569.0
569.5
570,1
570.6
571.1
571.7
572.2
572.7
573.7
573.2
574,2
574.7
575.2
575.2
576.2
576.2
577.2
577.7
578,0
578.5
579,0
579,6
580.0
580.7
581.3
581.9
582.4
582.9
583.5
584. 1
584.6
585.2
585.8
586,3
586.9
587.4
588.0
588.6
589.2
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DGM
Temp
Inlet
op
81
83
83
85
84
85
85
86
86
87
87
87
88
88
89
89
89
89
90
89
90
89
91
90
91
91
90
90
91
90
91
91
91
91
91
91
91
91
91
91
92
92
DGM
Temp
Outlet
op
81
82
82
83
83
84
84
85
85
86
86
86
87
87
88
88
88
89
80
80
80
89
90
90
90
90
90
90
90
90
90
90
90
91
91
90
90
90
90
91
91
91
Filter DGM #2
Temp Read
°F ft'
77
79
78
79
79
79
79
78
78
79
79
78
81
74
79
74
79
79
80
80
80
80
80
80
81
80
80
80
80
81
81
80
80
81
80
80
80
81
82
82
83
83
944.6
945.1
945.7
946.2
946.7
947.2
947.7
948.2
948.7
949.2
949,7
950.2
950.7
951,2
951,7
952.2
952.7
953,2
953,7
954.2
954.7
955,0
955.5
956.0
956.6
957.1
957.6
958.2
958,7
959.2
959.6
960.1
960.6
961.1
961.6
962,2
962.7
963.3
963.8
964.4
964.9
965.5
ROTO 2
Read
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DGM
Temp
Inlet
op
77
81
82
82
82
82
83
84
85
85
85
85
86
86
87
87
87
87
87
87
88
88
88
88
88
88
88
88
88
88
88
89
89
89
89
89
88
89
89
89
90
90
DGM
Temp
Outlet
°F
80
80
81
81
81
82
82
83
83
84
84
84
85
85
86
86
86
86
86
87
87
87
88
87
87
88
87
87
87
87
88
88
88
88
88
88
88
88
88
88
89
89
Filter
Temp
78
80
79
79
79
80
79
79
79
79
79
79
81
74
80
80
80
80
80
80
80
80
81
80
80
81
80
80
80
81
81
80
80
81
81
80
80
81
82
82
83
83
Tunnel
Velocity
&P
in.H,0
.267
.264
.269
.265
.265
.265
.268
.268
.272
.268
,269
.268
.264
.266
.265
.270
.265
.268
.265
.265
,263
,265
.260
,263
.260
,263
.265
.265
,260
.263
.265
.265
.265
.265
.263
.265
.265
.260
.268
.268
.265
.265
Draft
in.H20
.025
.023
.019
.018
,015
.040
.029
.025
.020
,019
.018
.017
.032
.025
.030
.020
.018
.015
.015
.022
.030
,025
.020
.020
.020
.015
.015
.015
.025
.028
.023
.030
.018
.015
.015
.015
.013
.040
.020
.020
.020
.018
Water temperature
inlet outlet
«p «p
174
179
177
176
174
173
180
179
177
176
175
174
180
180
179
178
176
176
175
173
180
180
179
178
178
176
175
174
173
180
180
179
178
177
176
175
174
173
ISO
179
178
176
179
185
182
181
179
178
186
184
182
181
180
178
185
185
184
183
182
180
ISO
178
186
185
184
183
182
181
180
179
178
186
186
185
183
183
181
180
179
178
186
185
183
182
-------
Furnace B Modified Method 5G Meter Box Data for Run I
m
UJ
420
430
440
450
460
470
480
490
500
510
520
530
540
550
560
570
580
590
600
610
620
630
640
650
660
670
680
690
700
710
720
730
740
750
760
770
780
790
800
810
820
830
Weight
Remain
Lb
63.5
63.5
63.0
6.3.0
67.5
67.5
58.5
58.5
58.0
58.0
57.5
57.5
56.5
54.0
53.5
53.5
53.5
5.3.5
53.0
53.0
51.0
50.0
50,0
50.0
50.0
49.5
49.5
49.0
47.0
46.5
46.5
46.0
46.0
46.0
46.0
44.0
43.5
43.0
43.0
4.3.0
43.0
43.0
Rue
Gas
Temp
°F
110
109
108
107
231
130
119
115
111
109
108
107
251
130
116
112
109
107
107
106
299
122
113
110
108
108
107
137
158
115
110
108
107
106
106
275
119
III
108
106
106
125
Tunnel
Temp
op
87
86
86
86
104
88
87
87
86
86
86
85
107
87
86
86
85
85
85
84
116
86
85
85
84
84
84
89
88
84
84
83
83
83
83
110
84
84
83
8.3
83
86
DCMfl
Read
ft3
589.8
590.4
591.1
591.6
592.1
592.2
592.7
593.3
593.8
594.4
594.9
595.4
. 596.0
596.5
597.0
597.5
598.1
598.6
599.2
599.7
600.2
600.7
601.3
601.8
602.3
602.8
603.4
603.9
604.4
605.0
605.5
606.1
606.6
607.2
607.7
608.2
608.8
609.3
609.9
610.4
611.0
611.5
ROTO 1
Read
30
30
30
30
20
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DGM
Temp
Inlet
«p
92
92
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
94
93
93
91
89
87
85
85
84
83
82
82
82
82
81
81
DGM
Temp
Outlet
°F
92
92
92
92
92
93
93
93
92
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
92
93
92
90
89
87
86
85
84
83
83
82
82
81
81
Filter DGM #2 ROTO 2 DGM DOM Filter Tunnel Draft Water temperature
Temp Read Read Temp Temp Temp Velocity in.H20 inlet outlet
°F ft* Inlet Outlet "F aP °F °F
°F "F in.H,0
83
84
84
84
84
82
84
85
86
85
86
85
86
85
85
85
85
85
85
85
85
85
85
85
84
84
84
83
82
82
83
82
81
81
80
80
80
80
80
80
79
79
966.1
966.6
967.3
967.9
968.3
968.5
969.0
969.5
970.0
970.5
971.1
971.6
972.1
972.6
973.2
973.7
974.2
974.7
975.3
975.8
976.3
976.8
977.3
977.9
978.3
978.8
979.4
979.9
980.4
980.9
981.4
982.0
982.5
983.0
983.6
984.1
984.6
985.2
985.7
986.2
986.8
987.3
30
30
30
30
20
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
20
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
90
90
91
91
91
91
91
91
91
91
91
91
91
91
91
91
91
91
91
91
91
91
91
91
91
91
91
91
91
89
89
88
86
85
84
83
83
82
83
82
82
82
89
90
90
90
90
90
90
90
90
90
90
90
90
91
91
91
91
90
91
90
91
91
90
90
91
91
91
91
90
90
88
88
87
86
85
84
83
83
83
83
82
82
83
83
84
84
84
84
83
84
84
84
84
84
85
85
85
85
84
84
84
84
85
84
84
84
84
83
83
83
83
82
82
82
82
82
81
82
81
81
SI
80
80
80
.265
.265
.265
.265
.260
.265
.267
.267
.267
.267
.268
.267
.261
.270
.268
.269
.268
.267
.270
.271
.263
.270
.270
.269
.270
.270
.268
.266
.268
.270
.269
.269
.270
.270
.270
.263
.220
.279
,271
.272
.272
.270
.015
.015
.015
.015
.050
.020
.018
.017
.016
.015
.015
.014
.050
.021
.019
.017
.016
.015
.015
.014
.042
.020
.018
.015
.015
.015
.014
.022
.021
.017
.016
.015
.014
.013
.012
.043
.016
.014
.012
.Oil
.011
.019
176
175
174
173
173
179
178
177
176
175
174
173
173
179
178
177
176
175
174
173
176
178
177
176
175
174
174
173
179
178
177
176
175
174
174
177
179
177
177
175
175
173
181
180
179
178
178
185
184
182
181
180
179
178
179
185
184
183
181
180
179
178
181
184
183
182
181
180
179
178
184
184
182
181
18!
180
178
182
184
183
182
181
180
179
-------
Furnace B Modified Melhod 5G Meier Box Data for Run I
Dale: BJune 1995
trt
F.lasped
Time
Min.
840
850
860
870
880
890
900
910
920
930
940
950
960
970
980
990
1000
10(0
1020
1030
1040
1050
1060
1070
1080
1090
1 100
1110
1120
II 30
1140
1150
1 160
1170
1180
1190
1200
1210
1220
1230
1240
1250
Weight
Remain
Lb
40,5
40.0
40.0
40.0
40.0
40.0
39.5
38.5
37.0
36.5
.36.5
36.5
36.5
36.0
36.5
33.0
33.0
32.5
32.5
32.0
32.0
31.5
30.5
28.0
27.5
27.5
27.5
27.5
27.5
27.0
26.5
24.0
24.0
24.0
23.5
23.5
23.5
23.0
23.0
20.5
20.5
20.0
Flue
Cas
Temp
»P
333
120
111
108
107
106
104
245
132
114
108
106
105
105
200
195
119
111
108
106
105
104
20,3
146
116
110
106
104
104
104
194
151
116
no
108
107
106
106
154
278
121
113
Tunnel
Tetnp
°F
110
84
83
83
83
82
82
103
85
83
82
82
82
82
94
84
84
83
83
82
83
82
96
86
83
82
82
86
83
83
95
87
84
84
84
84
84
84
91
102
86
86
DGM#1
Read
ft'
612.1
612.6
613.2
613.7
614.3
614.8
615.4
615,9
616.4
617.0
617.5
618.1
618.6
619.2
619,7
620.3
620.8
621.4
621.9
622,4
623.0
623.5
624.1
624.6
625.2
625.7
626,2
626.7
627.3
627.8
628,3
628.8
629.3
629.8
630.3
630.8
631.3
631.8
632.3
652,8
633.3
63.3.8
ROTO 1
Read
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DGM
Temp
Inlet
°p
81
Si
80
81
81
80
80
80
80
80
80
80
80
80
81
80
82
82
83
84
84
85
85
86
86
87
88
89
89
90
87
84
83
82
82
81
81
80
80
80
80
80
DGM
Temp
Outlet
op
81
81
81
81
81
80
80
80
80
80
80
80
80
80
80
80
81
81
82
83
83
84
85
85
86
86
87
88
88
89
88
86
83
83
82
81
81
81
80
80
80
80
Filter DGM #2 ROTO 2 DGM DGM Filter Tunnel Draft Water temperature
Temp Read Read Temp Temp Temp Velocity in.H20 inlet outlet
°F ft1 Inlet Outlet °F &P °F °F
"F °F in.H,0
987.8
988.3
988.9
989.4
989,9
990.5
991,0
991.5
992.0
992.6
993.1
993,6
994.2
954.7
995.2
995,7
996.3
996,8
997.3
997.8
998.4
998.9
999.4
78 1000,0
78 1000.5
77 1001.0
77 1001.5
78 1002.1
78 1002,6
77 1003.1
78 1003.6
79 1004.1
77 1004,6
78 1005.1
78 1005.6
78 1006.1
77 1006.6
77 1007.1
77 1007.6
77 1008.1
77 1008.6
.77 1009.1
79
79
79
79
78
78
78
78
78
78
78
78
78
78
78
78
77
76
77
76
77
77
77
30
30
30
30
30
.30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
82
82
82
81
81
81
81
81
81
81
81
81
81
81
81
80
81
81
82
82
83
83
83
83
83
86
87
89
89
90
87
85
84
83
82
82
82
81
81
81
81
81
82
82
81
81
81
81
81
81
81
81
81
81
81
81
81
80
81
81
81
82
82
82
83
83
83
85
86
87
88
88
88
86
85
84
83
83
82
82
81
81
81
8)
80
80
80
79
79
78
78
79
79
79
78
78
78
78
78
73
78
77
77
77
77
77
78
78
78
77
77
77
77
77
77
77
78
78
78
78
77
77
77
78
77
77
.270
,270
.270
.271
.270
,272
.272
.267
,272
.271
.272
.273
.270
.275
,270
.272
.274
,274
.275
,275
.275
.275
.272
.274
.275
.277
.274
.273
.272
.270
.267
.271
.268
.274
.269
.273
.276
.272
.267
.270
.270
.271
.023
,014
.014
.Oil
.011
.Oil
.011
.034
,017
.014
.012
,011
.011
.011
.029
.021
.016
.014
.013
.012
.012
.012
.030
.020
.019
.015
.015
.015
.014
.013
.030
.020
.015
.015
.013
.Oil
.Oil
.010
.019
.022
.015
.014
179
179
178
177
176
175
173
174
179
178
176
176
175
174
173
179
180
178
178
176
175
175
175
180
180
178
178
177
174
175
173
179
179
178
177
176
175
175
173
179
179
178
185
185
184
182
181
180
179
180
185
184
182
182
180
180
179
185
185
184
183
182
181
180
180
186
185
184
183
182
181
180
179
186
185
183
182
181
180
180
178
184
185
183
-------
Furnace B Modified Method 5O Meter Box Data for Run I
m
Elasped
Time
Min.
1260
1270
1280
1290
1300
1310
1320
1330
1340
1350
1360
1370
1380
1390
1400
1410
1420
1430
1440
1450
1460
1470
1480
1490
1500
1510
1520
1 530
1540
1550
1560
1570
1580
1590
1600
1610
1620
1630
1640
1650
1660
1670 „
Weight
Remain
Lb
20.0
19.5
19,5
19.5
19.0
17.0
16.5
16.5
16.0
16.0
16.0
16.0
15.58
13.50
13.50
13.00
13.00
13.00
13.00
12.50
12.50
11.00
10.00
09.50
09.50
09.50
09.50
09.40
09.50
08.00
07.00
06.50
06.50
06.50
06.50
06.50
06.50
06.00
05.00
04.00
04.00
04.00
Flue
Gas
Temp
°p
110
108
107
108
162
188
117
113
111
110
109
109
184
211
122
114
112
111
110
109
155
237
132
117
113
111
110
110
117
201
175
120
114
113
112
HI
110
175
213
136
118
114
Tunnel
Temp
op
86
85
86
86
93
92
87
87
88
87
87
87
97
95
89
89
88
89
88
87
93
108
90
90
89
89
90
90
91
102
95
91
91
91
91
91
91
99
105
93
92
91
DGM#I
Read
ft'
634.3
634.8
635.3
635.8
636.3
636.8
637.3
637.8
638.3
638.8
639.3
639.8
640.3
640.8
641.3
641.8
642.3
642.8
643.3
64.3.8
644.3
644.8
645.3
645.8
646.3
646.8
647.3
647.8
648.3
648.8
649.3
649.8
650,3
650.8
651,3
651.8
652.3
652.8
653.3
653.8
654.3
654.8
ROTO 1
Read
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
.30
30
30
30
30
.30
30
30
DGM
Temp
Inlet
°F
80
80
80
80
80
80
80
81
82
83
83
85
85
85
86
86
85
86
84
83
83
83
83
83
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
DGM
Temp
Outlet
°p
80
80
80
80
80
80
80
80
81
82
82
84
84
84
85
85
85
85
84
83
83
83
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
Filter DGM #2 ROTO 2 DGM DGM Filter Tunnel Draft Water temperature
Temp Read Read Temp Temp Temp Velocity in.H,0 inlet outlet
°F ft' Inlet Outlet °F A? °F °F
76 1009.6
75 1010.1
76 1010.6
75 1011.I
76 1011.6
76 1012,1
75 1012.6
75 1013.1
77 1013.6
77 1014.1
77 1014.6
77 1015.1
77 1015.6
77 1016.1
78 1016.6
78 1017.1
78 1017.6
78 1018.1
78 1018.6
78 1019.1
78 1019.6
78 1020.1
78 1020.6
78 1021.1
78 1021.6
77 1022.1
78 1022.6
77 1023.1
77 1023.6
77 1024.1
77 1024.6
77 1025.1
78 1025.6
77 1026.1
78 1026.6
78 1027.1
78 1027.6
78 1028.1
78 1028.6
78 1029.1
78 1029.6
78 1030.1
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
81
81
81
81
81
81
81
81
82
83
83
84
84
84
85
84
84
84
84
83
83
83
8.3
83
82
82
83
82
82
82
82
82
82
82
82
82
82
83
83
83
83
83
81
81
81
81
81
81
81
81
82
82
82
83
83
83
84
84
83
83
83
83
83
83
83
83
82
82
82
82
82
82
82
82
82
82
82
82
82
83
82
8.3
82
8.3
76
76
76
76
76
76
76
76
77
77
77
77
78
78
78
78
78
78
78
78
78
79
79
79
79
78
78
78
78
78
78
78
78
78
78
78
78
79
79
79
79
79
.268
.272
.270
.270
.267
.267
.269
.269
.269
,268
.267
.270
.268
.269
.268
.269
.269
.270
.268
.269
.267
.262
.268
.270
.266
.266
.269
.269
.266
.268
.269
.266
.268
.274
.270
,266
.269
.265
.364
.268
.271
.271
.013
.011
.011
.011
.023
.020
.015
.013
.012
.Oil
.011
.010
.025
.021
.015
.014
.014
.012
.011
.010
.019
.031
.016
.014
.013
.Oil
.010
.010
.015
,025
.019
.015
.013
.011
.010
.010
,01 i
.020
.025
.014
.013
.011
177
176
175
174
173
179
179
177
177
176
175
175
174
179
179
178
177
176
175
174
173
175
179
178
177
176
175
174
173
174
178
179
177
177
176
175
174
173
175
179
178
177
182
181
180
179
178
185
184
183
182
182
180
180
179
185
185
184
183
182
180
179
178
180
184
183
182
181
180
179
178
179
184
183
182
181
181
180
179
178
181
184
183
182
-------
Furnace B Modified Method 5O Meter Box Data for Run I
Date: WJune 1995
Elaspcd
Time
Min.
1680
1690
1700
1710
1720
1730
1740
1750
1760
1770
1780
1790
1800
1810
Weight
Remain
Lh
04.00
04.00
03.50
03.50
03.00
02.00
01.00
01.00
01.00
01.00
01.00
01.00
00.50
00.00
Flue
Gas
Temp
op
112
III
110
158
184
207
175
122
115
110
III
110
109
261
Tunnel
Temp
op
91
90
90
96
100
104
95
91
90
90
90
89
89
100
DGM «
Read
ft'
655.3
655.8
656.3
656.8
657.3
657.8
658.3
658.8
659.3
659.8
660.3
660.8
.661.3
661.8
'I ROTO 1
Read
30
.30
30
.30
30
30
30
30
30
30
30
30
30
30
1 DGM
Temp
Inlet
°F
82
82
82
82
82
83
83
83
83
83
83
83
82
83
DGM
Temp
Outlet
°F
82
82
82
83
82
83
83
83
83
83
83
82
82
83
Rlter DGM #2 ROTO 2 DOM DGM Filter Tunnel Draft Water temperature
Temp Read Read Temp Temp Temp Velocity in.H20 inlet outlet
°f ft' Inlet Outlet °F &P °F °F
°F °F in.H,0
78
78
78
78
78
78
78
79
79
78
78
78
78
78
1030.6
1031.1
1031.6
1032.1
1032.6
1033.1
1033.6
1034.1
1034.6
1035.2
1035.7
1036.3
1036.7
1037.2
30
30
30
30
30
30
30
30
30
30
30
30
30
30
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
82
83
83
83
83
83
83
83
83
83
83
83
83
79
79
79
79
75
80
79
79
79
79
79
79
79
78
.368
.270
.270
.268
.270
.267
.269
.271
.270
.270
.27!
.271
.270
.270
.011
.011
.Oil
.016
.021
.026
.019
.014
.012
.011
.Oil
.010
.010
.019
176
175
174
173
173
176
179
179
178
177
176
175
174
173
181
180
179
178
179
181
184
184
183
182
181
180
178
179
tn
Os
-------
Furnace B Modified Mclhod 5G Meier Box Data for Run 2
Dale: *»June 1995
m
Elasped Weight
Time
Min.
0
10
20
30
40
50
60
70
80
90
100
no
120
130
140
150
160
170
180
190
200
210
220
230
240
250
260
270
280
290
300
310
320
330
340
350
360
370
380
390
400
410
Remain
Lb
132.81
131.5
115.00
1 14.50
114.0
1 1 1 .5
97.0
96.0
95.0
94.5
81.5
78.5
77.5
77.0
72.5
66.0
65.0
64.5
63.0
57.5
56.5
56.5
56.0
54.0
52.0
52.0
52.0
49.5
48.5
48.0
47.5
45.5
44.5
44.5
44.0
43.0
41.5
41.5
41.5
40.5
38.0
38.0
Rue
Gas
Temp
»F
112
154
213
137
127
272
162
142
133
167
307
149
138
128
379
155
139
129
229
157
134
125
120
307
134
124
119
333
134
123
119
317
134
123
118
274
142
124
120
259
152
127
Tunnel
Temp
op
87
95
101
90
89
121
94
90
90
97
126
91
90
89
148
92
90
89
105
92
89
89
89
117
90
90
90
125
91
90
90
123
92
91
91
113
93
91
91
112
95
92
DGM#1
Read
ft-'
661.9
662.4
662.9
66.3.5
664.0
664.5
665.0
665.5
666.0
666.5
667.0
667.5
668.1
668.7
669.2
669.7
670.2
670.8
671.3
671.8
672.4
672.9
673.4
674.0
674.5
675.0
675.5
676.1
676.6
677.1
677.7
678.2
678.7
679.2
679.8
680.3
680.9
681.4
681.9
682.5
683.0
683.6
ROTO 1
Read
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DGM
Temp
Inlet
°F
82
82
83
83
83
84
85
85
85
85
86
86
86
86
86
85
84
83
82
82
83
82
82
82
83
82
82
82
82
82
82
82
82
82
82
81
81
8!
82
82
82
82
DOM
Temp
Outlet
op
81
82
82
82
83
83
84
84
84
85
85
85
85
86
86
85
84
83
83
83
83
82
82
82
82
82
82
82
82
83
82
82
82
81
82
81
81
81
82
82
82
82
Filter
Temp
op
76
76
77
77
77
77
78
77
77
78
79
78
78
78
78
79
79
78
79
85
80
78
78
84
89
89
88
89
89
89
90
87
83
88
87
83
90
85
89
87
83
81
DGMt2
Read
ft'
37.3
37.8
38.3
38.8
39.3
39.8
40.3
40.8
41.3
41.8
42.3
42.8
43.4
43.9
44.4
44.9
45.4
46.0
46.5
47.0
47.6
48.1
48.6
49.2
49.7
50.2
50.7
51.3
51.8
52.3
52,9
53.4
53,9
54.4
55.0
55.5
56.0
56.5
57.0
57.5
58.1
58.6
RC
Re
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DGM
Temp
Inlet
°p
80
80
81
81
82
83
84
84
84
84
85
85
84
85
84
84
84
83
83
82
83
83
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
DGM
Temp
Outlet
op
80
80
80
80
81
82
82
82
83
83
83
83
83
84
84
84
83
83
83
83
83
82
82
82
83
83
83
82
82
83
82
82
82
82
81
82
81
82
82
82
82
82
Filter
Temp
op
78
78
82
78
77
81
80
78
78
78
82
78
78
78
79
78
79
79
79
89
90
89
86
83
89
89
89
89
89
90
89
90
87
89
89
89
89
88
89
88
85
83
Tunnel
Velocity
AP
in.H20
.261
.258
.260
.260
.264
.253
.260
.261
.263
.258
.248
.260
.260
.262
.248
.263
.259
.260
.257
.260
.263
.264
.265
.255
.260
.264
.260
.257
.264
.261
.263
.260
.261
.261
.259
.256
.262
.261
.260
.257
.250
.260
Draft
in.H20
.013
.022
.031
.024
.020
.051
.030
.026
.023
.027
.041
.035
.025
.021
.063
.029
.023
.020
.039
.025
.020
.019
.017
.046
.030
.017
.015
.048
.020
.017
.015
.045
.019
.015
.014
.039
.020
.017
.013
.0.35
.019
.015
Water Temperature
Inlet
°F
173
170
176
173
171
170
177
174
172
168
174
173
171
168
179
174
171
169
167
174
172
171
169
170
173
171
169
171
173
170
169
170
172
171
169
169
172
170
168
168
17.3
171
Outlet
Op
182
178
185
182
180
179
187
184
181
177
185
185
182
179
181
186
183
180
177
186
183
181
179
180
183
ISO
179
182
184
182
179
181
183
181
179
179
183
181
179
178
184
182
-------
Furnace B Modified Method 5G Meter Box Data for Run 2
Date: 0June 1995
m
K—i
00
'-•f
Elasped
Time
Min.
420
430
440
450
460
470
480
490
500
510
520
530
540
550
560
570
580
590
600
610
620
630
640
650
660
670
680
690
700
710
720
730
740
750
760
770
780
790
800
810
820
830
Weight
Remain
Lb
38.0
37.5
35.0
34.0
33.5
33.5
32.5
30.0
29.0
28.5
28.5
28.0
25.0
23.5
23.0
23.0
22.5
20.0
20.0
19.5
19.5
18.0
16.0
16.0
15.5
15.5
14.5
12.0
11.5
11.5
11.5
10.5
08.5
08.0
08.0
08.0
06.0
04.5
04.5
04.5
04.5
02.5
Flue
Gas
Temp
°F
120
180
285
138
124
120
217
248
134
125
120
185
344
138
126
120
222
270
132
122
118
265
170
128
121
117
269
189
129
120
117
266
218
130
120
143
302
149
125
118
203
294
Tunnel
Temp
op
92
100
119
93
92
91
105
102
92
92
91
100
133
93
81
91
105
104
92
91
90
113
95
90
90
89
113
95
90
89
88
112
98
90
88
98
122
90
88
87
100
121
DGM#1
Read
ft1
684.1
684.7
685.2
685.7
686.3
686.8
687.3
687.9
688.4
688.9
689.4
690.0
690.5
691.1
691.6
692.1
692.7
693.2
693.2
693.7
684.2
694.7
695.3
695.8
696.3
696.8
697.4
698.0
698.5
699.1
699.6
700.2
700.7
701.2
701.7
702.3
708.8
703.4
705.9
704.4
705.0
705.5
ROTO 1
Read
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DOM
Temp
Inlet
°F
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
83
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
83
82
82
82
DGM
Temp
Outlet
oF
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
83
82
82
82
82
82
82
82
82
82
82
82
82
82
82
83
82
83
83
82
83
83
82
82
83
83
83
Filter
Temp
op
80
79
80
90
90
89
89
90
90
90
89
85
90
90
89
89
90
90
81
81
80
80
79
79
78
78
79
79
79
79
79
80
81
80
80
81
81
80
80
80
80
82
DGM #2
Read
ft'
59.1
59.7
60.2
60.7
61.2
61.8
62.3
62.8
63.2
63.7
64.2
64.8
65.3
65.8
66.3
66.8
67.3
67.8
67.9
68.3
68.9
69.3
69.8
70.3
70.8
71.3
71.8
72.4
73.0
73.5
74.0
74.5
70.0
75.5
76.0
76.6
77.1
77.6
78.1
78.6
79.2
79.6
RC
Re;
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DGM
Temp
Inlet
°F
82
82
82
82
82
82
82
82
82
82
82
82
82
82
83
83
82
83
82
82
82
82
82
83
83
82
83
83
82
82
83
82
83
82
83
82
82
82
82
82
82
83
DGM
Temp
Outlet
op
82
82
82
82
82
82
82
82
82
82
82
82
82
82
83
82
82
82
82
82
82
82
82
82
82
83
83
83
83
82
82
82
82
82
82
82
82
82
82
82
82
83
Filter
Temp
op
81
80
90
90
90
89
89
90
90
90
90
87
90
90
90
90
90
90
79
79
78
78
79
78
78
78
79
79
79
75
79
79
79
79
79
79
79
79
79
79
79
80
Tunnel
Velocity
AP
in.HjO
.260
.255
.250
.255
.258
.260
.255
.255
.260
.265
.260
.260
.250
.260
.260
.258
.255
.250
.260
.260
.260
.255
.258
.260
.260
.260
.255
.260
.262
.262
.262
.257
.226
.230
.230
.225
.224
.228
.242
.231
.227
.223
Draft
in.H20
.013
.025
.038
.020
.015
.013
.028
.025
.018
.015
.013
.025
.033
.020
.015
.015
.030
.023
.015
.015
.013
.038
.020
.015
.015
.020
.038
.020
.016
.014
.010
.040
.026
.016
.012
.030
.043
.017
.015
.013
.028
.041
Water Temperature
Inlet
op
169
168
170
172
170
169
167
173
173
171
169
167
171
173
171
169
167
173
172
170
168
168
173
172
170
168
168
173
172
170
168
167
173
172
169
166
169
173
171
169
167
170
Outlet
op
180
178
181
183
181
179
178
185
184
182
180
178
182
184
182
180
178
183
183
181
179
178
184
183
181
179
179
184
183
181
179
178
184
183
180
178
180
184
182
180
178
181
-------
Furnace B Modified Method 5G Meter Box Data for Run 2
Date: fcSJune 1995
Elasped Weight
Time
Min.
840
850
860
870
872
Remain
Lb
01. 0
01. 0
01. 0
00.5
0
Flue Tunnel
Gas Temp
Temp °F
op
141 89
122 87
117 87
223 103
239 107
DGM#I ROTO 1
Read
ft'
706.0
706.6
707.1
707.7
707.8
Read
30
32
30
30
30
DGM
Temp
Inlet
°F
83
82
82
82
S2
DOM
Temp
Outlet
op
83
82
83
82
82
Filter
Temp
op
80
79
79
79
78
DGM #2 ROTO 2 DOM
Read
ft1
80.3
80.7
81.2
81.7
81.8
Read
30
30
30
30
30
Temp
Inlet
op
83
83
82
82
83
DGM
Temp
Outlet
op
83
82
8.3
82
82
Filter
Temp
°F
79
78
78
78
78
Tunnel
Velocity
AP
in.HjO
.229
.229
.230
.225
.225
Draft
in.H20
.019
.015
.014
.030
.034
Water Temperature
Inlet
°F
173
171
169
167
167
Oullet
op
184
182
180
178
178
w
-------
Furnace B Modified Method 5G Meter Box Data for Run 3
Date: 19 June 1995
m
K>
o
Elasped
Time
Min,
0
10
20
30
40
50
60
70
80
90
100
110
120
130
140
150
160
170
180
190
200
210
220
230
240
250
260
270
280
290
300
310
320
330
340
350
360
370
380
390
400
Weight
Remain
Lb
139.52
131.00
128.00
127.50
127.00
126.50
19.0
19.5
19.0
18.5
18.0
17.5
17.5
107.5
106.0
105.5
104.5
102.5
096.0
095.0
094.5
094.5
094.0
093.5
093.5
088.0
087.0
086.5
086.5
086.0
086.0
086.0
082.5
082.0
082.0
081.5
081.5
081.0
080.5
077.5
077.0
Rue
Gas
Temp
«p
116
234
175
133
125
154
163
138
129
124
121
120
144
228
142
132
126
256
15!
138
129
125
122
120
135
172
138
129
123
120
119
117
190
131
125
121
119
118
156
166
132
Tunnel
Temp
op
92
116
98
94
93
98
97
95
93
93
9.3
93
98
106
95
95
94
117
96
95
95
95
95
95
98
99
96
96
95
95
95
95
100
96
96
96
95
95
100
99
96
DGM#1
Read
ft'
707.8
708,4
708.9
708.5
710.0
710.5
711.0
711.5
712.0
712.6
713.1
713.6
714.1
714.6
715.1
715.6
716.1
716.6
717. i
717.6
718.1
718.6
719.2
719.7
720.2
720.7
721.2
721.7
722.2
722.7
723.3
723.8
724.3
724.8
725.4
725.9
726.5
727.0
727.5
728.0
728.6
ROTO 1
Read
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
.30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DOM
Temp
Inlet
op
83
84
84
84
85
85
86
87
84
83
82
82
82
82
82
82
82
81
82
82
82
82
82
82
82
82
82
83
83
83
83
83
83
83
83
83
83
83
83
83
83
DOM
Temp
Outlet
"F
82
83
83
84
84
85
85
86
84
83
83
82
82
82
82
82
82
82
82
82
82
82
82
82
82
83
83
83
83
82
83
83
83
83
83
83
83
83
83
83
83
Filter
Temp
°F
78
84
81
79
78
79
80
78
78
80
80
81
82
85
81
83
83
84
82
83
84
84
84
84
84
83
84
84
84
84
84
85
85
85
85
85
85
85
85
85
85
DGM
Read
ft'
82.3
82.9
83.4
83.9
84.4
84.9
85.5
86.0
86.5
870
87.5
88.0
88.6
89.1
89.6
90.1
90.6
91.1
91.5
92.0
92.5
93.0
93.5
94.0
94.5
95.0
95.5
96.0
96.5
97.1
97.6
98.2
98.7
99.2
99.8
100.3
100.9
101.4
101.9
102.4
102.9
Filter DGMf2 ROTO 2 DGM DGM Filter Tunnel Draft Water Temperature
Read Temp Temp Temp Velocity in.H20 Inlet Outlet
Inlet Outlet °F aP °F °F
30
30
30
.30
30
30
30
30
30
32
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
«F
80
81
82
83
84
84
84
85
83
83
83
83
83
83
83
83
83
82
82
82
83
83
83
83
83
83
84
84
83
83
84
84
84
84
84
84
84
84
84
84
84
80
80
81
82
82
82
83
84
84
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
8.3
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
79
83
82
79
79
80
81
79
80
80
8!
81
82
85
83
83
83
85
82
83
8.3
83
84
83
84
84
84
84
84
84
84
85
85
85
85
85
85
85
85
85
85
.257
.251
.210
.270
.257
.253
.258
.262
.259
.259
.257
.263
.256
.256
.256
.256
.257
.250
.257
.256
.257
.256
.259
.255
.255
.255
.255
.280
.250
.255
.255
.260
.260
.258
.258
.260
.258
.258
,255
.255
.260
.Oil
.010
.025
.019
.019
.021
.055
.021
.019
.017
.015
.015
.020
,029
.021
.019
.018
.040
.023
.020
.019
.016
.015
.015
.019
.013
.020
.018
.015
.015
.013
.018
.020
.018
.018
.015
.013
.013
.019
.023
.019
172
172
177
175
173
171
181
179
177
175
175
173
171
177
170
173
171
172
179
178
177
175
174
173
172
178
178
176
175
174
173
172
178
177
176
175
173
172
171
178
177
177
177
183
181
179
177
185
184
182
180
179
178
176
183
182
179
178
177
185
183
182
181
180
178
177
183
183
181
180
179
178
177
184
183
181
180
179
178
177
18.3
182
-------
Furnace B Modified Method 50 Meier Box Data for Run 3
Date: 19 June 199.1
m
Elasped Weight
Time Remain
Win, Lb
410
420
430
440
450
460
470
480
490
500
510
520
530
540
550
560
570
580
590
600
610
620
630
640
650
660
670
680
690
700
710
720
730
740
750
760
770
780
790
800
810
076,5
076.0
076.0
075.5
075.5
074.5
071.0
070.0
070.0
069.5
069.5
069.5
069.0
065.0
064.5
063.5
063.5
063.5
063.0
062.0
059.0
058.5
058.5
058.0
050.0
058.0
056.5
054.5
054.0
054.0
053.5
053.5
053.5
051.0
050.0
050.0
049.5
049.5
049.5
049.0
046.5
Flue
Gas
Temp
°F
126
122
119
117
116
206
151
130
124
120
118
115
149
21!
135
127
122
118
116
229
148
128
123
119
116
114
258
142
125
119
117
115
149
307
132
123
118
116
115
221
149
Tunnel
Temp
op
95
94
94
94
94
105
97
94
94
93
93
93
97
100
94
93
93
93
92
107
95
93
92
92
92
91
112
93
92
91
91
91
96
124
92
91
91
91
90
105
93
DGM#1
Read
ft'
729.1
729.6
730.1
730.7
731.2
731.7
723.3
732.8
733.4
733.9
734.5
735.0
735.6
736.1
736.7
737.3
737.8
738.4
739.0
739.6
740.1
740.6
741.2
741.7
742.3
742.9
743.4
744.0
744.5
745.1
745.6
746.2
746.7
747.3
747.8
748.4
748.9
749.5
750.1
750.6
751.6
ROTO 1
Read
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DGM
Temp
Inlet
oF
84
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
82
82
82
82
82
82
82
82
82
82
82
82
82
81
82
82
81
81
81
81
81
81
81
81
81
DGM
Temp
Outlet
°F
84
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
81
81
81
81
Filler DGM
Temp Read
85 103.5
85 104.0
85 104.5
85 105.1
85 105.6
.85 106.1
86 106.6
86 107.2
85 107.7
85 108.2
85 108.7
85 109.3
85 109.8
86
85
85
85
85
85
85
85
85
85
85
84
84
84
84
84
84
84
10.3
10.9
11.5
12.0
12.5
13.1
13.7
14.2
14.7
15.3
15.8
16.4
17.0
17.5
18.0
18.5
19.1
19.6
84 120.2
84 120.7
85 121.3
84 121.8
84 122.3
84 122.9
83 123.4
83 124.0
83 124.5
84 124.1
Filler DGM #2 ROTO 2 DGM DGM Filter Tunnel Draft Water Temperalure
Read Temp Temp Temp Velocity in.H20 Inlet Outlet
Inlet Gullet °F aP °F °F
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
85
84
84
84
84
84
84
84
84
84
84
84
84
84
84
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
82
82
83
83
83
83
82
82
82
82
85
84
85
85
84
84
84
84
84
84
84
84
84
84
84
84
84
84
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
82
83
83
85
85
85
85
85
85
85
85
85
85
85
85
85
85
85
85
84
84
84
84
84
84
84
84
84
84
83
84
84
84
83
83
83
84
84
83
83
83
83
83
83
in.H20
.260
.258
.256
.258
.258
.255
.258
.258
.260
.258
.260
.260
.258
.258
.262
.255
.256
.256
.255
.247
.255
.257
.258
.255
.257
.256
.252
.256
.257
.257
.257
.255
.255
.254
.257
.257
.257
.258
.256
.252
.257
.015
.015
.015
.013
.013
.030
.020
.018
.015
.015
.015
.013
.020
.023
.018
.015
.015
.013
.013
.031
.020
.016
.014
.012
.011
.Oil
.032
.019
.015
.013
.012
.016
.016
.040
.016
.014
.012
.011
.Oil
.025
.019
176
175
174
173
172
172
174
177
176
175
174
172
171
177
177
176
174
173
171
171
178
177
175
174
172
171
172
177
176
175
174
172
171
175
176
175
174
173
172
171
178
181
180
179
178
177
177
184
183
182
181
180
178
177
184
184
182
181
179
178
177
185
184
182
180
179
178
178
184
182
181
180
179
177
182
183
182
181
179
178
177
184
-------
Furnace B Modified Method 5O Meter Box Data for Run 3
Dale: 19 June 1995
m
to
to
Elasped
Time
Min.
820
830
840
850
860
870
880
890
900
910
920
930
940
950
960
970
980
990
1000
1010
1020
1030
1040
1050
1060
1070
1080
1090
100
110
120
130
140
150
160
170
180
190
1200
1210
1220
Weight
Remain
Lb
045.5
045.5
045.5
045.5
045.0
044.0
042.0
041.5
041.5
041.5
041.5
041.0
040.5
037.5
037.5
037.0
037.0
0.36.5
036.5
036.5
035.5
033.5
033.0
033.0
032.5
032.5
032.5
32.5
029.5
029.0
029.0
029.0
029.0
028.5
028.5
028.0
025.5
025.5
025.5
025.5
025.5
Flue
Gas
Temp
°F
126
120
116
115
115
231
151
125
119
116
114
114
207
177
127
120
117
115
1 1.3
113
243
143
12.3
IIS
114
11.3
112
143
194
126
119
115
113
112
HI
221
152
124
118
115
114
Tunnel
Temp
op
91
91
90
90
90
106
93
91
90
90
89
89
102
94
90
89
89
88
88
88
107
90
88
88
88
88
87
92
94
89
81
88
88
88
88
104
93
90
90
90
90
DGM#1
Read
ft'
751.7
752.3
752.9
753.4
754.0
754.5
755.0
755.5
756.1
756.7
757.3
757.8
758.3
758.8
759.3
759.8
700.4
760.9
761.4
763.0
762.5
763.1
76.3.6
764.2
764.7
765.2
765.8
766.4
766.8
767.4
767.9
768.5
769.0
769.5
770.1
770.6
771.1
771.7
772.2
772.7
773.3
ROTO 1
Read
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
.30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
.30
30
30
30
30
30
30
30
30
DGM
Temp
Inlet
«p
81
81
81
81
81
81
81
81
80
81
81
80
80
81
81
81
81
80
80
80
80
81
80
80
80
80
79
80
80
80
80
80
79
79
80
80
80
80
80
80
80
DGM
Temp
Outlet
°F
82
81
81
81
81
81
81
81
81
81
81
81
81
81
81
81
81
81
80
80
80
80
80
80
80
80
80
80
80
80
80
80
79
80
80
80
80
80
80
80
80
Filter
Temp
°F
84
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
82
82
82
82
82
82
82
81
81
81
81
81
81
81
81
81
80
81
80
81
81
81
81
81
81
DGM
Read
ft'
125.6
126.2
126.7
127.2
127.8
128.3
128.9
129.4
130.0
130.8
131.0
131.5
132.0
132.5
133.0
133.5
1 34.1
134.6
135.2
135.7
1 36.3
136.8
137.3
137.9
138.4
138.9
139.5
140.1
140.6
141.1
141.6
142.2
142.7
143.2
143.8
144.3
144.8
145.3
145.8
146.4
147.0
Filter DGM #2 ROTO 2 DGM DGM Filter Tunnel Draft Water Temperature
Read Temp Temp Temp Velocity in.H20 Inlet Outlet
Inlet Outlet "F aP °F "F
°F °F in.H,0
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
.30
30
30
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
81
81
81
XI
81
81
81
80
80
80
80
80
81
80
80
80
80
80
80
81
81
81
81
81
81
83
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
81
81
81
81
81
81
81
81
81
80
81
81
80
80
81
81
80
81
81
81
81
81
81
81
83
83
83
83
82
82
8.3
83
82
82
82
82
82
82
82
82
82
82
81
81
81
81
81
81
81
80
80
80
81
80
80
81
81
80
80
81
81
81
81
81
81
.255
.256
.257
.256
.258
.252
.257
.256
.258
.256
.257
.258
.262
.261
.263
.26.3
.268
.263
.263
.265
.258
.262
.264
.264
.262
.262
.262
.261
.262
.262
.262
.262
.261
.261
.260
.256
.259
.260
.259
.258
.259
.015
.013
.012
.011
.010
.027
.020
.015
.014
.012
.Oil
.010
.022
.020
.011
.014
.012
.011
.011
.011
.038
.017
.014
.013
.012
.012
.011
.018
.021
.015
.014
.012
.Oil
.010
.011
.031
.018
.016
.014
.014
.012
177
175
174
173
172
171
177
176
175
174
173
172
171
178
177
177
176
175
174
172
172
178
177
176
175
174
173
172
179
178
177
175
175
174
173
172
179
177
176
175
174
183
181
180
179
178
178
183
183
182
180
179
178
177
184
184
182
181
180
179
178
177
184
183
182
180
179
179
177
185
184
18.3
181
181
179
178
178
185
184
182
1RI
180
-------
Furnace B Modified Method 5G Meter Box Data for Run 3
Dale: 19 June 1995
M
K>
OJ
Klasped
Time
Min.
1230
1240
1250
1260
1270
1280
1290
1300
1310
1320
1330
1.340
1 350
1360
1370
1380
1390
1400
1410
1420
14.30
1440
1450
1460
1470
1480
1490
1500
1510
1520
1530
1 540
1550
1560
1570
1580
1 590
1600
1610
1620
1630
Weight
Remain
Lh
025.5
025.0
022.5
022,0
022.0
021,5
021.5
021.5
021.5
020.0
018.5
018.5
018.0
018.0
018.0
017.5
017.5
016.5
014.5
014.5
014.5
014.5
014.0
014.0
014.0
013.5
011.5
011.0
011.0
011.0
011.0
01 1.0
011.0
OII.O
01 0.0
008.5
008.5
008.5
008.5
008.0
008.0
Hue
Gas
Temp
113
159
194
128
120
117
116
115
115
250
146
125
120
118
117
117
116
220
158
127
122
119
118
118
115
194
244
132
123
121
119
119
118
139
267
147
127
123
121
119
118
Tunnel
Temp
op
90
97
97
92
92
92
92
92
92
112
95
93
9.3
93
93
93
94
109
97
95
95
95
94
95
95
108
104
%
95
95
95
96
96
99
88
98
97
97
96
96
96
DGM#1
Read
ft1
773.8
774.4
774.9
775.4
778.0
776.5
777.0
777.6
778.1
778.6
779.2
779.7
780.2
780.7
781.3
781.8
782.4
782.9
783.4
783.9
784.5
785. 1
785.6
786.1
786.6
787.1
787.6
788.2
788.8
789.3
789.8
790.3
790.8
791.4
791.8
792.2
792.9
793.5
744.0
794.5
795.1
ROTO 1
Read
30
30
.30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
.30
30
DGM
Temp
Inlet
80
80
81
81
81
81
81
81
81
81
81
82
82
SI
82
81
82
82
82
82
82
83
83
82
8.3
83
83
83
83
83
84
84
85
86
86
86
86
86
85
84
84
DGM
Temp
Outlel
80
80
80
80
80
81
81
80
81
81
81
81
81
81
82
81
82
82
82
82
82
82
82
83
83
83
83
83
83
83
84
84
85
86
86
86
86
86
85
85
84
Filter
Temp
op
81
81
82
82
82
82
82
82
82
83
83
82
83
83
83
83
83
83
84
84
83
84
84
84
84
84
85
85
84
84
83
83
83
82
83
84
84
84
84
85
85
DGM
Read
ft1
147.5
148.0
148.5
149.0
149.5
150.1
150.6
151. 1
151.7
152,2
152.7
153.2
153.7
154.3
154.8
155.3
155.8
156.4
156.9
157.4
157.9
158.5
159,0
159.5
160.1
160.6
161.0
161.6
162,1
162.6
163.2
163.7
664.2
164.7
165.2
165.7
166,3
166,8
167.4
167.9
168.4
Filter DGM #2 ROTO 2 DGM DGM Filter Tunnel Draft Water Temperature
Read Temp Temp Temp Velocity in.H,0 Inlet Outlet
Inlet Outlet °F aP °F °F
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
81
81
81
81
81
81
81
82
82
82
82
82
82
82
82
82
82
83
83
8.3
83
83
83
83
83
84
84
84
84
85
85
86
87
87
87
87
87
85
84
84
81
81
82
81
81
81
81
81
82
82
82
82
82
82
82
82
82
82
82
83
83
83
83
84
84
83
84
84
84
84
84
85
85
85
86
86
87
87
85
85
84
81
81
81
81
82
82
82
82
82
82
83
82
82
82
83
83
83
83
83
83
83
84
84
84
84
84
84
84
84
83
82
82
81
81
82
83
8.3
84
84
84
85
in.HjO
.258
.256
.256
.258
.257
.259
.260
.256
.256
.251
.256
.255
.255
.254
.260
.255
.255
.250
.256
.255
.258
,255
.257
.253
.254
.254
.253
.253
.255
.254
.255
.254
.254
.256
.250
.256
.255
.256
.255
.256
.255
.Oil
.021
.019
.015
.014
.012
.012
.Oil
.Oil
.034
.018
.015
.013
.012
.012
.Oil
.010
.0.31
.020
.015
.014
.013
.012
.010
.Oil
.023
.021
.015
.014
.013
.011
.01!
.016
.016
.039
.019
.015
.014
.013
.013
.Oil
172
171
178
177
176
175
174
173
172
173
178
177
176
175
174
173
171
172
178
177
176
176
174
173
172
171
177
177
176
175
174
174
172
171
173
177
177
176
175
174
173
178
177
184
183
IS!
180
179
179
178
179
184
183
182
181
180
178
177
178
184
183
182
181
180
179
177
177
183
183
182
181
180
179
178
176
178
183
182
181
180
179
178
-------
l-'urnace B Modified Method 5G Meier Box Data for Run 3
Date: 19 June 1995
m
to
Elasped
Time
Min.
1640
1650
1660
1670
1680
1690
1700
1710
1720
1730
1740
1750
1760
1770
1780
1790
1800
1810
1820
1830
1833
Weight
Remain
Lb
008.0
007.5
005.5
005.5
005.5
005.5
005.5
005.5
005.0
005.0
003.5
002.5
002.5
002.5
002.5
002.5
002.5
002.5
001.5
000.5
000.0
Flue
Gas
Temp
°F
118
207
202
131
125
122
120
119
119
173
241
144
126
122
121
120
119
153
206
229
197
Tunnel
Temp
°F
96
109
103
98
97
97
97
97
97
104
116
99
98
97
98
98
97
102
109
114
103
DGM#I
Read
ft1
795.6
796.1
796.6
797.1
797.7
798.2
798.8
799.3
799.9
800.4
800.9
801.5
802.2
802.5
803.1
803.7
804.2
804.7
805.2
805.7
805.8
ROTO 1
Read
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DGM
Temp
Inlet
= p
84
84
84
84
84
83
83
83
84
83
84
84
84
85
85
86
87
87
88
88
87
DGM
Temp
Outlet
°F
84
84
84
83
83
83
83
84
83
83
83
84
83
84
85
86
86
87
87
87
87
Filter
Temp
°F
85
86
86
86
86
86
86
86
86
87
87
87
87
86
85
85
84
84
84
84
84
DGM
Read
ft1
169.0
169.5
170.0
170.5
171.0
171.5
172.1
172.6
173.2
173.7
174.2
174.7
175.3
175.8
176.4
177.0
177.5
178.0
178.5
178.0
179.0
Filler DGM #2 ROTO 2 DGM DGM Filter Tunnel Draft Water Temperature
Read Temp Temp Temp Velocity in.H;0 Inlet Outlet
Inlet Outlet °F A? °F °F
°F °F in.HjO
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
84
83
83
83
83
83
83
83
83
83
83
83
83
84
86
87
88
88
88
88
88
84
84
84
84
83
83
83
84
84
84
84
84
84
84
86
86
87
88
88
88
88
85
85
86
86
86
86
86
86
86
86
86
87
87
85
85
84
84
84
84
84
84
.255
.250
.252
.254
.255
.253
.252
.255
.256
.253
.251
.255
.257
.256
.256
.255
.256
.256
.253
.253
.255
.Oil
.029
.020
.018
.015
.012
.013
.Oil
.Oil
.020
.030
.016
.015
.013
.012
.Oil
.Oil
.018
.026
.030
.020
172
171
177
177
176
175
174
173
171
171
173
177
176
175
174
173
172
171
172
175
178
177
176
183
182
181
180
179
178
177
176
179
183
181
181
179
179
177
176
177
180
182
-------
Furnace B Modified Method 5G Meter Box Data for Run 4
Date: tt June 1995
tn
K)
Elasped
Time
Min.
0
10
20
30
40
50
60
70
80
90
100
110
120
130
140
150
160
170
180
190
200
210
220
230
240
250
260
270
280
290
300
310
320
330
340
350
360
370
380
390
400
410
Weight
Remain
Lh
136.86
127.00
126.50
126.50
1 19.50
113.50
113.00
109.50
102.00
101.00
100.50
092.00
090.50
090.00
089.00
083.50
082.50
082.00
081,00
077.50
077.00
076.50
075.50
073.00
072.50
072.00
070.50
068.00
067.50
067.50
064.50
064.00
063.50
063.00
060.00
059.50
050.00
058.50
055.50
054.50
054.50
054.00
Flue
Gas
Temp
°F
133
221
136
128
304
150
136
292
153
138
148
216
146
135
165
164
140
130
188
160
134
126
222
156
133
126
260
146
132
126
311
138
129
163
212
136
128
166
207
137
128
160
Tunnel
Temp
°F
91
100
92
91
134
93
92
127
94
93
99
102
93
43
100
96
93
43
102
96
94
93
107
%
94
94
113
%
95
94
112
%
95
101
102
96
96
101
102
97
96
102
DGM#I
Read
ft1
806.0
806.6
806.1
807,6
808.2
808.7
809.2
809.8
810.3
810.8
811.4
811.9
812.4
813.0
813.5
814.0
814.6
815.1
815,7
816.2
816.8
817.3
817.9
818.4
819.0
819,5
820.0
820.6
821,2
821.7
822.3
822.9
823.4
823.9
824.5
825.0
825.6
826.1
826.7
827.3
827,8
825,3
ROTO 1
Read
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DGM
Temp
Inlet
oF
78
78
77
76
75
75
76
77
78
79
77
76
76
76
76
76
76
76
76
76
76
76
77
77
77
77
77
77
77
77
77
77
81
82
83
84
85
81
80
80
79
79
DGM
Temp
Outlet
°F
78
78
78
77
76
76
76
76
77
78
78
77
77
77
77
76
76
77
77
76
76
77
77
77
77
77
77
77
77
77
78
78
79
81
82
83
84
83
82
81
80
79
Filter
Temp
"F
74
79
77
76
85
78
77
80
77
76
77
78
76
76
77
77
77
78
78
78
78
78
78
79
79
79
79
79
79
79
80
79
80
81
81
82
82
81
81
82
82
82
DGM #2
Read
ft'
179.1
179.6
180.2
180.7
181.2
181.7
182.2
182.8
183.3
183.8
184.3
184.9
185.4
185.9
186.5
187.0
187.5
188.0
188.5
189.0
189.6
190.1
190.6
191.1
191.7
192.2
192.7
193.3
193.8
194.3
194.9
195.5
196.0
196.5
197.1
197.6
198.1
198.6
199.1
199.7
200.2
200.8
RO1
Reac
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DGM
remp
Inlet
°F
78
78
77
77
76
76
76
77
78
78
78
78
78
78
78
78
78
78
78
78
78
78
79
79
79
79
79
79
79
79
80
80
81
82
82
83
84
82
81
81
81
80
DGM
Temp
Outlet
°F
78
78
78
77
77
76
76
77
77
78
78
78
78
78
78
78
78
79
78
78
78
79
79
79
79
79
79
79
80
80
80
80
80
81
81
82
83
83
82
82
81
81
Filter
Temp
»p
76
79
77
76
85
78
77
81
77
76
78
79
77
77
78
78
78
78
78
78
78
78
78
79
79
79
79
80
79
79
81
80
81
81
82
83
83
82
82
82
82
82
Tunnel
Velocity
aP
in.HjO
.262
.257
.258
,259
.248
.257
.258
.248
.261
,251
.252
.255
.258
.260
.258
.255
.257
.256
.254
.258
.258
.257
.256
.259
.260
.263
.259
.258
.262
.259
.257
.261
,260
.257
.264
.260
.261
.260
.257
.267
.260
.256
Draft
in.HjO
.015
.026
.020
.016
.048
.023
.020
.049
.025
.021
.025
,029
.020
.020
.024
.024
.020
.019
.024
,020
.018
.016
.029
.030
.016
.015
.034
.019
.016
.015
.022
.018
.015
.020
.022
.019
.016
.021
.022
.019
.015
.020
Water Temperature
Inlel
°F
170
173
171
169
168
171
168
167
172
169
168
173
171
170
167
173
171
169
167
173
170
168
167
172
170
168
168
172
169
167
173
171
169
167
173
171
169
167
173
171
169
167
Outlet
°p
179
183
ISI
178
180
182
178
179
183
180
178
184
182
ISO
177
184
1S1
179
177
183
180
178
177
183
180
178
179
183
180
177
183
182
179
177
184
181
179
177
184
181
179
177
-------
Furnace B Modified Method 5G Meier Box Data for Run 4
Dale: I»June 1995
w
Elasped
Time
Min.
420
430
440
450
460
470
480
490
500
510
520
530
540
550
560
570
580
590
600
610
620
630
640
650
560
670
680
690
700
710
720
730
740
750
760
770
780
790
800
810
820
830
Weight
Remain
Lb
051.50
050.50
050.00
050.0
049.00
046.50
046.00
046.0
046,0
045.0
042.0
041.5
041.5
041.0
040.5
037.0
035.0
035.0
034.5
034.5
033.5
030.0
030.0
029.5
029.5
029.0
026.0
025.0
024.5
024.5
024.5
023.0
021.0
020.5
020,5
020.5
020.5
019.0
017.0
016.5
016.5
016.5
Hue
Gas
Temp
op
300
143
130
125
221
191
132
129
124
235
2.31
140
130
126
206
321
150
135
122
123
251
184
139
129
124
218
360
146
132
125
122
255
184
1.36
127
122
194
300
163
133
126
122
Tunnel
Temp
°F
125
98
97
97
110
102
98
98
98
113
107
100
99
99
109
1.34
100
100
99
98
117
103
99
99
98
lit
142
100
98
97
97
116
101
97
%
95
105
125
99
97
96
95
DGM#I
Read
ft1
828.9
829.5
830.0
830.5
831.1
831.6
832.2
832.7
833.2
833.8
834.3
834.9
835.4
836.0
836.5
837.1
837.6
838.2
838.7
839.3
839.8
840,4
840.9
841.5
842.0
842,5
843.1
843.6
844.2
844.7
845.3
845.8
846.4
846.9
847.5
848.0
848.5
949.1
849.7
850.2
850.8
851.3
ROTO I
Read
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DGM
Temp
Inlet
°F
80
82
81
84
86
85
86
87
88
86
85
82
84
83
82
82
83
83
83
83
83
8.3
83
83
83
83
82
82
82
82
82
83
82
82
83
83
83
83
82
83
82
82
DGM
Temp
Outlet
op
80
81
81
82
84
84
85
85
86
86
86
84
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
83
82
83
83
83
83
83
83
83
83
83
83
83
83
Temp Read Read
°F n3
83
84
83
83
84
84
84
84
84
85
85
84
84
84
84
85
84
84
83
83
84
84
83
83
83
83
84
83
83
83
83
84
84
83
83
83
83
84
84
84
83
83
201.3
201.8
202.3
202.8
203.3
203.9
204.4
204.9
205.5
206.0
206.5
207.0
207.6
208.1
208.6
209.2
209.7
210.2
210.7
211.3
211.8
212.4
212.9
213,4
213.9
214.5
215.0
215.5
216.0
216.6
217.1
217.6
218.2
218,7
219.2
219,7
220.3
220.8
221,4
221.9
222.4
222.9
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DGM
Femp
Inlet
op
81
82
82
84
84
84
85
85
86
85
85
83
84
83
83
84
85
85
85
85
85
85
85
85
85
85
84
84
84
83
84
84
84
84
83
84
84
84
84
84
84
84
DGM
Temp
Outlet
°F
81
82
82
83
83
84
84
84
85
85
85
84
84
84
83
84
84
84
85
85
85
85
85
85
85
85
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
Filter
Temp
«p
83
82
82
83
83
83
83
83
83
84
85
84
84
84
84
86
85
84
84
84
85
85
85
84
84
84
85
84
84
84
84
84
84
84
83
84
84
85
84
84
84
84
Tunnel
Velocity
&P
in,H20
.255
.259
.257
.258
.255
.260
.255
.255
.255
.252
.250
.256
.260
.260
.245
.243
.250
.250
.250
.250
.248
.248
.255
.253
.250
.250
.248
.252
.250
.252
.253
.248
.250
.253
.253
.250
.250
.245
.253
.253
.254
.255
Draft
in.H20
.042
.020
.016
.015
.030
.025
.018
.016
.015
.035
.025
.020
.018
.015
.028
.048
.020
.018
.015
.015
.033
.023
.020
.015
.015
.029
.030
.020
.018
.015
.013
.035
.023
.018
.015
.013
.025
.033
,021
.017
.015
.012
Water Temperature
Inlet
op
179
172
179
169
168
174
172
171
168
168
173
171
170
169
167
172
173
172
170
168
167
174
171
170
168
167
172
172
171
169
167
167
173
171
170
168
166
169
173
173
171
169
Outlet
op
180
182
180
178
176
183
181
179
178
176
182
181
180
178
176
181
183
181
179
177
177
184
182
180
178
176
182
183
180
179
177
176
183
182
180
178
176
179
183
182
180
178
-------
Furnace B Modified Method 5G Meter Box Data for Run 4
Date: KS June 1995
Rlasped Weight Flue Tunnel DGM#IROTOI DGM
Time Remain Gas Temp Read Read Temp
Min. Lb Temp °F ft' Inlet
op op
tn
to
840
850
860
870
880
890
900
910
920
930
940
950
960
970
980
990
1000
1010
1020
1030
1040
1050
1060
1063
016.5
015.0
012.5
012.5
012.0
012.0
011.5
010.0
008.5
008.0
008.0
008.0
007.5
005.5
004.5
004.5
004.5
004.0
002.5
001.0
001.0
001.0
000.5
000.0
173
272
177
135
128
122
178
283
180
135
125
120
239
301
152
130
123
205
294
177
132
123
177
213
102
118
99
96
95
94
101
119
98
95
94
93
110
124
95
93
93
104
120
96
9.3
92
100
105
851.8
852.4
852.9
853.4
854.0
854.5
855.0
855.5
856,1
856.6
857.2
857.7
858.2
858.8
859.3
859.8
860.4
860.9
861,4
862.0
862.5
863.0
86,3.6
863.7
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
82
82
82
82
82
82
84
85
87
88
88
84
82
82
81
81
80
81
80
80
81
8i
82
81
DGM
Temp
Outlet
°F
83
82
82
82
82
82
83
84
85
87
86
85
83
82
82
81
81
81
81
80
81
81
81
80
83
83
84
83
82
82
82
83
83
84
82
82
82
83
82
82
82
82
82
82
82
81
81
81
223.5
224.0
224.5
225.1
225.6
226.1
226.6
227.1
227.7
228.2
228.7
229.3
229.8
230.3
230.8
231.4
231.9
232.4
232.9
233.5
234.0
234.5
235.0
235.2
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
30
DGM
Temp
Intel
°F
84
83
83
83
83
83
84 '
85
86
88
87
84
83
83
82
82
82
82
82
81
82
82
82
82
DGM
Temp
Outlet
»p
84
83
8.3
84
83
83
82
84
85
87
86
85
84
83
83
83
82
82
82
82
82
82
82
81
Filter
Temp
op
84
84
84
83
83
83
82
83
84
84
83
82
82
82
82
82
82
82
83
82
81
81
81
80
Tunnel
Velocity
aP
in.HjO
.252
.249
.253
.256
.256
.262
.261
.257
.262
.259
.259
.261
.256
.255
.261
.260
.265
.260
.258
.260
.262
.261
.259
.255
Draft
in.HjO
.020
.031
.024
.017
.014
.014
.022
.039
.032
.018
.016
.014
.042
.040
.020
.016
.015
.028
.040
.021
.016
.015
.023
.029
Water Temperature
Inlet
op
167
167
173
173
171
168
166
167
173
172
169
167
166
169
172
170
168
166
168
172
170
169
166
166
Outlet
op
176
177
184
182
180
179
176
178
183
182
ISO
177
177
180
183
181
179
176
179
183
181
179
177
176
-------
Appendix F - Method 5G Summary Data
Fl
-------
WOODSTOVE TEST INFORMATION
NAME: Russell Logan and Joey Valenti
DATE: 06/15/95
TEST No.:TD-MM5G-2A
DESCRIPTION: Modified Method 5G Testing of Furnace A @ High Heat Removal Rate
CONDITIONS
Ambient Temp.:
Barometric Press.:
Humidity:
FUEL INFORMATION
TYPE:
CHARGE WEIGHT:
MOISTURE:
HEATING VALUE:
66.09 F
30.02 in Hg
29.89 %
Red Oak
82.50 Ibs
29.03 %
8069.0 Btu/ dry Ibs of fuel
PRELIMINARY VELOCITY TRAVERSE
Dist (in)
0.4
1.5
4.5
5.6
Temp (F)
0.125 81
0.135 81
0.140 81
0.126 81
GENERAL
Pre-Test Leak:
Post-Test Leak:
Total Time:
AVERAGE HEAT OUTPUT
0.13 cfm
0.163 cfm
424 min
43,338 Btu/hr
MM5G WEIGHTS (grams)
FILTER A
FINAL: 0.7688
TARE: 0.6194
NET: 0.1494
CEM VALUES
PRE-TEST
ZERO SPAN
O2: 0.00 9.70
CO2: 0.00 6.48
CO: 6.10 20058.00
COdilu: 2.10 2006.50
JUM-THC: out of service
FILTER B
FINAL: 0.6236
TARE: 0.6231
NET: 0.0005
POST-TEST
ZERO SPAN
0.00 9.70
-0.10 6.50
8.40 20002.00
1.30 2006.50
PAN RINSE
FINAL: 2.6529
TARE: 2.6438
NET: 0.0091
ACTUAL SPAN
9.70 %
6.50 %
20100.00 ppm
2070.00 ppm
TIME:
O2:
CO2:
CO:
CO dilu:
RESULTS
0.672222222222
13.34 %
9.20 %
18888 ppm
2006.5 ppm
TIME:
O2:
CO2:
CO:
CO dilu:
0.81806
14.92 %
5.68 %
9542 ppm
1331.4 ppm
O2:
CO2:
CO:
CO dilu:
JUM-THC:
AVERAGES
14.34 %
6.33 %
11413.6 ppm
1393.73 ppm
n/a
Flow:
Fire rate:
Particulate:
EFFICIENCY:
TOTAL
TOTAL
(output/input)
146 cfm
4.104 dry kg/hr
35.10 g/hr
8.55 g/dry kg of fuel
0.48 mg/Btu
303,944 Btu output
516,041 Btu input
58.90%
F2
-------
TESTNo,:TD-MM5G-2B
DESCRIPTION: Modified Method 5G Testing of Furnace A @ High Heat Removal Rate
NAME:
DATE:
TEST No.:
DESCRIPTION:
CONDITIONS
Ambient Temp.:
Barometric Press.:
Russell Logan and Joey Valenti
34869
TD-MM5G-2A
Modified Method 5G Testing of Furnace A @ High Heat Removal Rate
67.62
30.00
F
inHg
Humidity: 29.89 %
FUEL INFORMATION
TYPE:
CHARGE WEIGHT
MOISTURE:
HEATING VALUE:
Red Oak
83.50 Ibs
25.14 %
8069.0 Btu7 dry Ibs of fuel
PRELIMINARY VELOCITY TRAVERSE
Dist(in)
0.4
1.5
4.5
5.6
Temp (F)
0.100
0.140
0.140
0.120
73
74
74
73
AVERAGE H
MM5G WEIGHTS (grams)
CEM VALUES
02:
CO2:
CO:
CO dilu:
JUM-THC: out
TIME: 0
O2:
CO2:
CO.
CO dilu:
FILTER A
FINAL:
TARE:
NET:
PRE-TEST
ZERO
-0.09
0.00
0.00
2.40
of service
.67708333333
17.44
3.54
4114
1694.3
0.7165
0.6258
0.0907
SPAN
9.71
6.48
19902.00
2006.80
%
%
ppm
ppm
TIME:
O2:
CO2:
CO:
CO dilu:
FILTER B
FINAL: 0.6300
TARE: 0.629
NET: 0.0010
POST-TEST
ZERO SPAN
-0.06 9.70
0.00 6.56
6.10 19880.00
1.20 2005.10
0.802083
12.02 %
8.26 %
9941 ppm
901.5 ppm
GENERAL
Pre-Test Leak:
Post-Test Leak:
Total Time:
0.04 cfm
0.035 cfm
457 min
40,822 Btu/hr
PAN RINSE
FINAL:
TARE:
NET:
2.6135
2.5974
0.0161
ACTUAL SPAN
9.70 %
6.50 %
20100.00 ppm
2070.00 ppm
O2:
CO2:
CO:
CO dilu:
JUM-THC:
AVERAGES
15.59 %
5.16 %
6248.54 ppm
1301.4 ppm
n/a
RESULTS
Flow:
Fire rate:
Partculate:
EFFICIENCY:
TOTAL
TOTAL
(output/input)
146 cfm
3.97 drykg/hr
49.90 g/hr
12.56 g/dry kg of fuel
0.71 mg/Btu
313,424 Btu output
538,406 Btu input
58.21%
F3
-------
NAME: Russell Logan and Joey Valenti
DATE: 06/27/95
TESTNo.:TD-MM5G-2C
DESCRIPTION: Modified Method 5G Testing of Furnace A @ High Heat Removal Rate
CONDITIONS
Ambient Temp.: 80.63
Barometric Press.: 30.03
Humidity: 84
FUEL INFORMATION
TYPE: Red Oak
CHARGE WEIGHT 87.0
MOISTURE: 23.90
HEATING VALUE: 8069.0
PRELIMINARY VELOCITY TRAVERSE
Dist (in)
0.4 0.145
1.5 0.145
4.5 0.140
5.6 0.125
MM5G WEIGHTS (grams)
FILTER A
FINAL:
TARE:
NET:
0.7640
0.6269
0.1371
F
inHg
%
Ibs
%
Btu/ dry Ibs of fuel
GENERAL
Temp (F)
77
77
77 AVERAGE h
77
FILTER B
FINAL:
TARE:
NET:
0.6305
0.6298
0.0007
GEM VALUES
O2:
CO2:
CO:
CO dilu:
JUM-THC:
TIME:
02:
CO2:
CO:
CO dilu:
RESULTS
PRE-TEST
ZERO
-0.27
-0.02
57.00
0.00
out of service
0.65277777778
7.57
12.00
14221
1064
Flow.
Fire rate:
Particulate:
EFFICIENCY:
TOTAL
TOTAL
(output/input)
POST-TEST
SPAN
9.56
6.80
39034.00
2004.60
%
%
ppm
Ppm
243
5.81
143.20
24.65
1.39
219,936
566,588
38.82%
ZERO
-0.03
0.02
57.00
4.20
TIME: 0.6875
02: 11.08
CO2: 9.00
CO: 25330
CO dilu: 1948
cfm
dry kg/hr
g/hr
g/dry kg of fuel
mg/Btu
Btu output
Btu input
SPAN
9.72
6.43
38606.80
2004.70
%
%
ppm
ppm
Pre-Test Leak:
Post-Test Leak:
Total Time:
0.008 cfm
0.009 cfm
329 min
40,347 Btu/hr
PAN RINSE
FINAL: 2.6365
TARE: 2.6226
NET: 0.0139
ACTUAL SPAN
9.70 %
6.50 %
40000.00 ppm
2070.00 ppm
02:
CO2:
CO:
CO dilu:
JUM-THC:
AVERAGES
9.552 %
10.305 %
17906.6 ppm
1224.325 ppm
n/a
F4
-------
WOODSTOVE TEST INFORMATION
NAME: Russell Logan and Joey Valenti
DATE: 06/30/95
TESTNo.:TD-MM5G-2D
DESCRIPTION: Modified Method 5G Testing of Furnace A @ High Heat Removal Rate
CONDITIONS
Ambient Temp.:
Barometric Press.:
Humidity:
FUEL INFORMATION
TYPE:
CHARGE WEIGHT
MOISTURE:
HEATING VALUE:
73.28 F
30.03 in Hg
84 %
Red Oak
81.2 ibs
22.14 %
8069.0 Btu/dry Ibs of fuel
PRELIMINARY VELOCITY TRAVERSE
Dist (in)
0.4
1.5
Temp (F)
0.115 85
0.135 85
4.5 0.135
5.6 0.125
MM5G WEIGHTS (grams)
FILTER A
FINAL: 0.7296
TARE: 0.6338
NET: 0.0958
84
84
GENERAL
Pre-Test Leak:
Post-Test Leak:
Total Time:
AVERAGE HEAT OUTPUT:
0.01 cfm
0,005 cfm
438 min
38,983 Btu/hr
FILTER B
FINAL:
TARE:
NET:
0.6348
0.6353
-0.0005
PAN RINSE
FINAL:
TARE:
NET:
2.6479
2.6408
0.0071
CEM VALUES
02:
C02:
CO:
CO dilu:
PRE-TEST
ZERO
-0.08
0.00
92.80
2.60
JUM-THC: out of service
SPAN
9.70
6.40
39383.90
2006.30
TIME: 0.49305555556
O2: 7.84 %
CO2: 12.50 %
CO: 24902 ppm
CO dilu; 1665 ppm
POST-TEST
ZERO
0.00
0.01
105.80
3.60
SPAN
9.44
6.41
39253.70
2005.40
TIME: 0.581944
O2: 9.28 %
CO2: 10.64 %
CO: 15381 ppm
CO dilu: 1016 ppm
ACTUAL SPAN
9.70 %
6.50 %
40000.00 ppm
2070.00 ppm
02:
CO2:
CO:
CO dilu:
JUM-THC:
AVERAGES
9.699 %
10.423 %
24386.4 ppm
1340.21 ppm
n/a
RESULTS
Flow:
Fire rate:
Particulate:
EFFICIENCY:
TOTAL
TOTAL
(output/input)
241 cfm
4.13 drykg/hr
61.00 g/hr
14.77 g/drykgoffuel
0.83 mg/Btu
288,354 Btu output
536,436 Btu input
53.38%
F5
-------
WOODSTOVE TEST INFORMATION
NAME: Russell Logan and Joey Valerrti
DATE: 06/28/95
TESTNo.:TD-MM5G-1A
DESCRIPTION: Modified Method 5G Testing of Furnace A @ Low Heat Removal Rate
CONDITIONS
Ambient Temp.: 73.38
Barometric Press.: 30.09
Humidity: 75
FUEL INFORMATION
TYPE: Red Oak
CHARGE WEIGHT 80.5
MOISTURE: 21.76
HEATING VALUE: 8069.0
PRELIMINARY VELOCITY TRAVERSE
Dist (in)
0.4
1.5
4.5
5.6
0.100
0.135
0.145
0.125
F
in Hg
Ibs
Btu/ dry Ibs of fuel
Temp (F)
85
86
87
87
GENERAL
AVERAGE h
MM5G WEIGHTS (grams)
CEM VALUES
02:
CO2:
CO:
CO dilu:
JUM-THC: out
TIME: 0
O2:
CO2:
CO:
CO dilu:
RESULTS
FILTER A
FINAL:
TARE:
NET:
PRE-TEST
ZERO
-0,26
0.00
36.60
1.60
of service
.57638888889
5.83
14.48
29236
2002
Flow:
Fire rate:
Particulate:
EFFICIENCY:
TOTAL
TOTAL
(output/input)
0.7305
0.628
0.1025
FILTER B
FINAL:
TARE:
NET:
0,6281
0.6291
-0.0010
POST-TEST
SPAN
9.20
6.44
39172.40
2005.20
%
%
ppm
ppm
231
2.44
38.50
15.79
0.89
247,498
533,471
46.39%
ZERO
0.38
0.02
85.40
2.00
TIME: 0.654167
02: 10.5
CO2: 8.54
CO: 9521
COdilu: 112
cfm
dry kg/hr
g/hr
g/drykgoffuel
mg/Btu
Btu output
Btu input
SPAN
8.38
6.46
39152.00
2003.70
%
%
ppm
ppm
Pre-Test Leak:
Post-Test Leak:
Total Time:
0.005 cfm
0.005 cfm
738 min
19,936 Btu/hr
PAN RINSE
FINAL:
TARE:
NET:
2.6461
2.6388
0.0073
ACTUAL SPAN
9.70 %
6.SO %
40000.00 ppm
2070.00 ppm
O2:
CO2:
CO:
CO ditu:
JUM-THC:
AVERAGES
10.92 %
8.74 %
14458.1 ppm
755.19 ppm
n/a
F6
-------
WOODSTOVE TEST INFORMATION
NAME: Russell Logan and Joey Valenti
DATE: 06/29/95
TESTNo.:TD-MM5G-1B
DESCRIPTION: Modified Method 5G Testing of Furnace @ Low Heat Removal Rate
CONDITIONS
Ambient Temp.:
Barometric Press.:
Humidity:
FUEL INFORMATION
TYPE:
CHARGE WEIGHT
MOISTURE:
HEATING VALUE:
71.82 F
30.08 in Hg
82 %
Red Oak
83.0 Ibs
20.40 %
8069.0 Btu/dry Ibs of fuel
PRELIMINARY VELOCITY TRAVERSE
Dist (in)
0.4
1.5
4.5
5.6
Temp (F)
0.110
0.137
0.135
0.117
85
84
84
82
AVERAGE h
MM5G WEIGHTS (grams)
CEM VALUES
O2:
CO2:
CO:
CO dilu:
FILTER A
FINAL:
TARE:
NET:
PRE-TEST
ZERO
-0.19
0.00
93.60
1.80
0.7344
0.6293
0.1051
SPAN
10.32
6.45
39278.20
2005.50
FILTER B
FINAL: 0.6327
TARE: 0.6328
NET: -0.0001
POST-TEST
ZERO SPAN
0.15 10.87
0.00 6.40
69.20 39160.20
4.40 2005.00
JUM-THC: out of service
TIME: 0
02:
CO2:
CO:
CO dilu:
.65416666667
9.12
11.28
31006
562
%
%
ppm
ppm
TIME:
O2:
C02:
CO:
CO dilu:
0.85625
9.61 %
9.23 %
11719 ppm
110 ppm
GENERAL
Pre-Test Leak:
Post-Test Leak:
Total Time:
0.005 cfm
0.005 cfm
655 min
21,138 Btu/hr
PAN RINSE
FINAL:
TARE:
NET:
2.6574
2.6508
0.0066
ACTUAL SPAN
9.70 %
6.50 %
40000.00 ppm
2070.00 ppm
O2:
CO2:
CO:
CO dilu:
JUM-THC:
AVERAGES
9.92 %
9.608 %
17524.6 ppm
839.26 ppm
n/a
RESULTS
Flow:
Fire rate:
Particulate:
EFFICIENCY:
TOTAL
TOTAL
(output/input)
238 cfm
2.86 dry kg/hr
48.60 g/hr
16.97 g/drykgoffuel
0.95 mg/Btu
236,067 Btu output
556,252 Btu input
42.44%
F7
-------
WOODSTOVE TEST INFORMATION
NAME: Russell Logan and Joey Vaienti
DATE: 10/24/95
TESTNo.:TD-MM5G-2
DESCRIPTION: Modified Method 5G Testing of Furnace A with Catalyst @ High Heat Output
CONDITIONS
Ambient Temp.:
Barometric Press.:
Humidity:
67.94
30.21
74
F
inHg
%
FUEL INFORMATION
TYPE:
CHARGE WEIGHT
MOISTURE:
HEATING VALUE:
Red Oak
84.0
21.74
8069.0
Ibs
%
Btu/ dry Ibs
of fuel
PRELIMINARY VELOCITY TRAVERSE
Dist (in)
0.4
1.5
4.5
5.6
0.090
0.141
0.140
0.125
Temp (F)
73
73
72
73
GENERAL
AVERAGE h
MM5G WEIGHTS (grams)
FILTER A
FINAL:
TARE:
NET:
0.7093
0.6302
0.0791
FILTER B
FINAL:
TARE:
NET:
0.6325
0.632
0.0005
CEM VALUES
O2:
CO2:
CO:
CO dilu:
JUM-THC:
TIME:
02:
CO2:
CO:
CO dilu:
RESULTS
PRE-TEST
ZERO
-0.27
0.05
0.01
4.88
6.1
0.6
9.8 %
10.64 %
0.923 %
SPAN
14.83
15.04
2.06
2006.84
81.2
507 ppm
Flow:
Fire rate:
Particulate:
EFFICIENCY:
TOTAL
TOTAL
(output/input)
239
4.68
53.80
11.49
0.65
264,724
556,757
47.55%
TIME:
O2.
CO2:
CO.
CO dilu:
cfm
dry kg/hr
g/hr
POST-TEST
ZERO
-0.27
0.05
0.01
4.88
12.21
0.686111
11.32
8.84
0.754
SPAN
14.89
15.43
2.07
2006.84
73.24
%
%
%
173 ppm
g/dry kg of fuel
mg/Btu
Btu output
Btu input
Pre-Test Leak:
Post-Test Leak:
Total Time:
0.015 cfm
0.018 cfm
401 min
39,922 Btu/hr
PAN RINSE
FINAL:
TARE:
NET:
2.6327
2.6234
0.0093
CO2:
CO:
CO ditu:
JUM-THC:
ACTUAL SPAN
15.00 %
15.00 %
2.01 %
2070.00 ppm
80.9 ppm
AVERAGES
O2: 11.087 %
9.377 %
13681 ppm
775.97 ppm
2527.43 ppm
F8
-------
WOODSTOVE TEST INFORMATION
NAME: Russell Logan and Joey Valenti
DATE: 10/25/95
TESTNo.:TD-MM5G-1
DESCRIPTION: Modified Method 5G Testing of Furnace A with Catalyst @ Low Heat Output
CONDITIONS
Ambient Temp.:
Barometric Press.:
Humidity:
FUEL INFORMATION
TYPE:
CHARGE WEIGHT
MOISTURE:
HEATING VALUE:
67.93 F
30.19 inHg
61 %
Red Oak
87.5 Ibs
18.90 %
8069.0 Btu/dry Ibs of fuel
PRELIMINARY VELOCITY TRAVERSE
GENERAL
Dist (in)
0.4
1.5
4.5
5.6
0.100
0.135
0.135
0.115
Temp (F)
67
67
67
67
Pre-Test Leak: 0.01
Post-Test Leak: 0.013
Total Time: 806
AVERAGE HEA' 23,993
cfm
cfm
min
Btu/hr
MM5G WEIGHTS (grams)
GEM VALUES
O2:
CO2:
CO:
CO dilu:
JUM-THC:
TIME: 0
O2:
CO2:
CO:
CO dilu:
RESULTS
FILTER A
FINAL:
TARE:
NET:
PRE-TEST
ZERO
-0.09
0.00
0.00
0.00
0
.51041666667
11.63
10.42
3.018
1298
Flow:
Fire rate:
Particulate:
EFFICIENCY:
TOTAL
TOTAL
(output/input)
0.7364
0.6129
0.1235
SPAN
15.08
15.45
2.11
2009.28
79.35
%
%
%
ppm
238
2.485
37.80
15.21
0.86
322,976
593,808
54.39%
TIME:
O2:
C02:
CO:
CO dilu:
cfm
dry kg/hr
g/hr
FILTER B
FINAL: 0.6150
TARE: 0.6139
NET: 0.0011
POST-TEST
ZERO SPAN
-0.09 15.14
0.00 14.94
0.00 2.07
4.88 2009.28
12.21 99.38
0.686111
11.84 %
9.25 %
1.428 %
2006 ppm
PAN RINSE
FINAL:
TARE:
NET:
2.6418
2.6318
0.0100
ACTUAL SPAN
15.00
15.00
2.01
2070.00
80.9
AVERAGES
02: 13.52
CO2: 7.323
CO: 0.9501
CO dilu: 540.912
JUM-THC: 1358.32
%
%
%
ppm
Ppm
%
%
Ppm
ppm
ppm
g/dry kg of fuel
mg/Btu
Btu output
Btu input
F9
-------
Manufacturer:
Model:
Date:
Run:
Project #:
Test Duration:
(minutes)
6/13/95
1
1810
SFBA EPA ADJUSTED EMISSION RESULTS
RESULTS
AVERAGE ADJUSTED EMISSION RATE:
Bum Rate (Dry kg/hr);
16.585
1.524
PRESSURE FACTOR: 0.97309 BAROMETRIC PRESSURE
TEMPERATURE FACTORS
DGM#1:
DGM #2:
VOLUMES SAMPLED
DGM#1:
DGM #2:
0.96776
0.96912
90.01393
88.21459
TOTAL TUNNEL VOLUME (scf): 660202.891
SAMPLE RATIOS
Sample Train 1: 7334.453
Sample Train 2: 7484.056
TOTAL EMISSIONS
Sample Train 1 (g): 436.3999
Sample Train 2 (g): 428.0880
EMISSION RATES
Sample Train 1 (g/hr): 14.4663
Sample Train 2 (g/hr): 14.1908
ADJUSTED EMISSION RATES
Sample Train 1 (g/hr): 16.7174
Sample Train 2 (g/hr): 16.4527
DEVIATION: 1.60%
DRY GAS METER VALUES
DGM #2
Average:
Start:
End:
Final:
Initial:
Final:
Initial:
TEMPERATURES (DEG. RANKIN)
DGM#1:
DGM #2:
CALIBRATION FACTORS
TUNNEL FLOW RATE:
DGM#1:
DGM #2:
PARTICULATE CATCH (mg)
Sample Train 1
Sample Train 2
29.115
29.11
29.12
661.836
567.534
1037.190
944.693
545.591
544.824
1.0136
1.0113
364.753
59.5
57.2
F10
-------
Manufacturer:
Model:
Date:
Run:
Project #:
Test Duration:
(minutes)
6/15/95
2
872
SFBA EPA ADJUSTED EMISSION RESULTS
RESULTS
AVERAGE ADJUSTED EMISSION RATE:
Bum Rate (Dry kg/hr):
36.009
3.352
PRESSURE FACTOR: 0.97727 BAROMETRIC PRESSURE
TEMPERATURE FACTORS
DGMn:
DGM #2:
VOLUMES SAMPLED
DGM#1:
DGM #2:
0.97327
0.97362
44.20632
42.83355
TOTAL TUNNEL VOLUME (scf): 314536.353
SAMPLE RATIOS
Sample Train 1: 7115.190
Sample Train 2: 7343.225
TOTAL EMISSIONS
Sample Train 1 (g): 557.8309
Sample Train 2 (g): 502.2766
EMISSION RATES
Sample Train 1 (g/hr): 38.3829
Sample Train 2 (g/hr): 34.5603
ADJUSTED EMISSION RATES
Sample Train 1 (g/hr): 37.5756
Sample Train 2 (g/hr): 34.4422
DEVIATION: 8.70%
DRY GAS METER VALUES
DGM#1
DGM #2
Average:
Start:
End:
Final:
Initial:
Final:
Initial:
TEMPERATURES (DEG. RANKIN)
DGM#1:
DGM #2:
CALIBRATION FACTORS
TUNNEL FLOW RATE:
DGM#1:
DGM #2:
PARTICULATE CATCH (mg)
Sample Train 1
Sample Train 2
29.24
29.24
29.24
707.779
661.926
81.840
37.326
542.500
542.303
1.0136
1.0113
360.707
78.4
68.4
Fll
-------
Manufacturer
Model:
Date:
Run:
Project #:
Test Duration:
(minutes)
SFBA EPA ADJUSTED EMISSION RESULTS
RESULTS
6-19-95 AVERAGE ADJUSTED EMISSION RATE:
Bum Rate (Dry kg/hr):
1833
17.676
1.677
PRESSURE FACTOR: 0.97376 BAROMETRIC PRESSURE
TEMPERATURE FACTORS
DGM#1:
DGM #2:
VOLUMES SAMPLED
DGM#1:
DGM #2:
0.97358
0.97243
94.17376
92.67136
TOTAL TUNNEL VOLUME (serf): 665485.824
SAMPLE RATIOS
Sample Train 1: 7066.574
Sample Train 2: 7181.138
TOTAL EMISSIONS
Sample Train 1 (g): 469.2205
Sample Train 2 (g): 476.1095
EMISSION RATES
Sample Train 1 (g/hr): 15.3591
Sample Train 2 (g/hr): 15.5846
ADJUSTED EMISSION RATES
Sample Train 1 (g/hr): 17.5693
Sample Train 2 (g/hr): 17.7832
DEVIATION: 1.21%
DRY GAS METER VALUES
DGM#1
DGM #2
Average:
Start:
End:
Final:
Initial:
Final:
Initial:
TEMPERATURES (DEC. RANKIN)
DGM#1:
DGM #2:
CALIBRATION FACTORS
TUNNEL FLOW RATE:
DGM #2:
PARTICULATE CATCH (mg)
Sample Train 1
Sample Train 2
29.135
29.22
29.05
805.843
707.840
179.098
82.325
542.330
542.970
1.0136
1.0113
363.058
66.4
66.3
F12
-------
Manufacturer:
Model:
Date:
Run:
Project #:
Test Duration:
(minutes)
6-21-95
4
1063
SFBA EPA ADJUSTED EMISSION RESULTS
RESULTS
AVERAGE ADJUSTED EMISSION RATE:
Burn Rate (Dry kg/hr):
36.951
2.834
PRESSURE FACTOR: 0.97343 BAROMETRIC PRESSURE
TEMPERATURE FACTORS
DGM#1: 0.97606
DGM #2: 0.97434
VOLUMES SAMPLED
DGM #2:
TOTAL TUNNEL VOLUME (set): 381915.228
55.50534
53.77269
SAMPLE RATIOS
Sample Train 1: 6880.693
Sample Train 2: 7102.401
TOTAL EMISSIONS
Sample Train 1 (g): 644.0329
Sample Train 2 (g): 688.9329
EMISSION RATES
Sample Train 1 (g/hr): 36.3518
Sample Train 2 (g/hr): 38.8861
ADJUSTED EMISSION RATES
Sample Train 1 (g/hr): 35.9177
Sample Train 2 (g/hr): 37.9840
DEVIATION: 5.59%
DRY GAS METER VALUES
DGM#1
DGM #2
Average:
Start:
End:
Final:
Initial:
Final:
Initial:
TEMPERATURES (DEG. RANKIN)
DGM#1:
DGM #2:
CALIBRATION FACTORS
TUNNEL FLOW RATE:
DGM#1:
DGM #2:
PARTICULATE CATCH (mg)
Sample Train 1
Sample Train 1
29.125
29.11
29.14
863.730
806.095
235.200
179.138
540.949
541.907
1.0136
1.0113
359.281
93.6
97.0
F13
-------
SFBA EPA ADJUSTED EMISSION RESULTS
Manufacturer
Model:
Date: 6-26-95
Run: 5
Project #:
Test Duration: 300
(minutes)
PRESSURE FACTOR:
TEMPERATURE FACTORS
DGM#1:
DGM #2:
VOLUMES SAMPLED
DGM#1:
DGM # 2:
TOTAL TUNNEL VOLUME (scf):
SAMPLE RATIOS
Sample Train 1 :
Sample Train 2:
TOTAL EMISSIONS
Sample Train 1 (g):
Sample Train 2 (g):
EMISSION RATES
Sample Train 1 (g/hr):
Sample Train 2 (g/hr):
ADJUSTED EMISSION RATES
Sample Train 1 (g/hr):
Sample Train 2 (g/hr):
RESULTS
AVERAGE ADJUSTED EMISSION RATE:
0.96741
0.98159
0.98050
15.15868
14.88113
111186.872
7334.866
7471.667
0.0073
0.0224
0.0015
0.0045
0.0081
0.0205
Bum Rate (Dry kg/hr):
BAROMETRIC PRESSURE
Average:
Start:
End:
DRY GAS METER VALUES
DGM#1 Final:
Initial:
DGM #2 Final:
Initial:
TEMPERATURES (DEG. RANKIN)
DGM#1:
DGM #2:
CALIBRATION FACTORS
DGM#1:
DGM #2:
TUNNEL FLOW RATE:
PARTICULATE CATCH (mg)
Sample Train 1 :
Sample Train 2:
0.014
0.000
28.945
28.94
28.95
879.547
863.798
250.758
235.245
537.903
538.500
1.0136
1.0113
370.623
0.0010
0.0030
DEVIATION:
86.60%
If deviation is greater than 7.5% due to low paniculate catch
The two emission rates shall not differ by 7.5%
of the weighted average emission rate limit (4.1 or 7.5) (5g-3)
Use the following:
Catalytic units
7.5% of 4.1 g/hr
Non catalytic units
7.5% of 7.5 g/hr
0.30%
-------
Appendix G - Organic Analyses Data Sheets
Gl
-------
January 26, 1996
Joey Valenti
Acurex Environmental
4915 Prospectus Dr. Suite F
Durham, NC 27713
Dear Mr. Valenti,
The Lab has completed the analysis of the MM5 train samples that were
submitted under the Emissions from Wood-Fired Residential Furnaces Project. Details of the
various sections of analytical work are detailed below. Analytical results for each sample and
other support documentation are detailed on the following sheets.
Receiving:
The following samples were received. Three sets of riata have been combined in this
report. The first set is the data from the tests done a* Funute /f in June of 1995. The
second set is the data from the June testing .0 K fu MM e fi and the third from the October
testing cf~ ft .. The descriptions of the samples are detailed on attached sheets.
The samples from f^u^~tl
-------
The GC/MS was tuned each day with perfluorotributylamine by the MS's data system.
Samples from the June testing were analyzed well outside the method specified hold times
due to the stop work order that was put into effect. The October testing samples were analyzed
within hold time.
The ^> . series of samples had a "Side A" and a "Side B" for each of the first two
tests. The four XAD extracts were each analyzed twice to demonstrate the instrument precision on
real samples. The analysis of the duplicates was on different days than the initial analysis. The
results were surprisingly good with RPDs around 5%.
Data:
Each of the analyzed fractions were compared with the target analyte list (see attached
sheets). If a peak was detected for the target ion inside the retention time window it was compared
with the reference spectra for the target compound. If the spectra matched, the peak was reported.
If any internal standards were outside the 8270 criterion it is noted on the sample summary
sheet.
The standard PAH target list was supplemented with four additional compounds,
2-Methylnaphthalene, Dibenzofuran, 7,12-Dimethylbenz(a)anthracene and
3-MethyIcholanthrene. Many on the samples had significant amounts of the first two supplemental
compounds.
In many of the samples the Naphthalene level was above the calibration level. Generally
the level was less than double the highest calibrated point. Please notify me if the further
expenditure of funds to rerun these samples diluted is needed.
If you have any questions on the data please feel free to call me.
G3
-------
Semi-Volatile Standard Workup Criteria
Tuning
In order to achieve maximum broad range sensitivity, the mass spectrometer was
computer tuned with perfluorotributylamine instead of the method specified
decafiuorotriphenylphosphine.
Calibration Check
The method specified checks are evaluated and the check sample rerun if
problems are detected.
Target Analysis
The calibrated range was 10 to 160 pg/ml of extract. Any target analyte detected
between 1 and 10 ng/ml were flagged "J" as estimated. Any target analyte
detected above 160 ug/ml were flagged "E" as estimated. A 1 ml final extract
volume is assumed unless otherwise stated. Units on the quantitation report are in
jo,g/ml of extract and dilution factors accounted for on the summary report. Units
on the summary report are in fig per train fraction. A 1 ul injection was used.
G4
-------
EPA/AEERL ONSITE LABORATORY SUPPORT CONTRACT
SAMPLE CHAIN OF CUSTODY RECORD
Page V of Z
rev. 11/94
Facility of Origin:
Facility of Destination:
Analyses Requested
OSL Project #:
Project:
F«O»A WOOD- Pifc^fc. 1^lB6it>6i4TlRl.
samples Collected By:'
LOC.M
Field
Sample
ID
Sample Description:
Date
and
Time
Request Results By:
Report Results To:
For Problems Contact (Name/Phone #);
,NJ \JftV.€4Tt ^m. 43>8o
Remarks:
Lab ID:
* LOvl
» Rcie*. -
6oitil
P.CTE&X-
foufcri
10
- i-Ovl
.- LOW
Comments:
Relinquished By (1):
Date/Time{1):
Received By (1):
Date/Time (1): Relinquished By {2):
Date/Time (2):
Received By (2):
Date/Time (2):
Disposal Information (Include Date. Time, Custodian, and Comments):
-------
EPA/AEERL ONSITE LABORATORY SUPPORT CONTRACT
SAMPLE CHAIN OF CUSTODY RECORD
Page 2. of
rev. 11/94
Facility of Origin:
proie»it;rT«^
Facility of Destination:
^Pft^fteeet orteite, L-AC»
i.
^CT,- *M -^.Dmrirt
Samples Collected By:' "Rotfseu. i^oc-.A4
Field
Sample
ID
rTp . iAM€"6i •'&•• 2'
^b-tA^Sta- r "2.t
"O.M'A'fCi'RL'Z
irT».M*s&.*.z6
r?D, MtASG ,*P(L2£
r.T-Mws&.r.it
"P.lAfAS'&.m^
r.t».M,A5C,.*.2
r.i>. «*»4 sa ;?n ,a
"t» . Mjv*5&. P. 2,
m^5a.pz.2
LD.MMgQ^^t
Sample
ftcc-Torfc
Description:
«L
44«£ - V\,G« CftN
Fiirree. - Hian C&^
ft 5-\CT££
^A"s> — A\fl«rt L^
Ae&To4& ftte-rb/JE
R.
,466 -WiG-dClli
> Pit.Te£. ~ Uisrt (.t>^
DP"n-Tee2. - Ui&u CT>)
)5AT> - WlGrt Cto"^
Comments:
Received By (1):
Disposal Information (Include
Date
and
Time
(./I1/1S-
(,/w/^s-
U/W /&0 »
Remarks:
*
'
"
«•
Relinquished By (1):
Received By (2): '
Lab ID:
Date/Time (1):
Daten"ime (2):
Date. Time, Custodian, and Comments):
o
-------
EPA/AEERL ONSITE LABORATORY SUPPORT CONTRACT
SAMPLE CHAIN OF CUSTODY RECORD
rev. 11/94
Page 3 of 5
Facility of Origin:
WOODiirtBvfe LA6>
3roject; £j*\vi»£tt>*i^> fitortv
VAeiVTlfJCt FotfWC.6«
Samples Collected By: ita6*
Field
Sample
ID
•nD.*A<&:at.s
•n>.iAiAfia.(?.5-
TD.lA.ASa.FW
n>.iAms&:*MJ
Sample
Facility of Destination:
CPAj/AfeKL oA*»Tt LA&
e
sJ
o&Ti - Fi^eti 1^B>it>e*4"nAi
CL 1-OGA4
At,&tT|
Description:
AcB-m4E e,M-&e - &UUK.
^tuTefc. - 2>v,Arf(k
PiutfelL 2. • filAAK
Aee,-roi4t. 1>t-hA^.
Comments:
Received By (1):
Disposal Information (Include
Date
and
Time
u/t«,^5-
l«/IS/^6"
U/|5/«.
n
^
1
K
,,
^
<
o
^
^
n
,c
1
-
Date/Time (1):
Relinquished By (2):
Date/Time (2):
3SL Project #:
Request Results By:
•
Report Results To:
i&6Nf ^At,£4"r«
For Problems Contact (Name/Phone #):
Remarks:
"
"
m
Relinquished By (1):
Received By (2): *
Lab ID:
Daten"ime(1):
Date/Time (2):
Date, Time, Custodian, and Comments):
o
—I
-------
Table 1: How to Analyze
Fl* I"/W.Q,C>& B
Probe and Filter Samples for PAH
Combine 1 ml from each of these well mixed,
correct volume extracts together and mix
well before PAH analysis. Retain the
ballance of the extracts separately.
filter 53-54
filter 57-58
Dish 1 (probe A) f^^A&e "&.
Dish 3 (probe C) (note: Areport shows
this probe as probe E in two places however
two Acurex personnel on separate occasions
observed the label to be Probe C. Based on
other identifying information we are assuming
probe C=probe E),
Multiply the final
concentration in
ug/ml by this factor
to derive the final
mass on the filter
and probe
Test and System
Number
20ml
filter 55-56
filter 59-60
Dish 2 (probe B)
Dish 4 (probe D)
filter 6S.-66
filter 69-70
Dish 5 (probe G)
Dish 7 (probe I)
Filter 67-68
Filter 71-72
Dish 6 (Probe H)
Dish 8 (probe J)
Filter 61-62
Dish 9 (Probe A)
Filter 63-64
Dish 10 (probe B)
Filter 77-78
Filter 81-82
Dish 1 1 (Probe G)
Dish 13 (Probe I)
Filter 79-80
Filter 83-84
Dish 12 (Probe H)
Dish 14 (Probe J)
Filter 85-86
Filter 87-88
Test 1 System 1
20
20
Test 1 System 2
i/
20
10
Test 2 System 1
Test 2 System 2
,»/£*
as
Test 3 System 1
10
20
20
Test 3 System 2
Test 4 System 1
Test 4 System 2
Test 5 System 1
Test 5 System.2
•1/2-7
G8
-------
7
TEST
1
1
2
2
3
3
4
4
5
5
1
1
1
1
2
2
2
2
3
3
4
4
4
4
5
5~
2
4
1
1
1
1
2
2
2
2
3
3
4
4
4
4
Sample Type
XAD
XAD
XAD
XAD
XAD
XAD
XAD
XAD
XAD
XAD
filter
filter
filter
filter
filter
filter
filter
filter
filter
filter
filter
filter
filter
filter
filter
/v//^
woodsample
woodsample
dishl
dish 2
dish 3
dish 4
dish 5
dish 6
dish?
dish 8 "
dish 9
dish 10 •
dish 1 1 .
dish 12 •
dish 13 •
dishl 4
ID
side A
sideB
side A
sideB
blank
Location of Test
{-UASH*-*/ £%
\ J
[
.
1
\J
Date
6/(13-14)/95
6/(13-14)/95
6/15/95
6/15/95
6/20/95
6/20/95
6/21/95
6/21/95
6/26/95
6/26/95
6/16/95
6/16/95
6/16/95
6/16/95
6/20/95
6/20/95
6/20/95
6/20/95
6/20/95
6/20/95
6/20/95
6/20/95
6/20/95
6/20/95
6/20/95
6/15/95
1
2
1
2
1
L 2
1
a
/
^
/
a.
i
a
1
2
1
2
1
2
2
/
/
%
f
a
/
a.
/
£
/
R
r
9-
/
5^
53-54 ^
55-56 iX
57-58 »X
59-60 ,/
65-66 »x-
67^8 ,x
69-70 •
71-72 ^X
61-62 _fe=_
63-64 ^x
77-78 tx-
79-80 /
81-82 ^x
83-84 X
87-88 _^
fzr-Zts
X
•X
iX
/
^
s
I/
I/
^
(/
I/
V
/
t/
A
B
C
D
G
H
1
J
A
B
G
H
I
J
G9
-------
REGIE VED
• 10/31/95.
,10/31/95.
« 10/31/95*
l« 10/3 1/95*1
10/31/95
• 10/31/95-
• 16/31/95 •
- 10/31/95.
•10/31/95,
• 10/31/95.
• 10/31/95.
-10/31/95*
SAMPLE GUST ID
TCD-MM5G-2-F2'
TCD-MMSG-2-PR
TCD-MM5G-X-2
IJCD-MM5G-FA1-
TCD-MM5G-FB1-
TCD-MM5G-PR1-
BLANK
ACETONE ONLY
TCD-MM5G-FA-5
TCD-MM5G-FB-5
TCD-MM5G-PR-5
DESCRIPTION
HIGH BURN-BACK
.. XHI(jHBlJkM-ffcttli)l""*-^»
( HIGH BURN-PAN^/
XSDtHUHBUlO^- —
/-LOW BURN RATE-FRONT'S.
LOW BURN RATE-BACK ~f
^-tLOW BURN RATE-FAN-^
,- " XAD
JTIONT HALF FILTER-BLANK
BACK HALF FILTER-BLANK
* PAN RINSE BLANK
COLLECTED
10/25/95
10/25/95
10/25/95
" 10/25/95
10/26/95
10/26/95
10/26/95
10/26/95
10/26/95
10/26/95
10/26/95
10/26/95
EXTkACXlliJ
11/1/95
11/1/95
11/6/95
11/2/95
11/1/95
11/1/95
11/6/95
11/2/95
11/6/95
11/2/95
11/1/95
11/6/95
CAPPED
11/2/95
11/2/95
11/6/95
11/3/95
11/2/95
1 11/2/95'"'
11/6/95
11/3/95
11/6/95
11/3/95
11/2/95
11/6/95
She.
CHECKED OUT
FOR GRAV/TCO
11/8/95 —
1 1/9/95 •^J
ii/io/9S->^
11/11/95 — i
11/13/95*")
li/14/95 C_
11/15/95 /T
11/16/95 —
11/17/95 —
11/18/95 I
11/19/95 '
11/20/95 X"
!t1
GC/MS
— • -
Tn-"— ~"
kMpORTED
I
- ^
— r^^
/i
L__ O
-J
Q
i—i
o
Pagel
-------
Samples for The Emissions from Wood-Fired Residential Furnaces Project
Furnace A
Sample ID. Date Sampled Compositing Date Analyzed MS File ID
TD-MM5G-PR-1A 6/28/95 with F and F2
TD-MM5G-F-1A 6/28/95
TD-MM5G-F2-1A 6/28/95
TD-MM5G-X-1A 6/28/95
TD-MM5G-PR-2A 6/15/95
TD-MM5G-F-2A 6/15/95
TD-MM5G-F2-2A 6/15/95
TD-MM5G-X-2A 6/15/95
TD-MM5G-PR-1B 6/29/95
TD-MM5G-F-1B 6/29/95
TD-MM5G-F2-1B 6/29/95
TD-MM5G-X-1B 6/29/95
TD-MM5G-PR-2B 6/19/95
TD-MM5G-F-2B 6/19/95
TD-MM5G-F2-2B 6/19/95
TD-MM5G-X-2B 6/19/95
TD-MM5G-PR-2C 6/27/95
TD-MM5G-F-2C 6/27/95
TD-MM5G-F2-2C 6/27/95
TD-MM5G-X-2C 6/27/95
TD-MM5G-PR-2D 6/30/95
TD-MM5G-F-2D 6/30/95
TD-MM5G-F2-2D 6/30/95
TD-MM5G-X-2D 6/30/95
TD-MM5G-PR-5 6/13/95
TD-MM5G-F-5 6/13/95
TD-MM5G-F2-5 6/13/95
TD-MM5G-PR-0 6/30/95
with PR and F2 1/25/96
with PR and F
none
1/17/96
with F and F2
with PR and F2 12/9/95
with PR and F
none
12/14/95
with F and F2
with PR and F2 12/8/95
with PR and F
none
12/13/95
with F and F2
with PR and F2 12/11/95
with PR and F
none
12/12/95
with F and F2
with PR and F2 12/9/95
with PR and F
none
12/12/95
with F and F2
with PR and F2 12/9/95
with PR and F
none
12/12/95
with F and F2
with PR and F2 12/11/95
with PR and F
none
12/8/95
WSCOMP1A.D
WSTDX1A.D
WSTD2A.D
WSTDX2AD.D
WSTDFP1B.D
WSTDX1BD.D
WSTD2B.D
WSTDX2B.D
WSTD2C.D
WSTDX2C.D
WSTD2D.D
WSTDX2D.D
WSTD5D.D
WSTDPROA.D
Gil
-------
WSPAHMS.XLS
SAMPLE: WS PAH Blank Resin Spike
MS FILE ;WSPAHMS.D
PROJECT: Emissions From Wood-Fired Residential. Heating Furnaces -
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 2B Nov 95 12:30
System Monitoring Compounds
2-Fluorophenol(surr#1 >
D6-PhenoHsurr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-Terphenyl(surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
3henanthrene
Anthracene
Fluoranthene
3yrene
Chrysene
Benzo(a)anthracene
Benzo(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
3enzo(k)fluoranthene
3enzo(a)pyrene
3-methylcholanthrene
IndenoH »2,3-cd)pyrene
3ibenz(a,h)anthracene
3enzo(ghi)perylene
Extrac
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
MDL
1.21
1
0,79
0.86
0.83
0.55
0.59
0.32
0.33
0.23
0.24
0.52
0.7
0.28
0,62
0.64
0.52
1
1
P/F
F
F
F
F
F
F
PQL
10
ml
X
LIMITS
21-100
10-94
35-114
43-1 1 6
10-123
33-141
amount (//g)
and % rec.
88
NS
86
89
NS
81
83
82
87
88
86
85
86
NS
86
95
NS
82
86
101
G12
-------
WSPAHMSD.XLS
SAMPLE: WS PAH Blank Resin Spike Duplicate
MS FILE .-WSPAHMSD.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 29 Nov 95 1 :30
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenal(surr#2)
D5-Nttrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenoI(surr#5)
D1 4-Terphenyl{surr#6)
Target Compounds
Naphthalene
2-methyInaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
Phenanthrene
Anthracene
:luoranthene
Pyrene
Chrysene
Benzo(a)anthracene
Benzo(b)fluoranthene
7,1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
Benzo(a)pyrene
-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
MDL
1.21
1
0.79
0.86
0.83
0.55
0.59
0.32
0,33
0.23
0.24
0.52
0.7
0.28
0.62
0.64
0.52
1
1
P/F
F
F
F
F
F
F
PQL
10
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
amount (//g)
and % rec.
92
NS
91
94
NS
84
87
85
95
94
89
89
87
NS
82
99
NS
102
85
99
G13
-------
WSGB725.XLS
SAMPLE:WS Glassware Blank
MS FILE :WSGB725.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 28 Nov 95 8:55
System Monitoring Compounds
2-FluorophenoI{surr$1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-FluorobiphenyI(surr#4)
2,4,6-tribromophenol(surr#5)
D 1 4-Terphenyl (surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
3ibenzofuran
:luorene
3henanthrene
Anthracene
:luoranthene
^yrene
Chrysene
3enzo(a)anthraeene
3enzo(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
Benzo(a)pyrene
3-methylchoIanthrene
Indenod ,2,3-cdJpyrene
3ibenz(a,h)anthracene
Benzo(ghi)perylene
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
5
1
P/F
F
F
F
F
F
F
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
PQL
50
amount |//g)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
i
G14
-------
WSCOMP1A.XLS
SAMPLE: TD-MM5G-(PR + F + F2)-1 A Composite of extracts
MS FILE :WSCOMP1A.D
PROJECT: Emissions from Wood-Fired Residential Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 25 Jan 96 2:32
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-Terphenyl(surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
Phenanthrene
Anthracene
:luoranthene
Pyrene
Chrysene
Benzo(a)anthracene
Benzo(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
3enzo(a)pyrene
i-methylcholanthrene
Indenod ,2,3-cd)pyrene
3ibenz(a,h)anthracene
3enzo(ghi)perylene
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
MDL
18.15
15
11.85
12.9
12.45
8.25
8.85
4.8
4.95
3.45
3.6
7.8
10.5
4.2
9.3
9.6
7.8
5
c
P/F
NS
NS
NS
NS
NS
NS
PQL
150
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
amount (JJQ)
ND
ND
ND
ND
ND
22 J
120 J
33 J
65 J
62 J
22 J
30 J
20 J
ND
ND
24 J
ND
22 J
25 J
29 J
G15
-------
WSTDX1A.XLS
SAMPLE: Acurex TD-MM5G-X-1A
MS FILE :WSTDX1A.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 17 Jan 96 14:29
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-Terphenyl(surr#6)
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
P/F
NS
NS
NS
NS
NS
NS
I
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Chrysene
Benzo(a)anthracene
Benzp(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
5enzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
50
50
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
amount (//g)
814 E
176
150
15 J
35 J
23 J
6.9 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G16
-------
WSTD2A.XLS
SAMPLE: TD-MM5G-(PR + F + F2J-2A Composite of extracts
MS FILE :WSTD2A.D
PROJECT: Emissions from Wood-Fired Residential Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 9 Dec 95 4:21
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-FluorobiphenyI(surrf4)
2,4,6-tribromophenol{surr#5)
D14-Terphenyl(surr#6)
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
3
P/F
NS
NS
NS
NS
NS
NS
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
; j
| !
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Chrysene
Jenzo(a)anthracene
Benzo(b)fluoranthene
7, 1 2-Dimethylbenz(aianthracene
Benzo{k)fluoranthene
Benzojajpyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Jenzo(ghi)perylene
MDL
18.15
15
11.85
12.9
12.45
8.25
8.85
4.8
4.95
3.45
3.6
7.8
10.5
4.2
9.3
9.6
7.8
PQL
150
amount (fjg)
NO
ND
ND
ND
ND
26 J
155
33 J
54 J
69 J
20 J
20 J
17 J
ND
ND
20 J
ND
ND
ND
ND
G17
-------
WSTDX2AD.XLS
SAMPLE: TD-MM5G-X-2A XAD High Burn Dup
MS FILE :WSTDX2AD.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 14 Dec 95 16:30
System Monitoring Compounds
2-Fluorophenol(surr#1 }
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-FluorobiphenyI(surrf4)
2,4,6-tribromophenoI(surr#5)
D1 4-Terphenyl(surr#6)
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
j
P/F
NS
NS
NS
NS
NS
NS
ml
X
I
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
i
s j
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:Iuorene
Phenanthrene
Anthracene
:luoranthene
3yrene
Chrysene
Benzo(a)anthracene
Benzo(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
$enzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
MDL
6,05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
amount (fjg)
1210E
258
167
15 J
30 J
16 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G18
-------
WSTDFP1B.XLS
SAMPLE: TD - MM5G-(F + F2 + PR)-1B Rinse and Filters from Test IB at Acurex
MSFILE:WSTDFP1B.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 8 Dec 95 12:36
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D14-Terphenyl(surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Chrysene
3enzo(a)anthracene
Benzo(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
Benzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
Extra c
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
MDL
18.15
15
11.85
12.9
12.45
8.25
8.85
4.8
4.95
3.45
3.6
7.8
10.5
4.2
9.3
9.6
7.8
5
3
P/F
F
F
F
F
F
F
ml
X (Composite
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
POL
150
amount (//g)
ND
ND
ND
ND
ND
ND
80 J
20 J
38 J
42 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G19
-------
WSTDX1BD.XLS
SAMPLE: TD-MM5G-X-1B
MS FILE :WSTDX1BD.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 1 3 Dec 95 11:11
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surrf2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5}
D1 4-Terpheny!(surrf 6)
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
P/F
NS
NS
NS
NS
NS
NS
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
i
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
'henanthrene
Anthracene
:Iuoranthene
5yrene
Chrysene
3enzo{a)anthracene
3enzo(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
3enzo(k)fluoranthene
3enzo(a)pyrene
3-methyIcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
amount (//g)
925 E
178
130
13 J
30 J
17 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G20
-------
WSTD2B.XLS
SAMPLE: TD-MM5G-(PR + F + F2)-2B Composite of extracts
MS FILE :WSTD2B.D
j
!
PROJECT: Emissions from Wood-Fired Residential Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 1 1 Dec 95 3:58
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surrf2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenoI(surr#5)
D14-Terphenyl(surr#6)
i
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Target Compounds
Naphthalene
2-methylnaphthaIene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
3henanthrene
Anthracene
:Iuoranthene
3yrene
Chrysene
3enzo(a)anthracene
Benzo{b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
Benzo(a)pyrene
3-methylchoIanthrene
ndenod ,2,3-cd)pyrene
3ibenz{a»h)anthracene
3enzo{ghi)perylene
MDL
18.15
15
11.85
12.9
12.45
8.25
8.85
4.8
4.95
3.45
3.6
7.8
10.5
4.2
9.3
9.6
7.8
5|ml
3 X
1
P/F
NS
NS
NS
NS
NS
NS
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
PQL
150
amount (fjg)
ND
ND
ND
ND
ND
18 J
136 J
28 J
55 J
53 J
17 J
17 J
16 J
ND
ND
17 J
ND
ND
ND
ND
G21
-------
WSTDX2B.XLS
SAMPLE: TD-MM5G-X-2B
MS FILE :WSTDX2B.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 12 Dec 95 10:52
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-Terphenyl(surr#6)
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
P/F
NS
NS
NS
NS
NS
NS
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
i <
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Chrysene
Benzo(a)anthracene
Benzo(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
Benzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
amount (//g)
700
107
82.2
10 J
30 J
12 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G22
-------
WSTD2C.XLS
SAMPLE: TD-MM5G-{PR + F + F2J-2C Composite of extracts
MS FILE :WSTD2C.D
PROJECT: Emissions from Wood-Fired Residential Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 9 Dec 95 3:29
System Monitoring Compounds
2-Fluorophenol{surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-FIuorobiphenyI(surr#4)
2,4,6-tribromophenoHsurr#5}
D1 4-Terphenyl(surr#6)
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Siml
j
3 X
I
P/f
NS
NS
NS
NS
NS
NS
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
I
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
3ibenzofuran
:luorene
3henanthrene
Anthracene
Fluoranthene
'yrene
Chrysene
3enzo(a)anthracene
Benzo(b)fluoranthene
7, 1 2-Dimethyibenz(a)anthracene
3enzo(k)fluoranthene
5enzo{a)pyrene
3-methylcholanthrene
ndenod ,2,3-cd)pyrene
)ibenz(a,h)anthracene
Jenzo(ghi)perylene
MDL
18.15
15
11.85
12.9
12.45
8.25
8.85
4.8
4.95
3.45
3.6
7.8
10.5
4.2
9.3
9.6
7.8
PQL
150
amount (fjg)
ND
ND
34 J
ND
24 J
61 J
242
55 J
96 J
110 J
24 J
29 J
31 J
ND
ND
34 J
ND
ND
ND
18 J
G23
-------
WSTDX2C.XLS
SAMPLE: TD-MM5G-X-2C
MS FILE :WSTDX2C.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 12 Dec 95 2:55
System Monitoring Compounds
2-FluorophenoI(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-FluorobiphenyI(surr#4)
2,4,6-tribromophenoI(surr#5)
D1 4-Terphenyl{surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
'henanthrene
Anthracene
Fluoranthene
3yrene
Chrysene
3enzo(a)anthracene
Benzo{b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
Benzo{a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
P/F
NS
NS
NS
NS
NS
NS
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
amount (fjg)
1640 E
270
228
20 J
30 J
21 J
5 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G24
-------
WSTD2D.XLS
SAMPLE: TD-MM5G-(PR + F + F2)-2D Composite of extracts
MS FILE :WSTD2D.D
PROJECT: Emissions from Wood-Fired Residential Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 9 Dec 95 2:42
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-FIuorobiphenyI (surrf 4)
2,4,6-tribromophenol{sijrrf5)
D 1 4-TerphenyI(surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
'henanthrene
Anthracene
:luoranthene
'yrene
Chrysene
3enzo(a)anthracene
3enzo(b)fluoranthene
7,1 2-DimethyIbenz(a)anthracene
Benzo(k)fluoranthene
Jenzo(a)pyrene
i-methylcholanthrene
Indenod ,2,3-cd)pyrene
>ibenz(a,h)anthracene
Jenzo{ghi)perylene
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
3
P/F
NS
NS
NS
NS
NS
NS
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
MDL
18,15
15
11.85
12.9
12.45
8.25
8.85
4.8
4.95
3.45
3.6
7.8
10.5
4.2
9.3
9.6
7.8
PQL
150
amount (fjg)
ND
ND
ND
ND
ND
ND
104 J
25 J
48 J
59 J
ND
16 J
ND
ND
ND
17 J
ND
ND
ND
ND
G25
-------
WSTDX2D.XLS
SAMPLE: TD-MM5G-X-2D
MS FILE :WSTDX2D.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 12 Dec 95 1:55
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surr#2S
D5-Nitrobenzene{surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D 1 4-TerphenyI (surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
Phenanthrene
Anthracene
Fluoranthene
'yrene
Chrysene
3enzo(a)anthracene
Benzo(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
3enzo(k)fluoranthene
3enzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
P/F
NS
NS
NS
NS
NS
NS
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
POL
50
amount (//g)
867 E
182
134
11 J
23 J
15 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G26
-------
WSTD5D.XLS
SAMPLE: TD-MM5G-{PR + F + F2)-5D Composite of extracts _,
MS FILE :WSTD5D.D
I
PROJECT: Emissions from Wood-Fired Residential Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 11 Dec 95 5:10
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Pnenol(surr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenoI(surr#5)
D1 4-TerphenyI(surr#6)
Extract
Volume
Dilution
5
3
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
P/F
NS
NS
NS
NS
NS
NS
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
i
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
3ibenzofuran
Fluorene
3henanthrene
Anthracene
Fluoranthene
3yrene
Chrysene
3enzo(a)anthracene
Benzo(b)fluoranthene
7,1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
lenzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
>ibenz(a,h)anthracene
Benzo(ghi)perylene
MDL
18.15
15
11.85
12.9
12.45
8.25
8.85
4.8
4.95
3.45
3.6
7.8
10.5
4.2
9,3
9.6
7.8
PQL
150
amount (fjg)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G27
-------
WSTDPROA.XLS
SAMPLE: TD - MM5G-PR-0 Acetone Blank
MS FILE :WSTDPROA.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 8 Dec 95 10:35
System Monitoring Compounds
2-FIuorophenoI(surr#1 )
D6-Phenol(surrf2)
D5-Nitrobenzene{surr#3)
2-FluorobiphenyI(surr#4)
2,4,6-tribromophenol{surr#S)
D14-Terphenyl(surr#6)
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
ml
X
P/F
F
F
F
F
F
F
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
•
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
3ibenzofuran
Fluorene
Phenanthrene
Anthracene
:luoranthene
'yrene
Chrysene
Jenzo(a)anthraeene
3enzo(b)fluoranthene
7,1 2-Dimethylbenz{a)anthracene
Benzo{k)fluoranthene
3enzo(a)pyrene
3-methylcholanthrene
ndenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
3enzo(ghi)perylene
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
amount (fjg)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G28
-------
Samples for The Emissions from Wood-Fired Residential Furnaces Project
Furnace B
Sample ID. Date on
Sample
Compositing Date Analyzed MS File ID
1- -X-Side A
l--X-SideB
M-F-53,54
l-l-F-57,58
1-1-D-l
l-l-D-3
1-2-F-55.56
l-2-F-59,60
1-2-D-2
1-2-D-4
2- -X-Side A
2- -X-Side B
2-1-F-65.66
2-1-F-69.70
2-1 -D-5
2-1-D-7
2-2-F-67.68
2-2-F-71.72
2-2-D-6
2-2-D-8
3-1-X
3-l-F-61,62
3-1-D-9
3-2-X
3-2-F-63564
3-2-D-10
6/13-14/95
6/13-14/95
6/16/95
6/16/95
6/16/95
6/16/95
6/15/95
6/15/95
6/20/95
6/20/95
6/20/95
6/20/95
6/20/95
6/20/95
6/20/95
6/20/95
none
none
Both
Filters
and
Dishes
Both
Filters
and
Dishes
none
none
Both
Filters
and
Dishes
Both
Filters
and
Dishes
none
Filter
and Dish
none
Filter
and Dish
12/6/95
1/25/96
12/6/95
1/16/96
11/28/95
11/28/95
12/8/95
1/16/96
12/6/95
1/17/96
11/27/95
11/27/95
12/13/95
1 1/28/95
12/13/95
11/28/95
WSICBXDA.D
WST1SADP.D
WSICBXDB.D
WST1SBXD.D
WST1S1.D
WST1S2.D
WSIT2XDA.D
WST2SAXD.D
WSIT2XDB.D
WST2SBXD.D
WST2S1.D
WST2S2.D
WSTT3S1.D
WST3S1.D
WSTT3S2.D
WST3S2.D
G29
-------
Samples for The Emissions from Wood-Fired Residential Furnaces Project
FurnaceB
Sample ID. Date on
Sample
4-1-X
4-1-F-77.78
4-1-F-81-82
4-1-D-ll
4-1-D-13
4-2-X
6/21/95
6/20/95
6/20/95
6/21/95
Compositing Date Analyzed MS File ID
none
Both
Filters
and
Dishes
none
1/22/96
WST4SYS1.D
11/27/95 WST4S1.D
12/14/95 WSTDT4S2.D
4-2-F-79,80
4-2-F-83.84
4-2-D-12
4-2-D-14
5-1-X-blank
5-l-F-85,86
5-2-X
5-2-F-87,88
6/20/95
6/20/95
6/26/95
6/20/95
6/26/95
6/20/95
Both
Filters
and
Dishes
none
none
none
none
11/27/95
1/17/96
1 1/28/95
12/14/95
11/28/95
WST4S2.D
WST5BKS1.D
WST5S1.D
WSTDT5S2.D
WST5S2.D
Sample ID is the Test-System-Type-Number(s) from the inventory of samples received from
Inchcape.
G30
-------
WS1CBXDA.XLS
SAMPLE: Test 1 XAD Side A
MS FILE :WSICBXDA.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 6 Dec 95 12:24
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenoi(surr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surrf5)
D1 4-TerphenyI(surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthyiene
Acenaphthene
Dibenzofuran
:luorene
3henanthrene
Anthracene
Fluoranthene
3yrene
Chryserie
3enzo(a)anthracene
Benzo(b)fluoranthene
7,1 2-Dimethylbenz(a}anthracene
Benzo(k)fluoranthene
3enzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz{a,h)anthracene
Benzolghilperylene
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
MDL
6.05
5
3.95
4.3
4,15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
5
1
P/F
F
F .
F
F
F
F
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
|
POL
50
amount (fjg)
839 E
128
288
18 J
44 J
64.0
70.0
14 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G31
-------
WST1SADP.XLS
SAMPLE: Test 1 XAD Side A
MS FILE :WST1SADP.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 25 Jan 96 3:54
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surr#2J
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-TerphenyHsurr#6)
Target Compounds
Naphthalene
2-methyInaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
3henanthrene
Anthracene
Fluoranthene
syrene
Chrysene
Benzo{a)anthracene
Benzo(b)fluoranthene
7,1 2-Dimethylbenz(a)anthracene
Benzo(k}fluoranthene
Benzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
5ibenz!a,h}anthracene
Benzo(ghi)perylene
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked j
Not Spiked
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
g
1
P/F
F
F
F
F
F
F
PQL
50
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
amount {//oj
769
121
260
18 J
43 J
61.6
67.9
13 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G32
-------
WST1SBXD.XLS
SAMPLE: Test 1 Side B XAD
MS FILE :WST1SBXD.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
.
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 16 Jan 96 15:16
System Monitoring Compounds
2-FluorophenoI(surr#1 )
D6-Phenol{surr#2)
DS-Nitrobenzene(surr#3)
2-F!uorobiphenyl{surr#4)
2,4,6-tribromophenol(surr#5)
D14-Terphenyl{surr#6)
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
P/F
NS
NS
NS
NS
NS
NS
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
i
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Chrysene
Benzo(a)anthracene
Benzo(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo{k)fluoranthene
Benzo{a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd}pyrene
Dibenz(a,hjanthraeene
Benzo(ghi)perylene
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
50
50
amount (fjg)
511
86.0
210
14 J
29 J
41 J
44 J
8.6 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G33
-------
WSICBXDB.XLS
SAMPLE: Test 1 XAD Side B
MS FILE rWSlCBXDB.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST; Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 6 Dec 95 2:13
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surrf3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-Terphenyl(surrf 6)
Extract
Volume
Dilution
% Re co very
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
P/F
F
F
F
F
F
F
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
'henanthrene
Anthracene
Fluoranthene
Pyrene
Chrysene
3enzo{a)anthracene
Benzo(b)fluoranthene
7,1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
Benzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz{a,h)anthracene
Benzo(ghi)perylene
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
amount |//g)
538
91.2
213
13 J
60 J
45 J
46 J
9 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G34
-------
WST1S1.XLS
SAMPLE:WS Filters 53,54,57 and 58 Dishes 1 and 3 (Composite of four Extracts
MS FILE :WST1S1.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 28 Nov 95 12:53
System Monitoring Compounds
2-Fluorophenolfsurr#1 )
D6-Pheno!(surrf2)
D5-Nitrtibenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
31 4-Terphenyl(surr#6)
Target Compounds
Naphthalene
2-methyInaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
3henanthrene
Anthracene
Fluoranthene
*yrene
Chrysene
3enzo(a)anthracene
Benzo(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Jenzo(k)fluoranthene
Benzo(a)pyrene
i-methylcholanthrene
Indenod ,2,3-cdjpyrene
Dibenz(a,h)anthracene
Benzofghijperylene
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
MDL
24.2
20
15.8
17.2
16.6
11
11.8
6.4
6.6
4.6
4.8
10.4
14
5.6
12.4
12.8
10.4
5
4
P/F
F
F
F
F
F
F
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
l
PQL
200
amount (fig)
ND
ND
ND
ND
ND
ND
43 J
ND
71 J
103 J
ND
21 J
28 J
ND
ND
27 J
ND
ND
ND
21 J
G35
-------
WST1S2.XLS
SAMPLE:WS Filters 55,56,59 and 60 Dishes 2 and 4 Composite of four Extracts)
MS FILE :WST1S2.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 28 Nov 95 1 :48
System Monitoring Compounds
2-Fluorophenol{surr#1 }
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-FIuorobiphenylfsurr#4)
2,4,6-tribromophenol(surr#5)
D14-Terphenyl(surr#6)
Extract
Volume
I
Dilution
5
4
ml
X
QSs 1 ,4,5 and 6 were just below 5
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
P/F
F
F
F
•F
F
F
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
Target Compounds
Naphthalene
2-methylnaphthaIene
Acenaphthylene
Acenaphthene
Dibenzofuran
:Iuorene
Phenanthrene
Anthracene
Fluoranthene
3yrene
Chrysene
Jenzo(a)anthracene
3enzo(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo{k)fluoranthene
3enzo{a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
)ibenz(a,h)anthracene
Benzo{ghi)perylene
MDL
24.2
20
15.8
17.2
16.6
11
11.8
6.4
6.6
4.6
4.8
10.4
14
5.6
12.4
12.8
10.4
PQL
200
amount if/g)
ND
ND
ND
ND
ND
ND
30 J
ND
58 J
89 J
ND
ND
22 J
ND
ND
ND
ND
ND
ND
ND
•
G36
-------
WSIT2XDA.XLS
SAMPLE: Test 2 XAD Side A
MS FILE :WSIT2XDA.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 8 Dec 95 1 :36
System Monitoring Compounds
2-FluorophenoI(surr#1 )
D6-PhenoI{surr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenoHsurr#5)
D14-Terphenyl(surr#6)
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
P/F
F
F
F
F
F
F
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
I •
Target Compounds
Naphthalene
2-methyInaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
3henanthrene
Anthracene
:luoranther»e
'yrene
Chrysene
3enzo(a)anthracene
Benzo{b)fluoranthene
7,1 2-Dimethylbenz{a)anthracene
ienzo(k)fluoranthene
3enzo(a)pyrene
3-methylcholanthrene
lndeno{1 »2,3-cd)pyrene
)ibenz(a»h)anthracene
Benzo|ghi)perylene
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
amount (//g)
872 E
129
318
20 J
32 J
64.7
125
30 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G37
-------
WST2SAXD.XLS
SAMPLE: Test 2 Side A XAD
MS FILE :WST2SAXD.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 16 Jan 96 16:12
System Monitoring Compounds
2-FluorophenoHsurr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surrf3)
2-FIuorobiphenyl(surr#4)
2,4,6-tribromophenol{surr#5)
D1 4-Terphenyl(surr#6)
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
P/F
NS
NS
NS
NS
NS
NS
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Chrysene
Benzo(a)anthracene
Benzofbjfluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
Benzo(a)pyrene
3-methylchoIar»threne
Indenof 1 ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo{ghi)perylene
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
50
50
amount (//g)
896 E
136
333
21 J
34 J
69 J
133
32 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G38
-------
WSIT2XDB.XLS
SAMPLE: Test 2 XAD Side B
MS FILE :WS1T2XDB.D
1
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 6 Dec 95 4:04
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene{surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol{surr#5)
D14-Terphenyl(surr#6)
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
P/F
F
F
F
F
F
F
i
mi
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
j
Target Compounds
Naphthalene
2-methyinaphthalene
Acenaphthylene
Acenaphthene
>ibenzofuran
:Iuorene
3henanthrene
Anthracene
Fluoranthene
'yrene
Chrysene
3enzo(a)anthracene
Benzo(b)ffuoranthene
7 , 1 2-DimethyIbenz(a5anthracene
Jenzo(k)fluoranthene
Jenzoia)pyrene
'-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Jenzo(ghi)peryiene
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
amount (fjg)
1000 E
162
406
26 J
45 J
95.8
118
27 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G39
-------
WST2SBXD.XLS
SAMPLE: Test 2 Side B XAD
MS FILE :WST2SBXD.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 17 Jan 96 10:28
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-PhenoIfsurr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl{surr#4)
2,4,6-tribromophenoHsurr#5)
D1 4-Terphenyl(surr#6S
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
ml
X
P/F
NS
NS
NS
NS
NS
NS
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
Phenanthrene
Anthracene
:luoranthene
'yrene
Chrysene
Benzo(a)anthracene
3enzo(b}fluoranthene
7, 1 2-DimethyIbenz{a)anthracene
Benzo(k)fluoranthene
Benzo(a)pyrene
i-methylcholanthrene
lndeno( 1 ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
50
50
amount (//g)
988 E
159
404
27 J
43.7
90.9
114
26 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G40
-------
WST2S1.D
SAMPLErWS MM5G Filters 65,66,69,70 dishes 5,7 {Composite of four Extracts)
MS FILE :WST2S1.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 27 Nov 95 4:07
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene{surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-Terphenyl(surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
'henanthrene
Anthracene
:luoranthene
Pyrene
Chrysene
Benzo(a)anthracene
3enzo(b)fluoranthene
7,1 2-Dtmethylbenz(a)anthracene
Jenzo(k)fluoranthene
3enzo(a)pyrene
3-methyleholanthrene
ndenod ,2,3-cdSpyrene
)ibenz(a,h)anthracene
Benzo(ghi)perylene
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
MDL
24.2
20
15,8
17.2
16.6
11
11.8
6.4
6.6
4.6
4.8
10.4
14
5.6
12.4
12.8
10.4
5
4
P/F
F
F
F
F
F
F
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
|
PQL
200
amount (fjg)
ND
ND
ND
ND
ND
ND
29 J
ND
106 J
161 J
27 J
37 J
51 J
ND
21 J
45 J
ND
29 J
ND
38 J
G41
-------
WST2S2.D
SAMPLE:WS MM5G Filters 67,68,71,72 dishes 6,8 (composite of four extracts)
MS FILE :WST2S2.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST; Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 27 Nov 95 6:02
System Monitoring Compounds
2-Fluorophenol(surr#1 }
D6-Phenol{surr#2!
D5-Nitrobenzene(surr#3)
2-FIuorobiphenyI(surr#4)
2,4,6-tribromophenoI(surr#5)
D 1 4-Terphenyl (surr#6!
Extract
Volume
Dilution
5
4
|
|
ml
X
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
P/F
F
F
F
F
F
F
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
1
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
>ibenzofuran
:luorene
Phenanthrene
Anthracene
:!uoranthene
'yrene
Chrysene
3enzo(a)anthracene
Benzo(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
Benzo(a)pyrene
i-methylcholanthrene
Indenod ,2,3-cd)pyrene
3ibenz{a,h)anthracene
tenzo(ghi)perylene
I
MDL
24.2
20
15.8
17.2
16.6
11
11.8
6.4
6.6
4.6
4.8
10.4
14
5.6
12.4
12.8
10.4
PQL
200
amount (//g)
ND
ND
ND
ND
ND
ND
ND
ND
68 J
110 J
25 J
32 J
44 J
ND
ND
45 J
ND
23 J
ND
31 J
G42
-------
WSTT3S1 .XLS
SAMPLE: Test 3 System 1 XAD
MS FILE :WSTT3S1.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 13 Dec 95 11:52
System Monitoring Compounds
2-FIuorophenoI(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-TerphenyI(surr#6)
Extract
Volume
Dilution
5
1
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
P/F
NS
NS
NS
NS
NS
NS
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
I ;
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Jibenzofuran
:luorene
3henanthrene
Anthracene
:luoranthene
3yrene
Chrysene
lenzo(a)anthracene
Benzo(b)fluoranthene
7,1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
Benzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cdlpyrene
)ibenz(a,h)anthracene
3enzo{ghi)perylene
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
amount (fig)
841 E
128
299
21 J
48 J
76.5
178
40 J
7.8 J
6.6 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G43
-------
WST3S1.XLS
SAMPLE: WS Filters 61 and 62 Dish 90 {Composite of Two Extracts)
MS FILE :WST3S1.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 28 Nov 95 10:57
System Monitoring Compounds
2-FluorophenoI(surr#1 )
D6-Phenoi(surr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-TerphenylSsurr#6j
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
3ibenzofuran
:luorene
*henanthrene
Anthracene
:luoranthene
3yrene
Chrysene
Benzo(a)anthracene
Jenzo(b)fluoranthene
7, 1 2-Dimethylbenz{a)anthracene
Benzo(k)fluoranthene
lenzo(a)pyrene
i-methylcholanthrene
lndeno(1,2,3-cd)pyrene
Dibenzja,h)anthracene
3enzo(ghi)perylene
Extract
Volume
Dilution
5
ml
2|X
QS # 6 just below 50% Criterion
% Recovery
Not Spiked
Not Spiked
Not Spiked^
Not Spiked
Not Spiked
Not Spiked
P/F
F
F
F
F
F
F
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
MDL
12.1
10
7.9
8.6
8.3
5.5
5.9
3.2
3.3
2.3
2.4
5.2
7
2.8
6.2
6.4
5.2
POL
100
amount (/ug)
ND
ND
ND
ND
ND
ND
21 J
ND
85 J
143
25 J
32 J
45 J
ND
17 J
43 J
ND
28 J
ND
38 J
G44
-------
WSTT3S2.XLS
SAMPLE: i Test 3 System 2 XAD
MS FILE :WSTT3S2.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 13 Dec 95 13:44
System Monitoring Compounds
2-Fluorophenol{surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D14-Terphenyl(surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
3ibenzofuran
:luorene
*henanthrene
Anthracene
:luoranthene
Pyrene
Chrysene
Benzo(a)anthracene
Benzofblfluoranthene
7, 1 2-Dimethylbenz(a)anthracene
3enzo(k)fluoranthene
Benzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
3ibenz(a,h)anthracene
Benzo{ghijperylene
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
P/F
NS
NS
NS
NS
NS
NS
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
amount (//g)
L 1260E
180
414
30 J
64.2
102
202
47 J
14 J
12 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G45
-------
WST3S2.XLS
SAMPLE: WS Filters 63 and 64 Dish 10 {Composite of Two Extracts)
MS FILE :WST3S2.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 28 Nov 95 1 1 :58
System Monitoring Compounds
2-Fluorophenol(surrf 1 )
D6-Phenol«surr#2)
D5-Nitrobenzene(surr#3j
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-Terphenyl(surr#6)
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
i
2
P/F
F
F
F
F
F
F
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
I
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
Phenanthrene
Anthracene
:luoranthene
Jyrene
Chrysene
Benzo(a)anthraeene
Benzo(b)fluoranthene
7,1 2-Dimethylbenz(a)anthracene
Jenzo(k)fluoranthene
lenzo(a)pyrene
i-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz{a,h)anthracene
3enzoighi)perylene
MDL
12.1
10
7.9
8.6
8.3
5.5
5.9
3.2
3.3
2.3
2.4
5.2
7
2.8
6.2
6.4
5.2
PQL
100
amount (fjg)
ND
ND
ND
ND
ND
ND
21 J
ND
55 J
103
17 J
22 J
28 J
ND
12 J
26 J
ND
17 J
ND
21 J
G46
-------
WST4SYS2.XLS
SAMPLE: . . Test 4 System 1 XAD
MSFILE:WST4SYS1.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST; Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 22 Jan 96 2:41
System Monitoring Compounds
2-FluorophenoHsurr#1 }
D6-Phenolfsurr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-Terphenyl(surr#6)
Target Compounds
Naphthalene
2-methylnaphthaIene
Acenaphthylene
Acenaphthene
3ibenzofuran
•luorene
Phenanthrene
Anthracene
:luoranthene
Pyrene
Chrysene
Benzo(a)anthracene
Benzo(b)fluoranthene
7, 1 2-DimethyIbenz
-------
WST4S1.D
SAMPLE: WS MM5G Filters 77,78,81,82 and dishes 11 and 13 (Composite of Fo
MS FILE :WST4S1.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 27 Nov 95 2:01
System Monitoring Compounds
2-Fluorophenol{surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene{surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol{surr#5)
D1 4-Terphenyt(surr#6)
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
4
ml
X
P/F
F
F
F
F
F
F
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
i
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
Phenanthrene
Anthracene
Fluoranthene
'yrene
Chrysene
3enzo(a)anthracene
3enzo(b)fluoranthene
7,1 2-Dimethylbenz(a)anthraeene
Benzo{k)fluoranthene
ienzo(a)pyrene
3-methyIcholanthrene
Indenod ,2,3-ed)pyrene
)ibenz(a,h)anthracene
Benzo(ghi)perylene
MDL
24.2
20
15.8
17.2
16.6
11
11.8
6.4
6.6
4.6
4.8
10.4
14
5.6
12.4
12.8
10.4
PQL
200
amount (#g)
ND
ND
ND
ND
ND
ND
69 J
ND
94 J
133 J
28 J
34 J
36 J
ND
ND
37 J
ND
ND
ND
26 J
G48
-------
WSTDT4S2.XLS
SAMPLE: Test 4 System 2 XAD
MS FILE :WSTDT4S2.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 14 Dec 95 11:54
System Monitoring Compounds
2-FluorophenoI(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene{surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D14-Terphenyl(surr#6)
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
P/F
NS
NS
NS
NS
NS
NS
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
i
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
3ibenzofuran
:Iuorene
'henanthrene
Anthracene
Fluoranthene
Pyrene
Chrysene
3enzo(a)anthracene
Jenzo(b)fluoranthene
7,1 2-Dimethylbenz(a)anthracene
5enzo(k)fluoranthene
5enzo(a)pyrene
3-methyIchoIanthrene
lndeno(1,2,3-cd)pyrene
Dibenz{a,h)anthracene
3enzo(ghi)perylene
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
POL
50
amount (//g)
1110 E
157
352
24 J
47 J
71.0
67.8
15 J
5.4 J
5.4 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G49
-------
WST4S2.D
SAMPLE:WS MM5G Filters 79, 80, 83, 84 Dishes 12,14 {Composite of Four Extr
MS FILE :WST4S2,D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 27 Nov 95 3:01
System Monitoring Compounds
2-Fluorophenoi(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-FIuorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-TerphenyI(surr#6!
Extract
Volume
Dilution
5
4
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
P/F
F
F
F
F
F
F
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:Iuorene
'henanthrene
Anthracene
:luoranthene
Pyrene
Chrysene
3enzo(a)anthracene
Benzo(b)fluoranthene
7,1 2-Dimethylbenz(a)anthracene
3enzo(k)fluoranthene
3enzofa)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
)ibenz(a,h)anthracene
Jenzo(ghi)perylene
MDL
24.2
20
15.8
17.2
16.6
11
11.8
6.4
6.6
4.6
4.8
10.4
14
5.6
12.4
12.8
10.4
PQL
200
amount (fjg)
ND
ND
ND
ND
ND
ND
71 J
21 J
104 J
145 J
24 J
31 J
39 J
ND
ND
39 J
ND
23 J
ND
31 J
G50
-------
WST5BKS1.XLS
SAMPLE: Test 5 System 1 XAD Blank
MS FILE ;WST5BKS1.D
|
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 17 Jan 96 15:29
System Monitoring Compounds
2-Fluorophenol{surr^1 }
D6-Phenoi{surr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D14-Terphenyl(surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Jibenzofuran
:luorene
Phenanthrene
Anthracene
:luoranthene
3yrene
Chrysene
3enzo{a)anthracene
Benzo(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
Benzo(a!pyrene
3-methyIcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
5enzo(ghi)perylene
Extract
Volume
Dilution
.
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
1
P/F
NS
NS
NS
NS
NS
NS
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
50
50
amount (//g)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G51
-------
WST5S1.XLS
SAMPLE:WS Filters 85 and 86
MS FILE :WST5S1.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 28 Nov 95 2:37
System Monitoring Compounds
2-FluorophenoI(surr#1 )
D6-Pheno!(surr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5}
31 4-Terphenyl(surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acendphthylene
Acenaphthene
Dibenzofuran
:Iuorene
shenanthrene
Anthracene
:luoranthene
*yrene
Chrysene
Benzofajanthracene
3enzo(b)fluoranthene
7, 1 2-DimethyIbenz(a)anthracene
Benzo(k)fluoranthene
5enzo(a)pyrene
3-methylcholanthrene
lndeno(1,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
Extract
Volume
5
Dilution) 1
mi
X
QSs 1,3 and 4 were just below 50
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
P/F
F
F
F
F
F
F
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
!
PQL
50
amount (fjg]
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G52
-------
WSTDT5S2.XLS
SAMPLE: Test 5 System 2 XAD
MS FILE :WSTDT5S2.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 14 Dec 95 14:35
System Monitoring Compounds
2-Fluorophenol(surr#1 !
D6-Phenoi(surr#2)
D5-Nitrobenzene{surr#3)
2-Fluorobiphenyl (surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-Terphenyl!surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
rluorene
Phenanthrene
Anthracene
:luoranthene
3yrene
Chrysene
3enzo(a)anthraeene
Benzo(b)fluoranthene
7, 1 2-Dimethylbenz{aSantriracene
Benzofkjfluoranthene
3enzo{a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
ml
1|X
P/F
NS
NS
NS
NS
NS
NS
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
!
MDL
6.05
5
3.95
4,3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
amount {fjg)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G53
-------
WST5S2.XLS
SAMPLE:WS Filters 87 and 88
MS FILE :WST5S2.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 28 Nov 95 3:24
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-FluorobiphenyHsurr#4)
2,4,6-tribromophenol(surr#5)
D14-Terphenyl(surr#6)
Extract
Volume
Dilution
5
1
ml
X
QSs 1 ,3 and 4 were just below 50
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
P/F
F
F
F
F
F
F
;
Target Compounds
Naphthalene
2-methyInaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
'henanthrene
Anthracene
Fluoranthene
Pyrene
Chrysene
Senzo(a)anthracene
Benzo{b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
ienzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
)ibenz{a,h)anthracene
3enzo(ghi)perylene
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
amount (/jg)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
' ND
ND
ND
ND
ND
ND
G54
-------
Samples for The Emissions from Wood-Fired Residential Furnaces Project
Sample ID,
TCD-MM5G-X-1
TCD-MM5G-FA1-1
TCD-MM5G-FB1-1
TCD-MM5G-PR1-1
TCD-MM5G-2-F2
TCD-MM5G-2-F1
TCD-MM5G-2-PR
TCD-MM5G-X-2
Blank XAD
Blank Acetone
TCD-MM5G-FA-5
TCD-MM5G-FB-5
TCD-MM5G-PR-5
Furnace A with Catalyst
Date Sampled Compositing Date Analyzed MS File ID
10/26/95
10/26/95
10/26/95
10/26/95
10/25/95
10/25/95
10/25/95
10/25/95
10/26/95
10/26/95
10/26/95
10/26/95
10/26/95
none
Filters
and
Rinse
none
Filter and
Rinse
none
none
none
Filters
and
Rinse
11/24/95
11/24/95
11/22/95
11/27/95
11/21/95
11/24/95
11/24/95
11/22/95
WSX1DIL.D
WSFABP1D.D
WSTCD2F2.D
WS2F12PR.D
WSTCDX2.D
WSMM5GBK.D
WSMM5GAB.D
WSFAPB5.D
G55
-------
WSX1DIL.XLS
SAMPLE: WS MM5G XAD Low Burn X1
MSFILE:WSX1D!L.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
11/24/95 5:20
System Monitoring Compounds
2-Fluorophenol(surr#1 >
D6-Pheno!(surr#2)
D5-Nitrobenzene(surr#3S
2-Fluorobiphenyl(surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-Terphenyl(surr#6)
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
10
P/F
F
F
F
F
F
F
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
=luorene
'henanthrene
Anthracene
:luoranthene
3yrene
Chrysene
Benzo(a)anthracene
Benzo(b)fluoranthene
7,1 2-Dimethy!benz(a!anthracene
3enzo(k)fluoranthene
Benzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
3enzo{ghi)perylene
MDL
60.5
50
39.5
43
41.5
27,5
29.5
16
16.5
11.5
12
26
35
14
31
32
26
POT
500
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
amount (#g)
4960
650
1100
64 J
100 J
98 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G56
-------
WSTCDX2.XLS
SAMPLE: WS XAD High Burn MM5G
MS FILE :WSTCDX2.D
PROJECT: Woodstove
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 21 Nov 95 5:02
System Monitoring Compounds
2-Fluorophenol(surr#1 }
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobiphenyl(surrf4)
2,4,6-tribromophenol(surr#5)
D14-TerphenyI(surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
3henanthrene
Anthracene
:luoranthene
syrene
Chrysene
3enzo(a)anthracene
3enzo(b)ftuoranthene
7, 1 2-Dimethylbenz(a)anthracene
3enzo(k)fluoranthene
3enzo{a)pyrene
3-methylcholanthrene
ndenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
3enzo(ghi)perylene
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
MDL
24.2
20
15,8
17.2
16.6
11
11.8
6.4
6.6
4.6
4.8
10.4
14
5.6
12.4
12.8
10.4
I
5
4
P/F
F
F
F
F
F
F
PQL
200
I
ml
y-
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
amount (//g)
2370
321
461
25 J
30 J
26 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G57
-------
WSFABP1D.XLS
SAMPLE: WS MM5G Low Burn FA, FB and PR-1
MS FILE : WSFABP1D.D
PROJECT: Emissions from Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 24 Nov 95 3:09
System Monitoring Compounds
2-Fluoropheno!(surr#1 )
D6-Phenol(surr#2j
D5-Nitrobenzene(surr#3)
2-FluorobiphenyI{surr#4)
2,4,6-tribromophenol(surr#5)
D1 4-Terphenyl(surr#6}
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Chrysene
Benzo(a)anthracene
Benzo(b)fluoranthene
7, 1 2-Dimethylbenz(a)anthracene
Benzo(k)fluoranthene
Benzo(a)pyrene
3-methylcholanthrene
lndeno{1,2,3-cd)pyrene
Dibenz{a,h)anthracene
Benzo(ghi)perylene
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
MDL
18.15
15
11.85
12.9
12.45
8.25
8.85
4.8
4.95
3.45
3.6
7.8
10.5
4.2
9.3
9.6
7.8
5
3
P/F
F
F
F
F
F
F
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
PQL
150
amount {/JQ}
ND
ND
ND
ND
ND
68 J
653
168
318
457
82 J
94 J
105 J
ND
41 J
104 J
ND
51 J
ND
78 J
I
G58
-------
WSTCD2F2.XLS
SAMPLE: WS MM5G High Burn Back MeC12 Extract
MS FILE :WSTCD2F2.D
I
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 22 Nov 95 1 1 :04
System Monitoring Compounds
2-FluorophenoI{surr#1 }
D6-Phenol(surr#2)
D5-Nitrobenzene{surr#3)
2-FluorobiphenyI(surr#4)
2,4,6-tribromopheno!(surr#5)
D 1 4-TerphenyI(surr#6)
Target Compounds
Maphthalene
2-methyInaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
5henanthrene
Anthracene
:luoranthene
'yrene
Chrysene
Benzo(a)anthraeene
Benzo(b)fluoranthene
7,1 2-DimethyIbenz(a)anthracene
Benzo(k)fluoranthene
Benzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
BenzofghiSperylene
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
5
1
ml
X
P/F
F
F
F
F
F
F
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
PQL
50
amount (fjg)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
5 J
ND
5 J
6 J
ND
7 J
6 J
ND
G59
-------
WS2F12PR.XLS
SAMPLE;WS MM5G High Burn Front, Pan
MSF!LE:WS2F12PR.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 27 Nov 95 1 1 :51
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene{surr#3)
2-FIuorobiphenyl{surr#4)
2,4,6-tribromophenol{surr#5) _j
D1 4-Terphenyl(surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
5henanthrene
Anthracene
Fluoranthene
Pyrene
Chrysene
Benzo(a)anthracene
Benzo(b)fluoranthene
7,1 2-Dimethylbenz(a)anthracene
3enzo(k)fluoranthene
3enzo{a)pyrene
i-methylcholanthrene
Indenof 1 ,2,3-cd)pyrene
)ibenz(a,h)anthracene
3enzo(ghi)pery!ene
Extract
Volume
Dilution
% Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
MDL
12.1
10
7.9
8.6
8.3
5.5
5.9
3.2
3.3
2.3
2.4
5.2
7
2.8
6.2
6.4
5.2
5
2
P/F
F
F
F
F
F
F
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
PQL
100
amount {//gj
ND
ND
16 J
ND
ND
38 J
346
77 J
138
247
46 J
50 J
61 J
ND
20 J
55 J
ND
34 J
ND
41 J
G60
-------
WSMM5GBK.XLS
SAMPLE:WS MM5G Blank
MS FILE :WSMM5GBK.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 24 Nov 95 6:17
System Monitoring Compounds
2-Fluorophenol(surr#1 )
D6-Phenol{surr#2)
D5-Nitrobenzene(surr#3)
2-Fluorobtphenyl(surrf4)
2»4,6-tribromophenol(surrf5)
D14-Terphenyl(surr#6)
Extrac
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
i
Target Compounds
Naphthalene
2-methylnaphthaIene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
Phenanthrene
Anthracene
Fluoranthene
3yrene
Chrysene
Benzo{a)anthracene
Benzo(b)fluoranthene
7,12-Dimethylbenz(a)anthracene
Benzo{k)fluoranthene
Benzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h}anthracene
Benzo(ghi)perylene
MDL
6.05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
5
1
P/F
F
F
F
F
F
F
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
POL
50
amount (//g)
8 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G61
-------
WSMM56AB.XLS
SAMPLE:WS MM5G Acetone Blank
MS FILE ; WSMM5GAB.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED: 24 Nov 95 4:11
System Monitoring Compounds
2-F!uorophenol(surr#1 )
D6-Phenol{surr#2)
D5-Nitrobenzene{surr#3)
2-FIuorobiphenyI(surr#4)
2,4,6-tribromophenol(surr#5)
D14-Terphenyl(surr#6}
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
Fluorene
'henanthrene
Anthracene
:luoranthene
Pyrene
Chrysene
Jenzo{a)anthracene
Benzo|b)fluoranthene
7, 1 2-Dimethylbenz(a)anthraeene
3enzo{k}fluoranthene
Benzo(a)pyrene
3-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
ienzo(ghi)perylene
Extract
Volume
Dilution
5
1
ml
X
All Internal Standards Below 50%
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
P/F
F
F
F
F
F
F
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
MDL
6,05
5
3.95
4.3
4.15
2.75
2.95
1.6
1.65
1.15
1.2
2.6
3.5
1.4
3.1
3.2
2.6
PQL
50
amount (fjg)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G62
-------
WSFAPB5.XLS
SAMPLE: WS MM5G Front, Back and Pan Rinses MecL2 Extract
MS FILE :WSFAPB5.D
PROJECT: Emissions From Wood-Fired Residential Heating Furnaces
ANALYST: Bill Preston
ANALYTICAL METHOD: SW-846-8270
ACQUIRED; 22 Nov 95 11:51
System Monitoring Compounds
2-FluorophenoI(surr#1 )
D6-Phenol(surr#2)
D5-Nitrobenzene(surr#3}
2-FIuorobiphenyl(surr#4)
2,4,6-tribromophenoI(surr#5)
D 1 4-Terphenyl(surr#6)
Target Compounds
Naphthalene
2-methylnaphthalene
Acenaphthylene
Acenaphthene
Dibenzofuran
:luorene
'henanthrene
Anthracene
:Iuoranthene
5yrene
Chrysene
3enzo(a)anthracene
Benzo(b)fluoranthene
7,1 2-Dimethylbenzia)anthracene
Benzo(k)fluoranthene
3enzo(a)pyrene
i-methylcholanthrene
Indenod ,2,3-cd)pyrene
Dibenz{a,h)anthracene
3enzo(ghi)perylene
Extract
Volume
Dilution
%Recovery
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
Not Spiked
5
%
P/F
F
F
F
F
F
F
MDL
18.15
15
11.85
12.9
12.45
8.25
8.85
4.8
4.95
3.45
3.6
7.8
10.5
4.2
9.3
9.6
7.8
PQL
150
ml
X
LIMITS
21-100
10-94
35-114
43-116
10-123
33-141
amount (//g)
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
G63
-------
TECHNICAL REPORT DATA
(Please read Instructions on the reverse before completing)
1. REPORT NO.
EPA-600/R-98-017
2.
3. RECIPIENT'S ACCESSION NO.
4. TITLE AND SUBTITLE
Emissions from Outdoor Wood-burning Residential
Hot Water Furnaces
5. REPORT DATE
February 1998
6. PERFORMING ORGANIZATION CODE
7. AUTHOR(S)
Joseph C.
Valenti and Russell K. Clayton
8. PERFORMING ORGANIZATION REPORT NO.
9. PERFORMING ORGANIZATION NAME AND ADDRESS
Acurex Environmental Corporation
P. O. Box 13109
Research Triangle Park. North Carolina 27709
10. PROGRAM ELEMENT NO.
It. CONTRACT/GRANT NO.
68-D4-0005, Tasks 1-043
and 2-041
12. SPONSORING AGENCY NAME AND ADDRESS
13. TYPE OF REPORT AND PERIOD COVERED
EPA, Office of Research and Development
Air Pollution Prevention and Control Division
Research Triangle Park, NC 277U
Final; 12/94- 3/96
14. SPONSORING AGENCY CODE
EPA/600/13
16.SUPPLEMENTARY NOTES AppcD project officer is Robert C. McCrillis, Mail Drop 61,
919/541-2733.
16. ABSTRACT
repOrt gives results of measurements of emissions from a single- pass
and a double- pass furnace at average heat outputs of 15,000 and 30,000 Btu/hr (4.4
and 8. 8 kW) while burning typical oak eordwood fuel. One furnace was also tested
once at each heat output while fitted with a prototype catalytic unit installed in the
combustion chamber. Emissions measured included: EPA Method 5G particulate,
semivolatile and condensible organics, 20 target polycyclic aromatic hydrocarbon
(PAH) compounds, and carbon monoxide. Emission results are presented in terms
of rate per hour, quantity per unit weight of wood burned, and quantity per unit of
heat delivered. Delivered efficiencies are also presented. Compared to a wide range
of residential heating options, these furnaces' emissions were of the same order as
other stick wood burning appliances. (NOTE: Modern outdoor residential wood- bur-
ning hot water furnaces are freestanding units situated outside the envelope of the
structure to be heated. They typically consist of a firebox and water reservoir, as-
sembled in a horizontal configuration. Hot combustion gases flow from the firebox
at one end, through channels or tubes in the water reservoir, to the stack. The gas-
es may pass through the water reservoir once to the stack at the end opposite the
firebox (one phase), or they may make two passes through the water reservoir.
17.
KEY WORDS AND DOCUMENT ANALYSIS
DESCRIPTORS
b.!DENTIFIERS/OPEN ENDED TERMS
c. COSATI Field/Group
Pollution Measurement
Hot Water Heating Catalysis
Residential Buildings
Oak Wood
Combustion
Emission
Pollution Control
Stationary Sources
13B
ISA
13M
11L
21B
14G
07D
18. DISTRIBUTION STATEMENT
Release to Public
19. SECURITY CLASS (This Report}
Unclassified
21. NO. OF PAGES
218
20. SECURITY CLASS {This page)
Unclassified
22. PRICE
EPA Form 222CM (9-73)
G64
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