xvEPA
United States
Environmental Protection
Agency
Industrial Environmental Research
Laboratory
Research Triangle Park NC 27711
EPA-600/7-81 -095b
May 1981
Thirty-day Field Tests
of Industrial Boilers:
Site 6 Gas-fired
Fire-tube Boiler
/
Interagency
Energy/Environment
R & D Program Report
-------
RESEARCH REPORTING SERIES
Research reports of the Office of Research and Development, U.S. Environmental
Protection Agency, have been grouped into nine series. These nine broad cate-
gories were established to facilitate further development and application of en-
vironmental technology. Elimination of traditional grouping was consciously
planned to foster technology transfer and a maximum interface in related fields.
The nine series are:
1. Environmental Health Effects Research
2. Environmental Protection Technology
3. Ecological Research
4. Environmental Monitoring
5. Socioeconomic Environmental Studies
6. Scientific and Technical Assessment Reports (STAR)
7. Interagency Energy-Environment Research and Development
8. "Special" Reports
9. Miscellaneous Reports
This report has been assigned to the INTERAGENCY ENERGY-ENVIRONMENT
RESEARCH AND DEVELOPMENT series. Reports in this series result from the
effort funded under the 17-agency Federal Energy/Environment Research and
Development Program. These studies relate to EPA's mission to protect the public
health and welfare from adverse effects of pollutants associated with energy sys-
tems. The goal of the Program is to assure the rapid development of domestic
energy supplies in an environmentally-compatible manner by providing the nec-
essary environmental data and control technology. Investigations include analy-
ses of the transport of energy-related pollutants and their health and ecological
effects; assessments of, and development of, control technologies for energy
systems; and integrated assessments of a wide range of energy-related environ-
mental issues.
EPA REVIEW NOTICE
This report has been reviewed by the participating Federal Agencies, and approved
for publication. Approval does not signify that the contents necessarily reflect
the views and policies of the Government, nor does mention of trade names or
commercial products constitute endorsement or recommendation for use.
This document is available to the public through the National Technical Informa-
tion Service, Springfield, Virginia 22161.
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EPA-600/7-81-095b
May 1981
Thirty-day Field Tests
of Industrial Boilers:
Site 6Gas-fired Fire-tube Boiler
by
W.A. Carter and H.J. Buening
KVB, Inc.
P.O. Box 19518
Irvine, California 92714
Contract No. 68-02-2645
Task No. 4
Program Element No. C9BN1B
EPA Project Officer: Robert E. Hall
Industrial Environmental Research Laboratory
Office of Environmental Engineering and Technology
Research Triangle Park, NC 27711
Prepared for
U.S. ENVIRONMENTAL PROTECTION AGENCY
Office of Research and Development
Washington, DC 20460
n,^, MDvlronfflfiTitaT Protects
u \ .', Ub'i "->/ 7 f f)7Jj-J',;
-------
ABSTRACT
This is a final report on a test program to evaluate the long-term
effectiveness of combustion modifications on industrial boilers. During
previous programs, short-term tests have been performed on industrial boilers
to determine the effect of combustion modifications on air pollutant emissions
such as NO , SO , CO, HC and particulate matter. The objective of this
X X
program was to determine whether combustion modification techniques which were
effective for short duration tests are feasible for a longer period. This
report presents results of a long duration field test of a 200 HP firetube
boiler using low excess air as the NOX control technology. The field test was
conducted with the unit firing natural gas and with the normal duty cycle.
The mean NO level for the 24-day test period was 29.5 ng/J with a geometric
dispersion of 1.05.
ii KVB11-6017-1266
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CONTENTS
SECTION PAGE
1.0 SUMMARY 1
1.1 Objective and Scope 1
1.2 Results 1
1.3 Conclusions 2
2.0 INSTRUMENTATION AND PROCEDURES 6
2.1 Emissions Measurement Instrumentation 6
2.2 Boiler Description and Characteristics 12
2.3 Daily Test Activity 14
3.0 TEST RESULTS 16
3.1 Continuous Monitor Certification Tests 16
3.2 Firetube Boiler Tests 19
4.0 REFERENCES 27
APPENDIX A 28
APPENDIX B 35
APPENDIX C 53
APPENDIX D 72
APPENDIX E 88
APPENDIX F 103
iii KVB11-6017-1266
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TABLES
TABLES PAGE
1-1 Summary of 24-hour Average Gaseous Emission 3
2-1 Analytical Instrumentation 8
2-2 Schedule of Daily Events - Site 6 15
3-1 Schedule of Certification Test Events 17
3-2 Instrument Specifications and Performance 18
3-3 24-hour Data - Dry Stack Gas Concentration 24
iv KVB11-6017-1266
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FIGURES
FIGURE PAGE
1-1 Log-Probability Plot of NO Emissions from a Firetube Boiler 4
2-1 Photograph of KVB Continuous Monitor for Measuring Gaseous 7
Emissions
2-2 Schematic of Continuous Monitor Sampling and Conditioning 9
System
2-3 Firetube Boiler (Typical) 13
3-1 Strip Chart Record of NO and 0_ Analyzer Output 21
3-2 Average Daily Thermal Input for Site 6 22
3-3 Average Daily NO Emissions for Site 6 23
3-4 Log-Probability Plot of NO Emissions from a Firetube 26
Boiler
KVBll-6017-1266
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SECTION 1.0
SUMMARY
1.1 OBJECTIVE AND SCOPE
The objective of this field test was to determine whether combustion
modification techniques which demonstrated reductions on air pollutant
emission during short term tests are feasible for longer periods. In
addition, boiler performance and reliability were monitored. The combustion
modifications have previously been shown to be effective on industrial boilers
(Refs. 1, 2, 3).
The program scope provides for 30-day field tests of a total of seven
(7) industrial boilers with design capacities ranging from 14.65 to 73.25 MW
output (50,000 to 250,000 Ib steam/hr). Fuels to be burned include natural
gas, light oil, residual oil, and coal. This final report is for a 200 HP
(6,900 Ib steam/hr), natural gas fired firetube boiler using low excess air
(LEA) as the emission control technology.
During the test period, continuous monitor certification tests were
performed concurrent with low NOX testing. Gaseous emissions measured were:
NO, CO, CO2 and O_. Particulate matter were not measured at this test site.
Boiler efficiency was calculated for several conditions during the program.
This report documents the test equipment and procedures, summarizes
the test data and discusses the data in relation to the control technology
employed for this boiler.
1.2 RESULTS
A natural gas-fired firetube boiler using low excess air (LEA) as the
control technology was selected for this field test. Selection of a firetube
boiler for testing was the result of recommendations from the American Boiler
Manufacturers Association and the EPA. It was felt that this type of
industrial boiler represented a large portion of the boiler population and it
1 KVB11-6017-1266
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was necessary to demonstrate feasibility of long-term implementation of NO
X
control on this type equipment.
The boiler selected for testing at Site 6 had previously been tested
by KVB under EPA Contract No. 68-02-1074 (Ref. 2). The short duration tests
conducted during the previous program had demonstrated a capability of
operating under low NO conditions. A previous program (Ref. 4) presented a
X
boiler survey and analysis performed to determine the population and
distribution of industrial boilers. This study showed that nationally
firetube boilers in the 10-16 MBtu/hr category account for 24 percent of the
total number of boilers and 8 percent of the total installed capacity.
After selection of the test site a continuous monitor was shipped to
the test site and installed. The next task was to perform monitor
certification tests as outlined in Performance Specification 2 and 3, 40CFR60,
Appendix B (See Appendix D). The monitor certification tests were performed
at the initiation of the test period and constituted the first part of the
long duration test.
The results of the long duration test are discussed in detail in
Section 3.0. A summary of the 24-hour average of gaseous emissions is
presented in Table 1-1. This table was compiled from the output of a data
logger which records 15-minute averages of gaseous emissions. An analysis of
the field test data was also conducted. Figure 1-1 presents a log-probability
plot of 24-hour averages of NO emissions. These data show that the mean NO
emission rate is 29.5 ng/J with a geometric dispersion of 1.05. This figure
also shows that 95 percent of-the NO measurements are less than 31.5 ng/J.
1.3 CONCLUSIONS
Based on the results of this long-duration test, several important
conclusions can be drawn.
1. Low excess air (LEA) is an effective NOX control
technology for the natural gas fired firetube boiler. The
LEA condition was maintained for 24 days with mean NO
emission level of 29.5 ng/J (53 ppm @ 3 percent O-, dry)
with a geometric dispersion of 1.05. The low NO
X
condition was maintained for the entire test period
2 KVB11-6017-1266
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TABLE 1-1. SUMMARY OF 24-HOUR AVERAGE GASEOUS EMISSIONS
**
ft
**
**
ft*
ft
LOAD
DATE TIME MWTH
?a HOUR DATA
DRY STACK GAS CONCENTRATION
02 C02 CO NO CO
VOIX VOLX PPHV PPMV PpMV
MEAS MEAS MEAS MEAS 3X02
NO
PPMV
3102
CO
NG/J
NO
NG/J
**
**
**
**
**
**
A********************************************************************************
**
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ft
ft
*
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**
**
*
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ft*
ft*
ft*
ft*
ft*
**
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ft*
**
**
ft*
*
ft*
**
**
*
8/ 5/60
B/ 6/60
8/ 7/80
8/ 8/80
8/12/80
8/13/80
e/ia/eo
e/is/80
8/18/80
8/19/80
6/20/80
8/21/80
8/22/80
8/25/80
8/26/80
8/27/80
8/28/80
8/29/80
9/ 2/80
9/ 3/80
V a/8o
9/ 5/80
9/ 8/80
9/ 9/80
9/10/80
9/11/80
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KVBll-6017-1266
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SITE 6 - Gas Fired Fire Tube Boiler ~~
__ Rated Capactiy: 250 HP
Fuel : Natural Gas
~
.|L1|i|
I =
~
_ -o -° °~" ° "
_ NO = 29.5 ng/J
g.d.= 1.05
1 1 1 1 1 II 1 1 1 1 1 1 1 II 1 1 I I I
31.05 .1.2 .51 2 10 20 30 40 50 60 70 80 90 95 98 99 99.8 99.9 99.9'
PERCENT LESS THAN
Figure 1-1. Log-Probability plot of NO Emissions from a firetube boiler.
-------
despite the extreme cyclic nature of the boiler
operation. The boiler often cycled from high fire to low
fire conditions in less than 15 minutes.
2. Boiler operation in the low NOX mode presented no
reliability or functional problems. The LEA mode can be
maintained for extended periods providing adequate
instrumentation and display are provided. An
indoctrination and training period for operators is
recommended.
3. The continuous monitor system utilizing an extractive
sampling system provided accurately reliable data for the
entire test period. Calibration of the instruments on a
daily basis is necessary as is maintenance of the sample
system.
4. The cyclic operation of this boiler is typical of a large
number of industrial boilers. An effective control
technology must be capable of operation over large load
changes.
KVB11-6017-1266
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SECTION 2.0
INSTRUMENTATION AND PROCEDURES
This section presents a description of the instrumentation used to
measure the gaseous emissions, the test procedures, and techniques for
certifying the continuous monitor and a description of the boiler tested.
2.1 EMISSIONS MEASUREMENT INSTRUMENTATION
The emissions measurements were made using a continuous monitor
fabricated by KVB for this program. The analytical instrumentation and sample
handling equipment are contained in a cabinet 1.2 m wide x 0.76 m deep x
1.83 m high (48"W x 30"D x 72"H). A photograph of the continuous monitor is
shown in Figure 2-1. Gaseous emission measurements were made with the
analytical instruments listed in Table 2-1.
2.1.1 Gaseous Emissions
The continuous monitor is equipped with analytical instruments to
measure concentrations of NO, CO, CO2, and 02« The sample gas is delivered to
the analyzers at the proper condition and flow rate through the sampling and
conditioning system shown schematically in Figure 2-2. A probe with a 0.7
micrometer sintered stainless steel filter was installed in the stack to
sample the flue gas. The following paragraphs describe the analytical
instrumentation.
A. Nitrogen Oxides
The oxides of nitrogen monitoring instrument was a Thermo Electron
chemiluminescent nitric oxide analyzer. The operational basis of the
instrument is the chemiluminescent reaction of NO and O^ to form NO in an
excited state. Light emission results when excited NO2 molecules revert to
their ground state. The resulting chemiluminescence is monitored through an
optical filter by a high sensitivity photomultiplier tube, the output of which
KVB11-6017-1266
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NOx
Figure 2-1. Photograph of KVB continuous monitor for measuring gaseous emissions.
KVBll-6017-1266
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TABLE 2-1. ANALYTICAL INSTRUMENTATION
Measurement
Emission Species Manufacturer Method Model No.
Nitrogen Oxides Thermo Electron Chemiluminescent 10A
Oxygen Beckman Instrument Polarographic 742
Carbon Dioxide Horiba Instrument NDIR PIR-2000
Carbon Monoxide Horiba Instrument NDIR PIR-2000
KVB11-6017-1266
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I
-------
is electronically processed so it is linearly proportional to the NO
concentration.
Air for the ozonator is drawn from ambient through an air dryer and a
10-micrometer filter element. Flow control for the instrument is accomplished
by means of a small bellows pump mounted on the vent of the instrument
downstream of a separator which insures that no water collects in the pump.
The basic analyzer is sensitive only to NO molecules. To measure NO
X
(i.e., NO + NO-), the N02 is first converted to NO. This is accomplished by a
converter which is included with the analyzer. The conversion occurs as the
gas passes through a thermally insulated, resistance heated, stainless steel
coil. With the application of heat, NO2 molecules in the sample gas are
reduced to NO molecules, and the analyzer then reads NO . NO0 is obtained by
X ^
the difference in readings obtained with and without the converter in
operation.
Specifications
Accuracy: 1% of full scale
Span drift; ± 1% of full scale in 24 hours
Zero drift: ± 1 ppm in 24 hours
Power requirements: 115 + 10V, 60 Hz, 1000 watts
Response: 90% of F.S. in 1 sec (NOX mode); 0.7 sec (NO
mode)
Output: 4-20 ma
Sensitivity: 0.5 ppm
Linearity: ± 1% of full scale
Vacuum detector operation
Range: 2.5, 10 25, 100, 250, 1000, 2500, 10,000 ppm F.S.
Only the NO concentration was measured during this program. Because
of the added complexity of heated sample lines and controllers necessary for
measuring NO and the small percentage of NO2 in the flue gas, based on
10 KVB11-6017-1266
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previous tests (Ref. 1, 2 and 3) EPA decided that only NO measurement was
necessary. Therefore, an unheated sample line was installed and the moisture
was removed from the sample gas by a drop out flask and a refrigerated
condenser.
B. Carbon Monoxide and Carbon Dioxide
Carbon monoxide (CO) and carbon dioxide (C0_) concentrations were
measured by Horiba Instruments PIR-2000 short path length nondispersive
infrared analyzers. These instruments measure the differential in infrared
energy absorbed from energy beams passed through a reference cell (containing
a gas selected to have minimal absorption of infrared energy in the wave
length absorbed by the gas component of interest) and a sample cell through
which the sample gas flows continuously. The differential absorption appears
as a reading on a scale of zero to 100 percent and is then related to the
concentration of the species of interest by calibration curves supplied with
the instrument. A linearizer was supplied with the CO analyzer to provide a
linear output over the range of interest. The operating ranges for the CO
analyzer are zero to 500, zero to 1000, and zero to 2000 ppm, and the ranges
for the CO2 analyzer are zero to 5, zero to 10, and zero to 20 percent.
Specifications
Accuracy:
Repeatability:
Zero drift:
Span drift:
Response time:
1% of full scale
± 0.5% of full scale
+ 1% of full scale in 24 hours
± 1% of full scale in 24 hours
selectable - 90% of full scale in 0.5, 1.2, 3, or
5 seconds
Power requirements: 115 VAC + 10%, 60 Hz
Warm up time: 30 minutes
Output: 0-10 MV
11
KVB11-6017-1266
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C. Oxygen
A Beckman Model 742 oxygen analyzer was used to continuously determine
the oxygen content of the flue gas sample. The oxygen measuring element
contains a silver anode and gold cathode that are protected from the sample by
a thin membrane of Teflon. An aqueous KCL solution is retained in the sensor
by the membrane and serves as an electrolytic agent. As Teflon is permeable
to gases, oxygen will diffuse from the sample to the cathode in the following
oxidation-reduction reaction:
Cathode reaction: 0- + 2H-O + 4e 4OH
Anode reaction: 4Ag + 4C1 » 4AgCl + 4e
With an applied potential between the cathode and anode, oxygen will
be reduced at the cathode causing a current to flow. The magnitude of this
current is proportional to the partial pressure of oxygen present in the
sample. The instrument has operating ranges of zero to 1 percent, zero to 10
percent, and zero to 25 percent oxygen.
Specifications
Accuracy: ± 1% full scale or ± 0.05% CL whichever is greater
Sensor stability: ± 1% of full scale per 24 hours
Response time: 90% in 20 seconds
Output: 0-10 MV
Power requirement: 120 + 10 VAC, 60 Hz
2.2 BOILER DESCRIPTION AND CHARACTERISTICS
The boiler at Site 6 was manufactured by Kewanee Division of-American
Standard. The nameplate rating of the unit is 200 HP (6695 MBH, 2.0 MW).
The boiler is of the scotch-type design wherein the combustion takes place in
a cylindrical furnace within the shell. Firetubes run the length of the shell
at the sides of and above the internal furnace. Gas from the furnace reverses
direction in a chamber at the rear and travels forward through the tubes to
the smokebox.
12 KVB11-6017-1266
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The firetube boiler at location 6 is a dryback 3-pass design, with a
refractory-lined rear chamber.
iii
Figure 2-3. Firetube Boiler (Typical)
Figure 2-3 shows the typical arrangement of a scotch-type firetube
boiler. The tested unit was self-contained with a forced draft system that
supplied combustion air at the required pressure to the burner. In the
burners chamber the fresh boiler room air was directed through a diffuser
plate and then mixes with the fuel. Metering of fuel and air was automatic
and changed with load demand. The unit was equipped with a combination oil
and gas burner. During the test program only natural gas was burned in a ring
burner. Maximum working pressure for steam is 15 Ib and for water is 30 Ib.
The maximum firing range was 8370 MBtu.
The unit was installed in a large photo developing laboratory and was
used to generate hot water for film processing during the hours of 5 a.m. and
approximately 9 p.m. on workdays.
The boiler was off line from approximately 11:00 p.m. until 5:00 a.m.
each day. The operation of the unit was very cyclic, with occasional firing
from high to low within 15 minutes.
13
KVB11-6017-1266
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2.3 DAILY TEST ACTIVITY
This section describes the daily test activity at Site 6 following the
monitor certification tests. The schedule of monitor certification test
events is presented in Section 3.1. A schedule of daily events is presented
in Table 2-2.
The data from the gaseous analyzers (NO, CO, CO-» and 0_) were
continuously recorded on strip chart recorders and an automatic data logger.
Gaseous data were read five times daily by a technician and recorded on the
form shown in Figure B-2, Appendix B. Boiler control room data were recorded
five times daily by the KVB technician. The gaseous emissions data were
recorded only during an eight hour shift, but the strip chart recorders and
data logger recorded the data 24 hours per day 7 days per week. No control
room data were recorded during the week-ends, however, the technician did
calibrate the instruments during the week-end.
Daily tasks consisted of 1) calibration and recording data,
2) consultation with operators to assure operation in the low NOX mode,
3) periodic maintenance of instruments and sample system, 4) visual inspection
and trouble shooting of sampling system and instrumentation console, and
5) procuring supplies and equipment for the particulate and Method 7 tests.
14 KVB11-6017-1266
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TABLE 2-2. SCHEDULE OF DAILY EVENTS - SITE 6
Time Event
0800 Calibrate (zero and span) gaseous
analyzers (NO, CO_, CO, and O^)
Record gaseous emissions data. Record
boiler control room data. Consult with
operators concerning boiler operation.
0900 Perform daily systems checkout.
1000 Calibrate and record gaseous emissions
data.
1200 Calibrate and record gaseous emissions
data. Record control room data.
1400 Calibrate and record gaseous emissions
data.
1600 Calibrate and record gaseous emissions
data. Record control room data.
1700 Calibrate analyzers prior to departing
plant. Perform visual check of
sampling systems and boiler
operation. Leave instructions with
operators.
15 KVBll-6017-1266
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SECTION 3.0
TEST RESULTS
This section summarizes the emission and efficiency data collected on
the natural gas fired firetube boiler. The boiler was tested in the as-found
condition initially and for 26 days in the low NOV condition. The tests were
Jx
conducted with Southern California natural gas as the fuel. The results
presented herein summarize the gaseous emissions data, efficiency, and
conclusions for the boiler operating under low NOX conditions for extended
duration.
3.1 CONTINUOUS MONITOR CERTIFICATION TESTS
The continuous monitor described in the previous section was used to
measure the boiler gaseous emissions. Following shipment to the test site,
the monitoring system was installed and certification tests performed in
accordance with Performance Specification 2 (PS2) and 3 (PS3), 40 CFR 60,
Appendix B (see Appendix D). These establish minimum performance
specifications that the NO and O2/CO2 monitoring system must meet in terms of
eight parameters: accuracy, calibration error, two and 24 hour zero drifts,
two and 24 hour calibration drifts, response time, and operational period.
The continuous monitor system was installed and instruments were
initially calibrated on August 4, 1980. The following day the monitor
performance certification began. A daily event schedule for the certification
tests is presented in Table 3-1.
The performance of the continuous monitor is summarized in
Table 3-2. Also shown in the table are the monitor specifications extracted
from PS2 and PS3. Included in this table is the performance of the CO
analyzer which is not covered by the performance specification. The CO
analyzer is used to monitor the combustion conditions in the boiler since it
is a very sensitive indicator of combustion performance. Tables C-1 through
16 KVB11-6017-1266
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TABLE 3-1. SCHEDULE OF CERTIFICATION TEST EVENTS
Date
8-4-80
8-4-80
8-5-80
8-5-80
8-5-80
8-5-80
8-6-80
8-6-80
8-6-80
8-6-80
8-6-80
8-7-80
8-7-80
8-7-80
8-7-80
8-7-80
8-7-80
8-7-80
8-7-80
8-7-80
8-7-80
8-7-80
8-7-80
8-7-80
8-7-80
8-8-80
8-8-80
8-8-80
8-8-80
8-11-80
8-12-80
8-13-80
8-14-80
8-15-80
9-11-80
9-11-80
9-11-80
9-11-80
9-11-80
9-11-80
9-11-80
9-11-80
9-11-80
Time
10:00
14:00
8:30
10:30
12:30
14:30
8:30
10:30
12:30
14:30
16:30
8:30
8:55
9:55
10:30
10:55
11:55
12:30
12:55
13:55
14:30
14:55
15:55
16:30
16:55
8:30
10:30
12:30
14:30
8:30
8:30
8:30
8:30
8:30
8:30
9:30
10:30
11:30
12:30
13:30
14:30
15:30
16:30
Event
Calibration error determination
Response time determination
Initial 24 hour zero and span reading
Initial 2 hour zero and span reading
1st 2 hour zero and span drift point
2nd 2 hour zero and span drift point
3rd 2 hour zero and span drift point
1st 24 hour zero and calibration drift point
Initial 2 hour zero and calibration reading
4th 2 hour zero and span drift point
5th 2 hour zero and span drift point
6th 2 hour zero and span drift point
7th 2 hour zero and span drift point
2nd 24 hour zero and calibration drift point
Initial 2 hour zero and calibration reading
1st set of relative accuracy samples taken
2nd set of relative accuracy samples taken
8th 2 hour zero and span drift point
3rd set of relative accuracy samples taken
4th set of relative accuracy samples taken
9th 2 hour zero and span drift point
5th set of relative accuracy samples taken
6th set of relative accuracy samples taken
10th 2 hour zero and span drift point
7th set of relative accuracy samples taken
8th set of relative accuracy samples taken
11th 2 hour zero and span drift point
9th set of relative accuracy samples taken
3rd 24 hour zero and calibration drift point
Initial 2 hour zero and calibration reading
12th 2 hour zero and span drift point
13th 2 hour zero and span drift point
14th 2 hour zero and span drift point
Initial 24 hour zero and span reading
4th 24 hour zero and calibration drift point
5th 24 hour zero and calibration drift point
6th 24 hour zero and calibration drift point
7th and final 24 hour zero and calibration drift
point
1st set of relative accuracy samples taken
2nd set of relative accuracy samples taken
3rd set of relative accuracy samples taken
4th set of relative accuracy samples taken
5th set of relative accuracy samples taken
6th set of relative accuracy samples taken
7th set of relative accuracy samples taken
8th set of relative accuracy samples taken
9th set of relative accuracy samples taken
17
KVBll-6017-1266
-------
TABLE 3-2. INSTRUMENT SPECIFICATIONS AND PERFORMANCE
Parameter
Specifications
Performance
A.
1.
2.
3.
4.
5.
6.
7.
8.
Thermo Electron Series 10 NO Analyzer
X
Accuracy
Calibration error mid
high
Zero drift (2 hour)
Zero drift (24 hour)
Calibration drift (2 hour)
Calibration drift (24 hour)
Response time
Operational period
_£ 20% of mean ref. value
_<_ 5% cal gas value
<_ 5% of cal gas value
2% of span
2% of span
2% of span
2.5% of span
15 minute maximum
168 hour minimum
B. Horiba Instruments PIR 2000 CO Analyzer
1. Zero drift (2 hour)
2. Zero drift (24 hour)
3. Calibration drift (2 hour)
4. Calibration drift (24 hour)
5. Response time
6. Operational period
_<_ 0.4 pet CO2
<_ 0.5 pet CO2
_£ 0.4 pet C02
<_ 0.5 pet CO
10 minutes
168 hour minimum
C. Beckman Instruments Model 742 O2 Analyzer
1.
2.
3.
4.
5.
6.
1.
2.
3.
4.
5.
6.
7.
Zero drift (2 hour)
Zero drift (24 hour)
Calibration drift (2 hour)
Calibration drift (24 hour)
Response time
Operational period
_£ 0.4 pet O2
_<_ 0.5 pet 02
_<_ 0.4 pet O_
_<_ 0.5 pet O2
10 minutes
168 hour minimum
Horiba Instruments PIR 2000 CO Analyzer
Calibration error mid
high
Zero drift (2 hour)
Zero drift (24 hour)
Calibration drift (2 hour)
Calibration drift (24 hour)
Response time
Operational period
_<_ 5% of cal gas value
_<_ 5% of cal gas value
2% of span
2% of span
2% of span
2.5% of span
15 minute maximum
168 hour minimum
18.4%
0.9%
0.55%
1.13%
1.5%
0.258%
1.6%
29 sec
624 hr
0.29%
0%
0.29%
0«08%
52 sec
624 hr
DNA*
DNA*
0.02%
0.06%
27 sec
624 hr
1.6%
0%
0.87%
1.92%
0.17%
1.97%
41 sec
624 hr
*Instrument has no zero adjustment
18
KVB11-6017-1266
-------
C-18, Appendix C, show the performance of each of the analyzers for the
certification tests.
The data presented in Table 3-2 show analyzers in the continuous
monitor bettered the performance specification values for each parameter for
each instrument.
Certified calibration gases were obtained from Scott Environmental
Technology Inc. The calibration gases included 50 percent and 90 percent span
gases for the NO, CO,/ CO, and O- analyzers, and a zero gas. In addition to
the certified analysis supplied by the vendor, sample flasks were taken for
each calibration gas and sent to an independent laboratory for analysis.
Relative accuracy tests for the NO analyzer were performed as outlined
in PS2 using EPA Reference Method 7 (phenoldisulfonic acid [PSD] colorimetric)
as the standard. Nine sets of three PDS flasks were collected at one hour
intervals at the beginning and end of the long duration test period. All
sample flasks were returned to an independent laboratory for analysis. The
results of the relative accuracy determination are shown in Tables C-17 and
C-18 for the start and end of the test. Both tests showed that the NO
instrument exceeded the accuracy requirements of PS2. The relative accuracy
of the Thermo Electron NO analyzer was about 18.7 percent based on the first
test series and about 18.2 percent based on the final test series. The
relative accuracy requirement published in PS2 is <_ 20 percent of mean
reference value.
3.2 FIRETUBE BOILER TESTS
The continuous monitor system was installed by KVB personnel on
August 4, 1980. A single unheated sample line was strung from the boiler
stack to the continuous monitor. A single stainless steel probe with a
sintered steel filter was installed in the center of the stack. Since only
natural gas was fired, no particulate measurements were made.
19 KVB11-6017-1266
-------
The boiler was initially tested in the "as found" condition on
August 5, 1980. The boiler was operating at a daily average of 2.1 x 10
Btu/hr thermal input. The NO emission rate measured at this condition was
44 ng/J (82 ppm @ 3% O2» dry).
After measuring the emissions with the boiler in the "as found"
condition the burner air registers were adjusted to lower the excess oxygen.
This condition was then maintained for the remainder of the test period.
The operation of the boiler was very cyclic. The boiler cycled from
high fire to low fire conditions several times per hour depending on demand.
The operation of the boiler is illustrated in Figure 3-1 which is a strip
chart recording of the NO and ^ analyzers for one day. Prior to 0500 the
boiler demand is off with only an occasional firing to keep the boiler warm.
After 0500 the demand requires that the boiler cycle more frequently. In the
early hours the firing rate is higher and the O2 level is lower. In the later
hours, the average load is lower with a correspondingly higher 02 level. On
occasion, high CO values were measured during high 02 operation. These high
02 values were encountered during low load demand and heavy unit cycling at
low load cycles. The unit usually was restarted repeatedly during the 15-
minute measured intervals. While restarting, the forced draft air fan damper
opens all the way to purge the boiler from unburned gas fuel. Then gas fuel
is injected through the nozzles in the ring burner and a. moment later ignition
takes place. During this purge and ignition cycle, high CO values in
conjunction with high O2 values are observed. The average daily load is shown
in Figure 3-2 where thermal input as a function of days from start of test is
shown. Thermal input was calculated from gas flow meter readings made during
the day by the KVB technician and the heat content of the gas obtained from
the local gas company.
A plot of the daily 24-hour average of NO emission is shown in
Figure 3-3 for the test period. These data are taken from the tabulated data
presented in Table 3-3.
The gaseous emissions data measured by the analyzers were recorded on
strip chart recorders and an automatic data logger. Strip chart records were
cross checked with the data logger record to detect any data gaps or
20 KVB11-6017-1266
-------
Figure 3-1. Strip chart record of NO and O analyzer output
en
o
to
a\
-------
3
4J
ffl
o
r-l
X
a
H
8.0
7.0
6.0
5.0
4.0
3.0
2.0
Fuel: Natural Gas
Capacity: 200 HP (8.4x10
BTU/HR Input)
10 20
DAYS FROM START OF TEST
30
40
Figure 3-2. Average Daily Thermal Input for Site 6.
22
KVB11-6017-1266
-------
40
o
30
20
"as found"
Fuel: Natural Gas
Capacity: 200 HP (8.4x10
BTU/HR Input)
I
10 20
DAYS FROM START OF TEST
30
Figure 3-3. Average Daily NO Emissions for Site 6.
23
KVBll-6017-1266
-------
TABLE 3-3.
**
ft«
**
**
**
**
24 HOUR DATA
DATE
* a/ s/eo
* 8/ 6/60
*» a/ 7/eo
»* a/ 8/eo
** e/12/eo
** 6/13/60
8/14/eo
** a/is/ao
* 8/16/80
** a/i9/80
** 8/20/80
** 8/21/80
** 8/22/60
** 8/25/80
** 8/26/60
8/27/60
** 8/28/80
** 8/29/80
*« 9/ 2/80
«« 9/ 3/ao
* 9/ 4/80
* 9/ 5/80
** 9/ 8/80
» 9/ 9/80
** 9/10/80
»* 9/11/80
LOAD
TIME MWTH
***********<
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
DWT
02
VOLX
MEAS
»******<
8.3
8.4
6.3
6.2
8.6
7.2
6.4
6.6
7.4
8.1
7.5
7.7
6.9
7.4
fc.5
7.
5.
5.
9.
7.
5.
5.
6,2
8.4
9.7
8.4
STACK (
CQ2
VOLX
MEAS
»******<
7.4
7.3
8,4
8.6
6.5
7.5
8.1
7.6
7,4
6.6
7.3
7.3
7.6
7,2
.0
.9
.8
.7
.7
.0
,6
.6
.5
6.7
6.0
6.9
IAS CONI
CO
PPMV
MEAS
>******<
20
31
37
61
21
27
26
24
32
30
27
18
26
27
23
35
73
22
57
107
89
49
99
370
197
544
:ENTRAT]
NO
PPMV
MEAS
»******)
58
57
51
59
39
40
43
42
39
36
40
41
43
39
43
40
49
50
37
37
46
47
48
42
39
43
!ON
CO
PPMV
3X02
>******<
28
44
45
96
30
35
34
30
42
42
36
24
33
35
28
47
85
25
89
143
105
58
120
531
313
761
NO
PPMV
3X02
>******<
82
81
62
71
56
52
52
53
51
53
53
55
55
51
53
S3
57
56
56
49
54
56
58
60
62
61
CO
NG/J
k******i
9
14
15
32
10
11
11
10
13
13
11
6
11
11
9
15
28
8
29
47
34
19
39
175
103
258
NO
NG/J
k*******
44'
44
33
38
30
28
28
28
27
28
29
30
29
26
29
29
31
31
31
it
2S
30
31
32
33
33
ft*
*«
**
**
**
***
**
*
**
**
**
**
«*
**
ft
**
*
*
**
**
*
*
**
ft
«*
**
ft*
**
**
**
**
24
KVB11-6017-1266
-------
anomalies. In addition, the records were verified by comparison with hourly
measurements recorded by a technician. A tabulation of hourly averages was
compiled for the entire test period. After the data were compiled, they were
spot checked and edited to detect obvious errors. The data were then
keypunched on cards for input to the computer. Twenty-four-hour averages were
then calculated from the hourly data. Table 3-3 presents a list of 24-hour
averages compiled from the 15-minute averages for the entire test period.
Emission factors for the gas-fired boiler were calculated using the
procedure set forth in 40 CFR 60, Subpart D. The NO emission factor (dry
basis) was calculated using the following equation:
20.9
E ~ °dFd 20.9 - % O
Where E = Pollutant emission rate, ng/J (Ib/million Btu)
C^ = NO concentration, ng/scm (Ib/scf)
F^ = Stoichiometric conversion factor, 2.43 x 10~
dscm/J (8.710 dscf/million Btu), for natural gas
O0 = Oxygen concentration, percent by volume, dry
*d
The conversion of ppm (N02) to ng/scm is made by multiplying by 1.912
x 106. TO convert from ppm/NO_ to Ib/scf, multiply by 1.19 x 10~7. No
emissions are measured as NO dry and reported as NO2.
Statistical analysis of the data was performed to determine the
distribution which best characterized the data. Figure 3-4 presentSithe log
of NO emission rate plotted vs. probability. The data result in a straight
line, indicating that the data are log-normally distributed. The data show
that the mean NO emission rate is 29.5 ng/J with a geometric dispersion of
1.05. For these data 99 percent of the values fall below 33 ng/J. These data
do not include the measurements taken with the boiler in the "as found"
condition or the data taken on August 8, 1980 when the monitor cabinet cooling
system was inoperative and excessive cabinet temperatures resulted in
anomalous data. The cabinet cooling system was subsequently repaired and
remained in operation for the remainder of the test.
25 KVB11-6017-1266
-------
10
9
8
, 7
6
5
4
3
2
1-3
tr>
c 100
- o 90
; w 2 80
I
i 60
50
40
30
20
V 10
cri
o
H1
_ ! 1 I I 1 || 1 1 I 1 1 1 1 II 1 1 I I 1
_
SITE 6 - Gas Fired Fire Tube Boiler
___ Rated Capactiy: 250 HP
Fuel : Natural Gas
MM* WV
HW WMH
_ _
MM W««
~ "mm
^ ~""° °^ " "
NO = 29.5 ng/J
g.d.= 1.05
1 1 1 1 1 it 1 1 1 1 1 1 1 II 1 1 1 1 1
31.05 .1.2 .51 2 10 20 30 40 50 60 70 80 90 95 98 99 99.8 99.9 99.99
^ PERCENT LESS THAN
M
^ Figure 3-4. Log-Probability plot of NO Emissions from a fire tube boiler.
CTi
-------
SECTION 4.0
REFERENCES
1. Maloney, K. L. et al., "Systems Evaluation of the Use of Low-Sulfur
Western Coal in Existing Small and Intermediate-Sized Boilers," EPA
Contract No. 68-02-1863, EPA 600/7-78-153a.
2. Cato, G. A. et al., "Field Testing: Application of Combustion
Modifications to Control Pollutant Emissions from Industrial Boilers -
Phase I," EPA 650/2-74-078a, NTIS No. PB 238 920, June 1975.
3. Cato, G. A. et al., "Field Testing: Application of Combustion
Modifications to Control Emissions from Industrial Boilers - Phase
II," EPA 600/2-76-086a, NTIS No. PB 253 500, April 1976.
4. "Assessment of the Potential for Energy Conservation Through Improved
Industrial Boiler Efficiency," KVB 8300-452.
27 KVB11-6017-1266
-------
APPENDIX A
EFFICIENCY MEASUREMENTS
28 KYBll-6017-1266
-------
EFFICIENCY
Unit efficiencies for boilers are calculated and reported according
to the ASME Power Test Codes for Steam Generation Units, PTC 4.1-1965. These
codes present instructions for two acceptable methods of determining thermal
efficiency. One method is the direct measurement of input and output and
requires the accurate measurement of the quantity and high-heating value of
the fuel, heat credits, and the heat absorbed by the working fluids. The
second method involves the direct measurements of heat losses and is re-
ferred to as the heat loss method. This method requires the determination
of losses, heat credits, and ultimate analysis and high-heat value of the
fuel. Some of the major heat losses include losses due to heat in dry flue
gas, losses due to fuel moisture content, losses due to combustible material
in refuse and flue gas, and radiation losses. Heat credits are defined as
those amounts added to the process in forms other than the chemical heat
in the fuel "as fired." These include quantities such as sensible heat in
the fuel, heat in the combustion air, and heat from power conversion in a
pulverizer or fan. The relationships between input, output, credits, and
losses for a steam generator are illustrated in Figure A-l.
KVB's experience has shown the heat-loss efficiency determination
method to be the most reliable when working with industrial boilers. Ac-
curate fuel input measurements are rarely possible on industrial boilers due
to the lack of adequate instrumentation, thus making the input-output method
undesirable. The accuracy of the efficiency based on the heat loss method
is determined primarily by the accuracy of the flue gas temperature measure-
ment immediately following the last heat removal station, the stack gas
excess 0_ level, the fuel analysis, the ambient temperature, and proper
identification of the combustion device external surfaces (for radiation
losses). Determination of the radiation and other associated losses may
appear to be a rather imposing calculation, but in practice it can be ac-
complished by utilizing standard efficiency calculation procedures. Inac-
curacies in determining efficiency occasionally occur even with the heat
29 KVB11-6017-1266
-------
INPUT
ENVELOPE
LOSSES (L)
HEAT IN FUEL (H,) (CHEMICAL)
HEAT IN ENTERING AIR
HEAT IN ATOMIZING STEAM
SENSIBLE HEAT IN FUEL
PULVERIZER OR CRUSHER POWER
BOILER CIRCULATING PUMP POWER
PRtwtRY AIR FAN POWER
Rf CIRCULATING CAS FAN POWER
HEAT SUPPLIED BY MOISTURE
IN ENTERING AIR
HEAT IN COOLING WATER
CREDITS (BJ
BOUNDARY , ,, j
c ^
L 1
r ^
L r~'
HEAT IN PRIMARY STEAM
HEAT IN OESUPERHEATER WATER AND CIRCULATING PUMP INJECTION WATER
HEAT IN FEEDWATER
HEAT IN SLOWDOWN AND CIRCULATING PUMP LEAK-OFF WATER
HEAT IN STEAM FOR MISCELLANEOUS USES
HEAT IN REHEAT STEAM OUT
HEAT IN DESUPERHEATER WATER
t HEAT IN REHEAT STEAM IN
UNSURNED CARBON IN REFUSE
HEAT IN DRY GAS
MOISTURE IN FUEL
MOISTURE FROM BURNING HYDROGEN
MOISTURE IN AIR
HEAT IN ATOMIZING STEAM
-co
CARBON MONOXIDE
UH
UNBURNED HYDROGEN
UHC UNBURNEDHYDROCARBONS
RADIATION AND CONVECTION
RADIATION TO ASH PIT. SENSIBLE HEAT IN
SUA3 t LATENT HEAT OF FUSION OF SLAG
SENSIBLE HEAT IN FLUE DUST
HEAT IN PULVERIZER REJECTS
L.
HEAT IN COOLING WATER
SOOT BLOWING
OUTPUT = INPUT - LOSSES
DEFINITION: EFFICIENCY (PERCENT) = (%} = « '°°
J0°
* '00
HEAT BALANCE: H, + B = OUTPUT + L OR ^ (%) = I _ p-^g
Figure A-l. Heat balance of steam generator.
30
KVB11-6017-1266
-------
loss method primarily because of out-of-calibration unit instrumentation
such as the stack gas exit temperature. However, this problem has been re-
solved by KVB test engineers through the use of portable instrumentation
and separate temperature readings.
The abbreviated efficiency test procedure which considers only the
major losses and the chemical heat in the fuel as input will be followed.
Tables A-l and A-2 are the ASME Test Forms for Abbreviated Efficiency Tests
on steam generators which exemplify the type of forms to be used for re-
cording the necessary data and performing the required calculations.
KVB has developed a program for the HP-67 calculator which will pro-
vide the heat loss efficiency from the stack data. Figure A-2 shows the HP-
67 keyed calculation sheet for calculating efficiency by the ASME Heat Loss
Method.
KVB11-6017-1266
-------
SUMMARY SHEET
TABLE A-l
ASME TEST FORM
FOR ABBREVIATED EFFICIENCY TEST
PTC 4.1-od
TEST NO. ' BOILER NO.
DATE
OWNER OF PLANT LOCATION
TEST CONDUCTED BY OBJECTIVE OF TEST
DURATION
BOILER MAKE & TYPE RATED CAPACITY
STOKER TYPE & SIZE
PULVERIZER, TYPE & SIZE BURNER, TYPE & SIZE
FUEL USED MINE COUNTY STAT6
SIZE AS FIRED
PRESSURES & TEMPERATURES FUEL DATA
1
2
3
4
s
6
7
8
9
10
11
12
13
14
STEAM PRESSURE IN BOILER DRUM
STEAM PRESSURE AT S. H. OUTLET
STEAM PRESSURE AT R. H. INLET
STEAM PRESSURE AT R. H. OUTLET
STEAM TEMPERATURE AT S. H. OUTLET
STEAM TEMPERATURE AT R H INLET
STEAM TEMPERATURE AT R.H. OUTLET
WATER TEMP. ENTERING (ECON HBOILER)
STEAM QUALITY?". MOISTURE OR P. P.M.
AIR TEMP. AROUND BOILER (AMBIENT)
TEMP AIR FOR COMBUSTION
TEMPERATURE OF FUEL
GAS TEMP. LEAVING (Boiler) (Eeon.) (Air Htr.)
GAS TEMP. ENTERING AH (If conditions to be
psio
psio
p*ia
psio
F
F
F
F
F
F
F
F
F
UNIT QUANTITIES
15
16
17
18
19
20
21
22
23
24
25
ENTHALPY OF SAT. LIQUID (TOTAL HEAT)
ENTHALPY OF (SATURATED) (SUPERHEATED)
STM.
ENTHALPY OF SAT. FEED TO (BOILER)
(ECON.)
ENTHALPY OF REHEATED STEAM R.H. INLET
ENTHALPY OF REHEATED STEAM R. H.
OUTLET
HEAT ABS/LB OF STEAM (ITEM 16-ITEM 17)
HEAT ABS/LB R.H. STEAM (ITEM 19-ITEM 18)
DRY REFUSE (ASH PIT + FLY ASH) PER LB
AS FIRED FUEL
Biu PER LB IN REFUSE (WEIGHTED AVERAGE)
CARBON BURNED PER LB AS FIRED FUEL
DRY GAS PER LB AS FIRED FUEL BURNED
Btu/lb
Btu/lb
Btu/lb
Btu/lb
Btu/lb
Btu'lb
Btu/lb
Ib/lb
Btu/lb
Ib/lb
Ib/lb
HOURLY QUANTITIES
26
27
28
29
30
31
ACTUAL WATER EVAPORATED
REHEAT STEAM FLOW
RATE OF FUEL FIRING (AS FIRED wt)
TOTAL HEAT INPUT (''*? 2S x ltem 41>
HEAT OUTPUT IN BLOW-BOWN WATER
J|J*L (lt«m 26»!t«m 20)+(lt»m 27tltem 21) + ltem 30
OUTPUT 1000
Ib/hr
Ib/hr
Ib/hr
kB/hr
kB/hr
kB/hr
FLUE GAS ANAL. (BOILERXECON) (AIR HTR) OUTLET
32
33
34
35
36
CO,
o,
CO
Nj (BY DIFFERENCE)
EXCESS AIR
% VOL
% VOL
% VOL
% VOL
%
COAL AS FIRED
PROX. ANALYSIS
37
38
39
40
MOISTURE
VOL MATTER
FIXED CARBON
ASH
TOTAL
41
42
Btu per Ib AS FIRED
ASH SOFT TEMP.'
ASTM METHOD
% wt
COAL. OR OIL AS FIRED
ULTIMATE ANALYSIS
43
44
45
4lS
47
40
37
CARBON
HYDROGEN
OXYGEN
NITROGEN
SULPHUR
ASH
MOISTURE
TOTAL
COAL PULVERIZATION
48
49
50
64
GRINDABILITY
INDEX*
FINENESS %THRU
50 M*
FINENESS % THRU
200 M«
51
52
S3
44
41
OIL
FLASH POINT F'
Sp. Gravity Deg. API*
VISCOSITY AT SSU'
BURNER SSF
TOTAL HYDROGEN
% wt
Btu per
Ib
GAS
54
55
56
57
58
59
60
61
CO
CH« METHANE
C,H, ACETYLENE
C,H« E
THYLENE
C2H6 ETHANE
H2S
CO,
H,
HYDROGEN
TOTAL
62
63
41
TOTAL
% wt
DENSIT
HYDROGEN
r.
Y 68 F
ATM. PRESS.
Btu PER CU FT
Btu PER LB
INPUT.OUTPUT ITEM 31 « 100
EFFICIENCY OF UNIT *
ITEM 29
HEAT LOSS EFFICIENCY
65
66
67
nfl
69
70
71
72
HEAT LOSS DUE TO DRY GAS
HEAT LOSS DUE TO MOISTURE IN FUEL
HEAT LOSS DUE TO H,0 FROM COMB. OF H3
HEAT LOSS DUE TO COMBUST. IN REFUSE
HEAT LOSS DUE TO RADIATION
UNMEASURED LOSSES
Btu/lb
A. F. FUEL
TOTAL
EFFICIENCY * (100 - It.m 71)
%
F!
'Not Required for Efficiency Testing
T For Point of Measurement S*e Por. 7.2.8. 1-PTC 4.1-1964
32
KVB11-6017-1266
-------
CALCULATION SHEET
TABLE A-2
ASME TEST FORM
FOR ABBREVIATED EFFICIENCY TEST
PTC 4.1-b (1964)
Revised September, J96S
OWNER OF PLANT
30
24
25
36
"
£5
66
67
68
69
70
71
72
HEAT OUTPUT IN BOILER SLOW-DOWN
If impractical to weigh refuse, this
item 4 C0) /
ITEM 32 ITEM 33 f ITEM 35
11 x + 8 x *7\
3 x
n CO
EXCESS °i
AIRt - 100 x - -..-
-2682Nj - <
-------
FIGURE A-2
HP-67 KEYED CALCULATION SHEET
ASME ABBREVIATED EFFICIENCY CALCULATION - HEAT LOSS METHOD
Test No.
Date
Location
Unit No.
Fuel
A. FROM FUEL ANALYSIS:
Wt. % in as-fired fuel: C
(Turn Calculator Off and Then On. Load Program Card.)
», Moisture %, H %, S
Al:(5TO 0}
High heating value of fuel as-fired
AS s(STO 4)
A2!(ST01> A3s(ST02) A4:(STO3)
Btu/lb
B. FROM FLUE GAS ANALYSIS:
Volume t in flue gas of: O.
Bl:(STO 5)
%> CO,
CO
C. FROM REFUSE (FLY ASH AND ASH PIT) ANALYSIS:
Cl. Fraction of dry refuse in fuel
B2:(STO 6) B3:(STO 7)
Ibs dry refuse/lb as-fired fuel
(STO B)
C2. Heating value of dry refuse (weighted average) Btu/lb dry refuse
C3. wt. % of combustibles in refuse
(STO 9)
(f J> % S) (STO 4) (f P S S)
D. MEASURED TEMPERATURES
Ol. Gas temp, leaving boiler, econ. or air heater
D2. Comb, air temp.
E. FROM STEAM TABLES:
El. Enthalpy: H2O(g) at temp. Dl « 1 psia
£2. Enthalpy: H Oil) at comb, air temp.
(STO A)
(STO B)
(STO C)
Btu/llj
(STO D)
Btu/lb
% of gross heat input
F. FROM AH1A STANDARD RADIATION LOSS CHART (UNLESS MEASURED) 8
Fl. Heat loss due to radiation
(STO E)
6. FROM U::iT SPECIFICATIONS (if available, otherwise enter 0):
61. Unmeasured losses % of gross heat input
(f f ^ S)(STOO)(f P $ S)
100J2B1 - B3)
1. Excess Air % 0.5364(100 - Bl - B2) - (2B1 - B3)
2. (optional) Pounds dry gas per pound of fuel »
(A)
Bl + 4B2 + 700
Al
Cl X C2
3A4
(R/S)
dry gas/lb as-fired fuel
3.
4.
5.
6.
7.
8.
J(B2 T BJ> 1 J.UO ilSUO 1 tJ \ BUU 1
L ^"looj J
Heat Losses
24 x EQ.2 x (Dl - D2)
Due to noisture in fuel *^ * * . ~
100 x Cl x C2
Total Losses m Sum of calculated losses * Fl * Gl
Efficiency - 100 - Total Losses
% of Gross
Heat Input
(B)
(C)
(D)
(E)
(f )
(f b)
(Optional)
Btu/lb as-fired fuel*
(R/S)
(R/S)
(R/S)
(R/S)
(R/S)
100
34
KVBll-6017-1266
KVB 6015-21 (Rev 1)
11/7/78
-------
APPENDIX B
DATA RECORDING FORMATS
35 KVBll-6017-1266
-------
DOCUMENTATION OF RESULTS
Field Measurements
During testing, two sets of measurements are recorded: 1) control
room data which indicate the operating condition of the device and 2) emis-
sions data that are the readouts of the individual analyzers.
The concentration of nitric oxide (NO), carbon dioxide (CO ), carbon
monoxide (CO), and oxygen (O ) are measured and recorded. The concentration
of these species are measured and displayed continuously by analyzers and
strip chart recorders mounted in a console. The strip chart recordings are
retained for future reference.
A number of data sheets have been developed for use in field measure-
ments. These data sheets are listed below together with their purpose.
An example of each sheet follows.
Figure No.
Title
Purpose
B-l
B-2
B-3
B-4
B-5
B-6
B-7
B-8
Thirty-Day Field Test Data Sheets
Gaseous Emissions Data
Nozzle Size, Qm and AH Calculations
Response Time for Continuous
Instruments
Zero and Calibration Drift (24 hr)
Zero and Calibration Drift (2 hr)
Accuracy Determination (NOx)
Calibration Error Determination
Record control room data
Record Gaseous Emissions
Analyzer data
Calculate nozzle size,
flow rate, and AH for
Method 5 Test
Continuous monitor certi-
fication
Continuous monitor certi-
fication
Continuous monitor certi-
fication
Continuous monitor certi-
fication
Continuous monitor certi-
fication
36
KVBll-6017-1266
-------
Figure No.
Title
Purpose
B-9
B-10
B-ll
B-12
B-13
B-14
Analysis of Calibration Gas Mixture Continuous monitor certi-
fication
Particulate Calculation Sheet
Stack Data
Particulate Emission Caculations
Velocity Traverse
Liquid or Solid Fuel Calculation
Calculate weight of solid
particulate catch
Record volumes, tempera-
tures, pressures of Method
5 control unit.
Calculate particulate em-
mision factors
Record temperature and
velocity profile of stack
Calculate stoichiometric
properties of fuel
37
KVBll-6017-1266
-------
Figure B-l.
KVB, Inc.
THIRTY DAY FIELD TEST DATA SHEET
Site
Fuel
Test No.
Date
Time
Load
Test Description
Windbox, in. H^O
Furnace, in. H_O
Overfire air, in. H^O
f.
Boiler exit, in. H,O
Economizer exit, in. H^O
f.
ID fan inlet, in. H^O
Steam flow, kpph
Time/
Integrated steam flow k Ibs
Air flow indie.
Superheater outlet temp. °F
Flue gas temp,
economizer inlet, °F
Flue gas temp,
economizer outlet, °F
Temp F.W. economizer
outlet, °F
Feed Water Control, %
Temp F.W. heater, °F
F.W. economizer inlet, °F
Steam pressure, psig
Fuel feed
Overfire air damper
F.D. fan
F.D. fan damper
I.D. fan
I.D. fan damper
38
KVBll-6017-1266 (continued)
Data Sheet 6017-26
12/12/78
-------
Figure B-l. (Continued)
THIRTY DAY FIELD TEST DATA SHEET
Page 2
Test No.
Smoke Indicator Chart
Rotary speed
Spill plate setting
Grate speed
Over fire air damper,
% open
Fuel flow, Time/lbs
Flame observations
Bed thickness
General furnace
appearance
Clinkers
Ambient air temp, °F
& F.D. fan inlet temp.
Comments:
39
Data Sheet 6017-26
12/12/78
KVBll-6017-1266
-------
Figure B-2.
KVB, INC.
GASEOUS EMISSIONS DATA
Date
Engr.
Low NO Control Method
A
Unit No.
Fuel
Unit Type
Location
Capacity
Burner Type
1. Test No.
2 . Time
3. Load
4. Process Rate
5. Flue Diam. or
Size, ft
6. Probe Position
7. Oxygen (%)
8. NOX (hot)
read/3% 0., (ppm)
9. NO (hot)
read/ 3% 0,, (ppm)
- - 4.
10. NO (hot)
read/ 3% O^ (ppm)
. 2 "* "
11. Carbon Dioxide
(%)
12. Carbon Monoxide
(ppm) uncor/cor
13. Opacity
14 . Atmos . Temp .
(°F/°C)
15. Dew Point Temp.
(°F/°C)
16. Atmos. Pressure
(in. Hg)
17. Relative
Humidity (%)
40
Data Sheet
6015-23
9/29/78
KVBll-6017-1266
-------
Figure B-3.
KP-67 Keyed Calculation Sheet
NOZZLE SIZE, O and AH CALCULATIONS
Test Mo.
Unit No.
Crew: Enqr.
DATA
Constants
Pi tot Factor, Fs
Orifice Factor, J
Orifice Dian. , D (in.)
Ideal Meter Flow? Q (ACFM)
n
MOTE: TO RECALCULATE IDEAL
RESTORE DATA IN REGISTERS 4
STACK AND RE-ENTER % HjO, %
Date
Fuel
Key
(STO 1)
(STO 2)
(STO 3)
(STO 4)
NOZZLE SIZE,
THRU B, CLEAR
0 , and % COj
Location
Sampling Method
Techs.
Actual Conditions
Meter Temperature, Tm(*F)
Barom. Press. . Pgar '*n* "''
Static Press. Diff., AP6 (iwg)
Nozzle Temp., Tn (*F)
Stack Vel. Press.. Ap (iwg)
Caseous Stack Composition
% H?0 (%)
% 0, dry (%)
% CO, dry (%)
Key
(STO 5)
(STO 6)
(STO 7)
(STO 8)
(STO 9)
ENTER
ENTER
IDEAL HOZZLE CALCULATION
(A) Ideal Nozzle Size, D
nijdeaij
inches
METER FLOW RATE AND ORIFICE PRESS. DIFF. CALCULATIOn
Actual Nozzle Size, D ,. . ,.
n (Actual J ~~ *
(C) Actual Meter Flow Rate, °_(Act ,,
(RCL 7) Orifice Press. Diff., AH to obtain 0 ., ,.
m (Actual i -^
NOTE: To Determine Qn, and AH for Other Actual Nozzle Size, Key in Dn/Aetuajj, Press C for Q, then RCL 7
_ for AH. _ _ _
For one Dn(ACtual) fc'ith Changing Stack Velocity Pressure (Ap) and Nozzle Temperature (Tn)
(It is not necessary to restore data in registers 4-8 for these calculations)
inches
*CFH (on meter)
iwg
.
Ap (ENTER)
(iwg)
Tn
CF)
(E)
(ACFH)
(R/S) AH'
(iwg)
EQUATIONS
\3/ *. " IJ-
/ \ .
^'
.1.)
!., (2) nf - «d (% 'f°^ "*) « ^ «% 1,0)
" ' « 2«»AOOI (11.* >to * tf.)
(TB » M0> U3.» », » AH^) - «" Mo ' W.
i - l.n uten a - m«fe« of lt«»£ion« to obtain tut (An - AH )
'* -J%ru-
2MTS
4*0) - 7M (^ / «a
(in. of Mit*r)
KVB11-6017-1266
KVB 6015-25 (Rev. 1)
12/13/78
-------
Figure B-4.
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
RESPONSE TIME FOR CONTINUOUS INSTRUMENTS
Date of Test
Span Gas Concentration ppm
Analyzer Span Setting ppm
1 seconds
Upscale 2 seconds
3 seconds
Average upscale response seconds
1 seconds
Downscale 2 seconds
3 seconds
Average downscale response seconds.
System average response time (slower time) = seconds.
% deviation from slower _[average upscale minus average downscale]
_[average upscale minus average downscalel
I slower time J
system average response ' -1 -- ' x 100%
Data Sheet 6017-35
42 40CFR60/App. B
7/1/77
KVBll-6017-1266
-------
Figure B-5.
KVB
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (24-HOUR)
Engineer
Date
and
Time
Zero
Reading
Zero Span
Drift Reading
(AZero) (After Zero Adjustment)
Calibration
Drift
(ASpan)
Zero Drift = [Mean Zero Drift*
+ C.I. (Zero)
T [Instrument Span] x 100
Calibration Drift = [Mean Span Drift*
T [Instrument Span] x 100
*Absolute Value
+ C.I. (Span)
43
Data Sheet 6017-34
40CFR60/App. B
7/1/77
KVBll-6017-1266
-------
*.
&l
o
H
NJ
cn
Data
Set
No.
9
10
11
12
13
14
15
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (2 HOUR)
Engineer
Time
Begin End
Date
Zero
Reading
Zero
Drift
(Azero)
Span
Reading
Span
Drift
(ASpan)
Calibration
Drift
(Span-Zero)
Zero Drift « [Mean Zero Drift*
Calibration Drift « [Mean Span Drift*
*Absolute Value.
+ CI (Zero)
] f [Span] x 100 =
+ CI (Span) ) T [Span] x 100
ua
c
K
n>
i
en
CD
Data Sheet 6017-
40CFR60/App. B
7/1/77
-------
MONITOR PERFORMANCE TEST DATA SHEET
ACCURACY DETERMINATION (NO )
x
Engineer
Test
No.
1
2
3
4
5
6
7
8
9
Date
and
Time
,
Reference Method Samples
NO
X
Sample 1
(ppm)
NO
X
Sample 2
(ppm)
Mean refei
test valu
95% Confidence intervals = + ppm
Accurac
* Expl,
, Mean of the differences + 95%
NO
X
Sample 3
(ppm)
NO Sample
Average
(ppm)
ence method
> (NO )
X
(N0x)
confidence interval ,
Mean reference method value
iin and report method used to determine integrated averages
Analyzer 1-Hour
Average (ppm) *
NO
X
Difference
(ppm)
NO
X
Mean of
the differences
% (NO )
w
Ln
CO
o
t->
~~]
CTi
Data Sheet 6017-32
40CFR60/App.
7/1/77
-------
Figure B-8.
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
CALIBRATION ERROR DETERMINATION
Calibration Gas Mixture Data
Mid (50%) ppm High (90%) ppm
Calibration Gas Measurement System .
Run # Concentration/ ppm Reading, ppm Differences, ppm
10
11
12
13
14
15
Mid High
Mean difference
Confidence interval + +
Mean Difference2 + C.I. ,__
Calibration error = Average calibration Gas Concentration * 10°
Calibration gas concentration - measurement system reading
Absolute value
Data Sheet 6017-31
40CFR60/App. B
7/1/77
46 KVB11-6017-1266
-------
Figure B-9.
KVB
Engineer_
MONITOR PERFORMANCE TEST DATA SHEET
ANALYSIS OF CALIBRATION GAS MIXTURES
Date: Reference Method Used:
Mid-Range Calibration Gas Mixture
Sample 1 ppm
Sample 2 ^ ppm
Sample 3 ppm
Average ppm
High-Range (span) Calibration Gas Mixture
Sample 1 ppm
Sample 2 ppm
Sample 3 ppm
Average ppm
Data Sheet 6017-30
4 7 40CFR60/App. B
7/1/77
KVBll-6017-1266
-------
Figure B-10.
Test No._
Box No.
Test Description
PARTICULATE CALCULATION SHEET
Test Crew
Date
Location
Sample Probe Position
Dry Gas Meter Vol. (ft )
Final
Initial
Total
Impinger Water Vol (ml)
1 2 3 S. Gel Total
Final
Initial
A Vol
Beaker No.
Date
Weighed
Tare 1
Wt. 2
3
4
5
6
Avq
Bottle No.
Impinger
Content (Water)
Rinse (ml)
Date Weighed
or 250 Bake
Final 1
Wt. 250 2
3
4
5
6
Avg
Residue wt
Final 250-Tare
Date Weighed
or 650 Bake
Final 1
Wt. 650 2
3
4
5
6
Avg
Residue Ht
Probe
(Acetone)
Probe
(Water)
Cyclone
(Acetone)
Flask
(Dry)
Filter
Mo.
-
Blank
No.
Comments: Data Sheet 6002-3
48
KVBll-6017-1266
-------
Figure B-ll.
Date_
Load
Location
KVB, INC.
STACK DATA
Unit No.
Test No.
Engr. "
Fuel
Sample Box No.
K#/hr or MBtu/hr
Meter Box No.
Filter No.
Probe No.
Probe Length
Filter Heater Setting
Probe Heater Setting
Stack Moisture
Ambient Temperature
Nozzle Diameter
Atmospheric Pressure
Weather
Stack Gas Pressure, Ps
Abs. Stack Press., AP=P
Stack Gas Sp. Gravity,
Stack Area, As
1
% J-
Op
in. diam'
in.Hg f
1
iwg |
,,+407= iwga
Gs n.d.
ft*
^\
W
Remarks
Final Meter:
Initial Meter:
Time
Total
Avg.
Vm
Meter
Volume
Heading
(CF)
Vacuum
Gage
Reading
(iwg)
AP
Pitot
Tube
Pressur*
(iwg)
H
Orfice
Pressure
s Diff
(°F)
Stack
Temp.
(°F)
°F
°F
+ 460
Impinger
Temperature
Out
(OF)
In
(Op,
Filter
Box
Temp.
(°F)
Meter
Temp.
(Op)
-
R
49
KVB11-6017-1266
fiO-13
11/20/75
-------
Figure B-12.
Test No. Date_
nit No. Fuel.
Pitot Factor, Fs -83
HP-67 KEYED CALCULATION SHEET*
PARTICULATE EMISSION CALCULATIONS
Location
Engr.
Sampling Train and Method
Barometric Pressure, P in. Hg
Dai (STO 0)
Tot. Liquid Collected, V
Velocity Head,
ml Total Particulate, M
(STO 1)
iwg Stack Temp., Ts
n-
jn gm
I STO
(STO 4)
(STO2)
"F stack Area, As
ft
ISTO 5)
Sample Volume, Vm_
ft Stack Press., Psg_
(STO 6)
Orifice Press. Diff., H
iwg Excess 0 , XO % %
2 2 (STO 8)
Sample Time, 6_
(STO
min Nozzle Dia., Dn
(STO 7)
_iwg,(Flue Gas Density/Air Density)@ Ts, Gs
n.d.
(STO A)
(STO B)
(STO C)
in. Meter Temp., T
°F
m-
TSTODT
Select Fe
SC Feet/104 Btu
Oil (A)
92.2
Gas (B)
87.4
Coal (C)
98.2
Other :
(->)
Press (E) if meter is not temperature compensated.
1. Sample Gas Volume Vm
std
0.0334 Vm(P. + H/13.6)
oar
Vw . = 0.0474 V,
std Ic
2. Water Vapor
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C = 0;0154 Mn/Vm
b. C = 2.205 x ID*"6 Mn/Vm
c. C = Eq. 4b x 16.018 x 10
5. Abs. Stack Press. Ps = P x 13.6 + Psg
oar
std
3
6. Stack Gas Speed Vs = 174 Fs /APTsJ
407 1.00
Ps X Gs
7. Stack Gas Flow a. Qsw = Eq. 6 x As x
Rate @ 70°F
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow
9. XO factor
10. Emission
Ms
Eq. 7b x Eq. 4b x 60
XO f = 2090/(20.9 - X02%)
a. £ - Eq. 4b x Fe x Eq. 9
b. E = Eq. 4c X Fm x Eq. 9 X 1000
14077 x T
SCF
SCF
N.D.
grains/DSCF
Ib/DSCF
grams/DSCM
in. w abs.
ft/min
_ WSCF/min
DSCF/min
lb/hr
N.D.
Ib/MMBtu
ng/joule
11. % Isokinetic
* - " 2 "
6 x Vs x Ps x Dn
*If calculating by hand:
1) Convert Ts and Tm to °R
2) Multiply EQ 1 by 530/Tm(0R) if meter not temperature compensated.
3) Fffl = 2.684 x 10~5 x Fe 50 Data Sheet 6002-4
Revised 9/27/78
KVB11-6017-1266
-------
Figure B-13.
KVB, Inc.
VELOCITY TRAVERSE
- nject:_
bate:
Test Description:
Location:_
Unit:
Test:
Fuel:
Stack Cross Section
Personnel:
Barometric Press, (in. Hg):_
Absolute Static Press, in Stack (in. Hg):_
Pitot Tube Coefficient:
(P.)
(Cp)
vs = 85'48 S I P
1/2
Time
Traverse Point
Port Depth
Velocity.
Head
(in. H20)
AP
\
Gas Temp.
(°F)
Gas Temp.
(°R)
TS
Molecular
Wt.
MS
Velocity
(ft/sec)
VS
02
Cone.
(% Dry)
51
Data Sheet KVB 6002-13KVB11-6017-1
-------
Figure B-14.
KVB
Test No._
Fuel
Date
Location
No.
Fuel Sample Ho.
Fuel Sample Point
LIQUID OR SOLID FUEL CALCULATIONS
(f)(CL REG), (f) (P
-------
APPENDIX C
CONTINUOUS MONITOR CERTIFICATION DATA SHEETS
53 KVB11-6017-1266
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
RESPONSE TIME FOR CONTINUOUS INSTRUMENTS
Date of Test
Span Gas Concentration
Analyzer Span Setting
ppm
ppm
seconds
Upscale
7 seconds
7 seconds
Average upscale response £
seconds
seconds
Downscale
seconds
seconds
Average downscale response ct
seconds.
System average response time (slower time) = 2^,3 seconds.
% deviation from slower _[average upscale minus average downscale
system average response slower time
54
Data Sheet 6017-35
40CFR60/App* B
7/1/77
KVBll-6017-1266
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
RESPONSE TIME FOR CONTINUOUS INSTRUMENTS
Date of Test g fy
Span Gas Concentration //? g ppm
Analyzer Span Setting ^y _ ppm
Upscale
1
2
3
seconds
4-7
seconds
seconds
Average upscale response
, ~7 seconds
seconds
Downscale
2
3
seconds
seconds
Average downscale response
System average response time (slower time)
, "7 seconds.
seconds.
% deviation from slower average upscale minus average downscale
system average response
f
I
slower time
[
J
/3,jT.
55
Data Sheet 6017-35
40CFR60/App. B
7/1/77
KVBll-6017-1266
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
RESPONSE TIME FOR CONTINUOUS INSTRUMENTS
Date of Test
Span Gas Concentration
Analyzer Span Setting
ppnr *%>
Upscale
2
3
seconds
_seconds
seconds
Average upscale response c?^, 3 seconds
Downscale
2
3
seconds
seconds
seconds
Average downscale response
System average response time (slower time)
seconds.
seconds.
% deviation from slower _ [average upscale minus average downscale
"
system average response
_ .
slower time
56
Data Sheet 6017-35
40CFR60/App. B
7/1/77
KVBll-6017-1266
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
RESPONSE TIME FOR CONTINUOUS INSTRUMENTS
Date of Test g ' & ~ 00
Span Gas Concentration
Analyzer Span Setting /^^
-------
MONITOR PERFORMANCE TEST DATA SHEET
Data
Set
No.
1 ^--;r
2
3
4
5 5TA0
li|.'2>0
[i?'^G
rtfc'.:>J
|0 '.30
IZ'3.")
/H;SO
ib'.Bo
(>&: >y
1030
Jr. <-<>
1^:30
End
Date
B- S ^! >
j O\J
9
'
*
!
Y
:
V
Zero
Reading
O
D
5
o
0
(5
5
"5
3
c?
1
1
1
/
0
3
3
5
Zero
Drift
(AZero)
O
5
-5
0
5
2.
0
1
O
0
o
3
0
2.
Zero Drift = [Mean Zero Drift* \>hl! + CI (Zero) |,)c| ]
Calibration Drift - [Mean
*Absolute Value.
Span
Reading
Z34
235
23H
Z^H
2.SM
23S
Z 53
E3H
avi
23H
2VS
2 "' ^i
E^t/
Z3H
;'3ji
23V
a 3^
2 iM
Span
Drift
(ASpan)
~_
)
-1
O "
-
O
-1
0
o
-
1
-1
6
6
0
O
6
Calibration
Drift
(Span-Zero)
1
-fc
5
o
~fe
-2.
o
-Z
0
0
0
- "5
o
-Z
T [Span] x 100 = 1,15
Span Drift* , 3 r; 7 + CI (Span) .Z?7 ] * [Span] x 100 = . 2. 5 ,? .
Ul
00
en
o
en
Data Sheet 6017-33
40CFR60/App. B
3/26/79 (Rev. 1)
-------
O-IC
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (2 HOUR)
Data
Set
No.
1 StA 11 r
2
3
4
5 5WT
6
7
8
9
10 5V,,V,T
11 -
12
13
14
15 Si/'iiT"
16
17
18
19
20
Time
Begin
oars. >
10:50
12: So
^l'5o
og;3.)
lo;30
ia:3o
IL/;30
If. 30
02", 50
;o;3.0
1 2 ; So
K/.SO
it?:iO
02:30
io;3o
/a; So
K/:3o
End
Date
8-S-SO
1
B-6-80
i
fc-V-fcO
2- 0 » * i'N
A ^ v, *
1
Zero
Reading
0
O
o
0
0
0
0
0
0
0
0
0
0
o
0
0
0
-/
Zero
Drift
(Azero)
O
O
o
0
o
o
0
-
0
o
0
o
_
o
o
-/
Zero Drift = [Mean Zero Drift* . /*f3 + CI (Zero) . /A" ]
Span
Reading
/7,3
J7.3
J7.8
17.3
H,8
/?,s
/7.%
/7J
/7.3
/ 7J
/7/8
/7.X
/7-3
/y.jj
/?/S ~
/?. 0
/7.2
Span
Drift
(Asp an)
0
O
O "
O
0
o
0,5
O ,
O
o
o
o
0.*
+ o.B
Calibration
Drift
(Span-Zero)
0
O
o
-.
o
o
O
o.s
o
o
o
:')
O
o.%
/ /-^
T [Span] x 100 = /,
-------
6z-
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (2 HOUR)
Data
Set
No.
T
2
3
4
c
6
7
8
9
10 -tfTfifr
11
12
13
14
1 *> C-l
16
17
18
19
20
Time
Begin
ov, - j
lo ; 6*'^
IE '30
IM'30
O&IB-J
|o;3>0
i ^ - 30
IM.'SO
|t!30
OB '."So
lo1, 'so
IZ'.^O
IH.'So
Jib 'SO
0^:50
10:50
/ z : So
Ul'SO
End
Date
S-S-ViO
r
E-fc-^o
y
S-7-SD
y
S-?-S«
Y
Zero
Reading
r\ r*j »-ii
!
5
;
i
i
;
i
it
Zero Drift = [Mean Zero Drift* - +
Zero
Drift
(AZero)
b i'-t ,~i
'
1
1
i
i
1
CI (Zero) ]
Span
Reading
1.Z7
CM?
^.ZJ
c\,ZJ
1.Z7
c/,27
fl'll
^.27
ff,27
S-27
9,27
^,2?
9,27
cf 2 v
{M?
f|./: / "
^-ZO
r..' /
Span
Drift
(ASpan)
o
o
0
o
O
O
o
-
0
o
o
<1
G
-O.O7
O.OY
Calibration
Drift
(Span-Zero)
O
o
o
o
O
o
o
o
o
O
O
_
0-07
O.c >'
T [Span] x 100 = *
Calibration Drift = [Mean Span Drift* O- >l -f CI (Span) . oo^t ] -r [span] x 100 = -
*Absolute Value.
O ! b
en
o
o
H
~j
i
H-1
NJ
CTi
Data Sheet 6017-33
40CFR60/App. B
3/26/79 (Rev. 1)
-------
1 M
o - ii>'
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (2 HOUR)
Data
Set
No.
1 5T»KT
2
3
4
5 ^.TAi
i H ; so
02:30
10:30
u:3o
Miso
ib!3o
oa;3o
)o:M>
/1130
l{/.'3o
/fe'.3o
ofc.jo
,0;jo
U'.So
fH'50
End
Date
3- 5 -SO
8-fc-&0
8-7-fco
8- 9- So
Zero
Reading
O
O
2.
o
o
0
c>
o
0
G
i
i
O
Q
0
O
z
2
2
Zero
Drift
(AZero)
O
Z
o
0
o
o
o
-1
1
o
o
«.
I
o
o
Zero Drift = [Mean Zero Drift* . t/^f + CI (Zero) ,:-,( 7 + CI (Span) .S
Span
Reading
^60
cioa
ri9S
900
^00
905
'1(>0
7,^>
Span
Drift
(ASpan)
O
-s
0 '
_
o
o
0
1
, *
o
o
o
** ^f
2
o
Calibration
Drift
(Span-Zero)
O
-3
o
o
o
C7
i
-. j
Q
6
-H
o
0
T [Span] x 100 = , f, f, S .
'/S ] T [Span] x 100 = .
/y 5 .
w
H
H
CT»
O
Data Sheet 6017-33
40CFR60/App. B
3/26/79 (Rev. 1)
-------
KVB
Engineer .-*'. Z
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (24-HOUR)
MO I MST u j!".','. NJT - "7 r c D S f ,-c; E 3 iO
Date
and
Time
02*30
$ - k - £. o
OE.'iu
8 -7-3'-1
OS: Bo
S - 8 - ? 0
Of ; "i
8-n -So
OS 'SO
£ ' t* "" i5 '>^
OX . io
g - /S -SO
OS 30
Ci 3?
S - ' 5 - ?°
O S : 3 o
Zero
Zero Drift
Reading (AZero)
O
-2.
<2
-H
0
-5
-z
0
O
-2
+ Z
-M
-5
42
O
0
Span
Reading
(After Zero Adjustment)
23H
233
235
2Vi
a3M
2^5
23M
23S
23H
Calibration
Drift
(ASpan)
-1
*l
-2
-H
^'
4H
0
Zero Drift = [Mean
Calibration Drift
*Absolute Value
Zero Drift* 2.IM2
[Instrument Span] x
= [Mean Span Drift*
[Instrument Span] x
+ C.I. (Zero) l."?2? ]
100 = l.'sHS .
2,-!2^ + C.I. (Span) 1
100 = 1.57Z .
Soo ]
*,,'- = 250
62
Data Sheet 6017-34
40CFR60/App. B
7/1/77
KVBll-6017-1266
-------
KVB ./
Engineer //
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (24-HOUR)
Date
and
Time
S- S- 2o
C B
O t ' 3O
'S ~ 7 - S^>
OS ' 30
£ ~ (5 P ^
08' SO
g-fl-So
0 S : 3 o
Sr- 12 -£0
0? ', io
%- 13-30
o'a:3o
0^:50'
0 8 '. 3 Q
Zero
Zero Drift
Reading (AZero)
O
o
o
0
o
o
o
0
V
.
o
o
o
0
0
o
0
Span Calibration
Reading Drift
(After Zero Adjustment) (ASpan)
/9.S %
/7,S/'., C?
/ 7, % */j 0
/7/iA °
/?.i'': ~
/7- S /. 0
/?. ^A 0
17. '( :'. °
yg^ , -t .2.
Zero Drift = [Mean
Calibration Drift
*Absolute Value
Zero Drift* &
[Instrument Span] x
= [Mean Span Drift*
[Instrument Span] x
+ C.I. (Zero) ^ ]
100 « C
O20 + c.I. (Span) '0?O ]
100 = /V5O %
Sf-^-- 50
,_ Data Sheet 6017-34
OJ 40CFR60/App. B
7/1/77
KVBll-6017-1266
-------
KVB
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (24-HOUR)
'/
Engineer M
Date Zero Span Calibration
and Zero Drift Reading Drift
Time Reading (AZero) (After Zero Adjustment) (ASpan)
& £"'&£>
& Cs j G ' ^**
8-6 &&
35' * . * 5? &
8-0-80
***'?/ \
**£?'*/
g-/2-&&
*'£://
& -/j~- $ '
9,S~? 0
<9,3
*Absolute Value
^ ^^ -- ---^~ %
64
Data Sheet 6017-34
40CFR60/App. B
7/1/77
KVBll-6017-1266
-------
KVB
Engineer jj
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (24-HOUR)
~L >>'> ^ '<'>r'' - -'- ~ ~ !"' J f ! '-'/; Pi ^
Date
and
Time
g - 3 -jjo
?, - fc- ?' '
OS'?,.}
&--?: 60
& - i-SO
O 2; .' 3 o
Zero Span Calibration
Zero Drift Reading Drift
Reading (AZero) (After Zero Adjustment) (ASpan)
0
0
-2
-2
100
0 solute Value
Zero Drift* 1JH + C.I. (Zero) . 1s?0 ]
[Instrument Span] x 100 = .2 IS /^.
= [Mean Span Drift* / /^ + C.I. (Span) O.^-? ]
[Instrument Span] x 100 = . ;"/? /#
SP^- 1 -* .' uj
65
Data Sheet 6017-34
40CFR60/App. B
7/1/77
KVBll-6017-1266
-------
KVB
Engineer /&& '
MONITOR PERFORMANCE TEST DATA SHEET
CALIBRATION ERROR DETERMINATION
Calibration Gas Mixture Data
Mid (50%) /£>& ppm High (90%)
ppm
Run #
Calibration Gas
Concentration, ppm
Measurement System
Reading, ppm
Differences, ppm
2 //
tea
0
0
4 ,'-/
5 ff
1 //
O
/y
10
0
11 //
O
12 //
& -
13
14
a
15//
O
Mean difference
Confidence interval
Calibration error =
Mid High
. :
Mean Difference + C.I.
Average Calibration Gas Concentration
100
Calibration gas concentration - measurement system reading
Absolute value
Data Sheet 6017-31
40CFR60/App. B
7/1/77
KVB11-6017-1266
-------
Engineer /% ^
S -4
MONITOR PERFORMANCE TEST DATA SHEET
CALIBRATION ERROR DETERMINATION
Calibration Gas Mixture Data
Mid (50%) J,
4 // /78 /?£
5 // /a /&
0
&
O
6 tf /Zg J7.& &
i V to /&
8 0 s^ ^^
9 // /^? /<£
' O
O
O
10 ^ ^ ^? ^?
11 ^ /^^ 7^5
12 ff /o /&
&
o ' -
13 / /7.& J7,% O
14 g> £? jy @
15 // /7^ /^^
Mean difference
Confidence interval
, ,_ ^ . Mean Difference + C.I.
CallDi ciLiori error ".'_,., , , L x
Average Calibration Gas Concentration
Calibration gas concentration - measurement system reading
Absolute value
&
Mid High
0 0
+ & +
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
CALIBRATION ERROR DETERMINATION
4-
Calibration Gas Mixture Data
Mid (50%) &.O pi«i ^ High (90%) */ 7^ *
Calibration Gas Measurement System
Run f Concentration, ppm Reading, ppm
Differences, ppm
1 0 A/<* **re <3Gfrcs'9 -"
11 /-/ f,j ^ -0,3
12 // £~,& t-i' 0
13 // ^_^ 4?/
14 # 0A/A - -
15 ^ 1.3 qj
Mean difference
Confidence interval
2
^ , ., ^ . Mean Difference + C.I.
Calibiation error -j _., .- ~, j_ . x
Average Calibration Gas Concentration
Calibration gas concentration - measurement system reading
Absolute value
b'
-0,2
-0.2
Mid High
.01 ,2Z
+ .06 +.08
100 ' . L % i , 0 *
68
Data Sheet 6017-31
40CFR60/App. B
7/1/77
KVBll-a017-l266
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
CALIBRATION ERROR DETERMINATION
Calibration Gas Mixture Data
Mid (50%) £&& ppm High (90%) ?&<.
? J>pm
Co A >j ,- 1 v -A ;, HOfLtCiA f>i(2. ZOOO
Calibration Gas Measurement System
Run # Concentration, ppm Reading, ppm
Differences, ppm
1 0 # o $
2 H ^00 -bfc
3 0 & O
4 // *?&£> *$&&
-5
O
ff *£"// tf&o *?&&
Mean difference
Confidence interval
_ ... ,. Mean Difference + C.I.
Average Calibration Gas Concentration
Calibration gas concentration - measurement system reading
Absolute value
o
o
Mid High
+ '"' + D
100 ' -, % I %
6q
Data Sheet 6017-31
40CFR60/App. B
7/1/77 KVBll-6017-1266
-------
MONITOR PERFORMANCE TEST DATA SHEET
ACCURACY DETERMINATION (NO )
x
Engineer
Test
No.
1
2
3
4
5
6
7
8
9
Date
and
Time
8 - 7- &&
8 <-^~
3- 7'S!c?
y :,-;-^r
£ - /- £i&
//;^-,r-
g - 7- &
/<2 !^6~
£ - 7- Sc?
/3:£-&
& ' 7- £&
/4-,5-ff-
8- 7' g&
te~:^$-
& - 7- &&
te-'jrr-
Reference Method Samples
NO
X
Sample 1
_ , (PPm)
&'3C:4- <-v--, crrt,-
7&
g&
7J&2\.c,~
&&
7.*l?£,s,~
S9
&S
73
7c2
£3
£&
-7'
73
6?
Mean reference method
test value (NO ) '3
95% Confidence intervals = + 3.£& ppm
Accurac
* Expla
.i-_ _ Mean of. the differences + 95%
X
(H0x)
confidence interval ,^^
Mean reference method value " *""
tin and report method used to determine integrated averages
Analyzer 1-Hour
Average (ppm) *
NO
^*~-\ X
a/ ^%,
-------
MONITOR PERFORMANCE TEST DATA SHEET
ACCURACY DETERMINATION (NO )
x
Engineer H ,
U ? fl i fi
Test
No.
1
2
3
4
5
6
7
8
9
Date
and
Time
o
Sf- u - So
|s:3o
<3 - 11- Su
H '-10
^ -11-^0
/^:3>o
'f -H- 80
lb'30
Reference Method Samples
NO
X
Sample 1
(ppm)
6H
SB
£7
73
S2
^
^
76
feb
NO
X
Sample 2
(ppm)
85
10
^6
75
12.
7V
71
7?
AIR U-AIC
NO
X
Sample 3
(ppm)
*H
^
£3
73
%b
li
So
S£
Au^- i r ^- :<
NO Sample
Average
(ppm)
72
?/
71
7H
«o
7o
74
si
86
Mean reference method
test value (NO ) 7- ?
95% Confidence intervals = + V' ^ ppm
Accurac
* Explc
.. Mean of the differences + 95%
X
(NO )
A
confidence interval __,_
Mean reference method value
lin and report method used to determine integrated averages
Analyzer 1-Hour
Average (ppm) *
NO
X
7fe
5?>
5^
t3
77
^7
t-s
65
7Y
Difference
(ppm)
NO
X
_
^
13
^o
ii
3
3
&
Ib
8
Mean of
the differences ' ''
/%£
% (NO )
CD
CTl
O
to
-------
APPENDIX D
CONTINUOUS MONITOR PERFORMANCE SPECIFICATIONS
72 KVB11-6017-1266
-------
App.B
Title 40Protection of Environment
_
IVn sczcuiCATioN TTST r»o-
crstrara roi MONTTOU or SOi tjrp KOi
rmou STinomiT aotracza *' "*
I. Principle and Applicability.
1.1 Principle. The concentration of sulfnr
dioxide or oildei of nitrogen pollutant* in
tack emissions I* measured 07 s> continu-
ously operating emission measurement tya-
tem. Concurrent with operation of the con-
tinuous monitoring system, the pollutant
concentrations are also measured with refer-
ence methods (Appendix A). An average of
the continuous monitoring intern data Is
computed for each reference method testing
period and compared to determine the rela-
tive accuracy of the continuous monitoring
system. Other texts of the continuous mon-
itoring system are also performed to deter-
mine calibration error, drift, and response
characteristic* of the system.
1.3 Applicability. This performance spec-
ific* t Ion Is applicable to evaluation of con-
tinuous monitoring systems for measurement
of nitrogen oxides or sulfur dioxide pollu-
tants. These specifications contain test pro-
cedures, Installation requirements, and data
computation procedures for evaluating the
acceptability of the continuous monitoring
systems.
2. Apparatus.
3.1 CallbrsSoa O*a Mixtures. Mixtures of
known concentrations of pollutant gas In a
diluent gas shall be prepared. The pollutant
gas shall be sulfur dioxide or the appropriate
oxlde(s) of nitrogen specified by paragraph
6 and within rubparts. For sulfur dioxide gxs
mixtures, the diluent pis may be air or nitro-
gen. For nitric oBde (NO) gas mixtures, the
diluent gas shall be oxygen-free «10 ppm)
nitrogen, and for nitrogen dioxide (NO,) gas
mixtures the diluent gas ihall be air. Concen-
trations of approximately 60 percent and 90
percent of span are required. The BO percent
gas mixture Is used to set and to check the
pan and Is referred to as the span (as.
8.2 Zero Gat A gas certified by the manu-
facturer to contain less than 1 ppm of the
pollutant gas or ambient air may be used.
a a Equipment for measurement of the pol-
lutant gas concentration using the referent*
method specified In th* applicable standard.
9.4 Data Recorder. Analog chart recorder
or other suitable device with input voltage
range compatible with analyser system out-
put. The resolution of the recorder's data
output shall be sufficient to allow completion
of the test procedures within this speetfl-
eaHon.
3£ Continuous monitoring system for SO,
or NO. pollutants a* applicable.
S. Definitions.
t.l Continuous Monitoring System. The
total equipment required for the determina-
tion of a pollutant gas concentration is
source effluent. Continuous monitoring sys-
tems consist of major subsystems as follows:
«.l.l Sampling Interface. That portion of
e extractive continuous monitoring system
that performs on* or more of the following
operations: Acquisition, transportation, and
.conditioning of a sample of the source efflu-
ent or that portion of an in-sltu continuous
- monitoring system that protects the analyzer
from the effluent.
3.1.2 Analyzer. That portion of the con-
tinuous monitoring system which senses the
pollutant gas and generates a signal output
that Is a function of the pollutant concen-
tration.
3.1.3 Data Recorder. That portion of the
continuous monitoring system that provides
a permanent record of the output signal in
terms of concentration units.
32 Span. The value of pollutant concen-
tration at which the continuous monitor-
ing system Is set to produce the maximum
data display output. The span shall be set
at the concentration specified in each appli-
cable subpart.
3J Accuracy (Relative). The degree of
correctness with which the continuous
monitoring system yields the value of gas
concentration of a sample relstlve to the
value given by a defined reference method.
This accuracy is expressed in terms of error.
which is the difference between the paired
concentration measurements expressed as a
percentage of the mean reference value.
8.4 Calibration Error. The difference be-
tween tee pollutant concentration indi-
cated by the continuous monitoring system
and the known concentration of the test
gas mixture.
3.S Zero Drift. The change la the continu-
ous monitoring system output over a stated
period of time of normal continuous opera-
tion when the pollutant concentration at
the time for the measurements is tero.
.3.0 Calibration Drift. The change IB the
continuous monitoring system output over
a stated time period of normal continuous
operations when the pollutant concentra-
tion at the time of the measurements is the
same known upscale value.
8.7 Response Time. The time Interval
.from a (tep change in pollutant concentra-
tion at the input to the continuous moni-
toring system to the time at which 95 per-
cent of the corresponding final value is
reached as displayed on the continuous
monitoring system tiata recorder.
3.8 Operational Period. A minimum period
of time over which a measurement system
is expected to operate within certain per-
formance specifications without unsched-
uled maintenance, repair, or adjustment.
3.9 Stratification. A condition identified
ty a difference in excess of 10 percent be-
tween the average concentration in the duct
or stack and the concentration at any point
more Uian 1.0 meter from the duct or stack
wall.
4. Installation Specifications. Pollutant
continuous monitoring systems (SO, and
NO.) shall be installed at a sampling loca-
tion where measurements can be made which
are directly representative (4.1), or which
can be corrected so as to be representative
(4.2) of the total emissions from the affected
73
KVB11-6017-1266
-------
Chapter IEnvironmental Protection Agency
App.B
facility. Con form an ce with this requirement
ball be accomplished u follow:
4.1 Effluent gases may be assumed to be
nonstratlfied If a sampling location eight or
more stack diameter* (equivalent dlameten)
downstream of an; air in*leakage is se-
lected. This assumption and data correction
procedures under paragraph 4.2.1 ma; rot
be applied to sampling locations upstream
of an air pieheater In a steam generating
facility under Bubpart D of this pan. For
sampling locations where effluent gaaes are
either demonstrated (4.3) or ma; be as-
sumed to be nonstratl&ed (eight dlameten).
a point (extractive systems) or path (tn-sltu
systems) of average concentration ma; be
monitored.
4.2 For sampling locations -where effluent
g«j«j cannot be assumed to be nonstratl-
fled (less than eight diameters) or have been
shown under paragraph 4.3 to be stratified,
results obtained roust be consistent!; repre-
sentative (e.g. a point of average concentra-
tion ma; shirt with load change*} or the
data generated b; sampling at a point (ex-
tractive systems) or across a path (In-sltu
systems) must be corrected (4.2.: and 433)
so as to be representative of the tola! emis-
sions from the affected faculty. Coaform-
ance with this requirement ma; be accom-
plished in either of the following ways:
4.2.1 Installation of a diluent continuous
monitoring system (O, or CO, u explicable)
In accordance with the procedures under
paragraph 4.2 of Performance Specification
3 of this appendix. If the pollutant aad
diluent monitoring systems are not of the
same type (both extractive or both tn-iitu).
the extractive system must uae a multipoint
probe.
4.2.2 Installation of extractive poUutaat
monitoring systems using multipoint sam-
pling probes or lo-sttu pollutant monitoring
systems that sample or tie* emissions which
are consistently representative of the total
emissions for the entire cross section. The
Administrator may require data to be sub-
mitted to demonstrate that the emission*
sampled or viewed are consistent!; repre-
sentative for several typical faculty process
operating conditions.
43 The owner or operator ma; perform a
traverse to characterize an; stratification of
effluent gases that might exist In a stack or
duct. If BO stratification It present, sampling
procedures under paragraph 4.1 ma; be ap-
plied even though the eight diameter criteria
U Dot met.
4.4 When single point sampling probes for
extractive syitems are Installed within the
stack or duct under paragraphs 4.1 and 42.!.
the sample ma; not be extracted at any point
less than 1.0 meter from the stack or duct
wall. Multipoint sampling probes installed
under paragraph 432 may be located tt any
points necessary to obtain consistently rep-
resentative samples.
8. Continuous Monitoring flvrtem Per-
fiormaaee Specifications
The continuous monitoring system shall
meet the performance specifications la Table
3-1 to be considered acceptable under this
method,.
TABU 2-1.Performance peeifleatloni
Ftranarr
SptdftmUoi
1. Acwtncj <
i Calibration error'_.
a. Zero drift (2 h) >
*. Zero drtrt .
6. Calibration drift 04 h)'
7. Response time .......
t- OprnUoc*] puled..
.... <3C pet nf lie mean valut of lie returnee method list
data.
.£» pet of each (SO pet, 80 pet) calibration jaa nurture
value.
.... 3 pet of spaa
Do.
.... Do.
.... it peu of spaa
.... U Ella "«"trmm
.... 188 h minimum.
1 Etprtstd as IUCT of sbsoluu mean value plot U pet eonfidenoel nterral of a Miles of lists.
6. Performance Specification Tnt Proce-
dures. The following test procedures shall be
used to determine eonfonnance with the
requirements of paragraph 6. Por NOt *n-
Jyzers that oxidize nitric oxide (NO) to
nitrogen dioxide (NO,), the response time
test under paragraph 6.3 of this method shall
be performed using nitric oxide (NO) spaa
(as. Other tests for NO. continuous monitor*
ing systems under paragraphs e.I and 63 and
all tests for sulfur dioxide systems shall ,be
'performed using the poUutaat spaa .(as spe-
cified by each subpart *
6.1 Calibration Error Test Procedure. Bet
up and calibrate the complete continuous
monitoring system according to the manu-
facturer's written Instructions. This may be
accomplished either la the laboratory or In
the field.
0.1.1 Calibration Oas Analyses. Triplicate
analyses of the gu mixtures shall be per-
formed within two weeks prior to use using
Reference Methods 8 for BO, and 7 for NO..
Analyze each calibration gas mixture (50%.
0%) and record the results on the example
sheet shown la Pigur* 3-1. Each sample test
result must be within 20 pereeat of the aver-
aged result or the test* shall be repeated.
This step ma; be omitted for non-ertrartlve
monitors where dynamic calibration gas mix-
tures are not used (6.1 J),
6JJ Calibration Error Test Procedure.
Make a total of 16 nosconcecutlve measure-
ments by alternate!; using zero gas sad each
calibration gas nurture/concentration (e.R_
0%, 60%. fi%. 90%. 60%. 90%. 80%, 0%.
»te.).»ui uuunbauin ruiUluuuuu u.LiiUlm'.
M« tmri
74
KVB11-6017-1266
-------
App.B
Title 40Protection of Environment
cell* whose concentrations are certified bj
toe manufacturer to be functionally equiva-
lent to these gas concentrations Convert the
continuous monitoring system output read-
tugs to ppm anil record the results on the
example aheet abown In Figure 2-2.
6.3 Field Test for Accuracy (Relative).
Zero Drift, and Calibration Drift. Install and
operate the continuous monitoring system in
accordance with the manufacturer's written
Instructions and drawings u follows:
6.3.1 Conditioning Period. Offset the tero
setting at least 10 percent of the span ao
that negative zero drift can be quantified.
Operate the system for an Initial IBS-hour
conditioning period In normal operating
manner.
6.2.3 Operational Test Period. Operate the
continuous monitoring system for an addi-
tional IBS-hour period retaining the eero
offset. The system stall monitor the source
effluent at all times except when being
zeroed, calibrated, or backpurged.
6.3.2.1 TJM»trt T>gt fn- Arrtifft-T M?,f^«»f*T*}n^
For continuous monitoring systems employ-
Ing extractive sampling, the probe tip for the
continuous monitoring system and tie probe
tip for the Reference Method campling train
should be placed at adjacent locations in the
duet. For NOX continuous monitoring sys-
tems, make 37 HOX concentration measure-
ments, divided Into nine seta, using the ap-
plicable reference method. Ho more than one
set of tests, consisting Of three Individual
measurements, shaU be performed in any
one hour. All Individual measurement* of
each tet shall be performed concurrently,
or within a three-minute interval and the
results averaged. For SO, continuous moni-
toring systems, make nine BO, concentration
measurements using the applicable reference
method. Ho more than one measurement
ah all be performed In any one hour. Record
the reference method test data and the con-
tinuous monitoring system concentrations
on the example data aheet ahown In Figure
.9-4.
6.2.2,3 Field Test for Zero Drift and Cali-
bration Drift. For extractive systems, deter-
mine the values given by tero and span gu
pollutant concentrations at two-hour Inter-
yals until IS acts of data are obtained, far
producing P T-P^-^^^XIttou-tbit provlrtee-a
ttern
(or the computed zero drift) on the
example data aheet ahown In Figure 3-4.
The two-hour periods over which measure-
ments are conducted ceed not be consecutive
but may not overlap. All measurements re-
quired under «>fi« paragraph may be eon-
ducted concurrent with tests under para-
graph 6.3.2.1.
6.2.2.3 Adjustments. Zero and calibration
corrections _anj^»t'"ftan'ffnS_jr> tJiowefj qnly
l~ CectibnTCclTcnttry^lBcln.dlng--tbe
t*di»*laatqurcejnd--
tlflKI riy the- manufacturer-to-be functlotr-
ally^qulvalent4o-60 percent of span eonoen
Jntion. Record the eero and spaa netware-
__
at 24-hour~lritervalB or at such shorter In-
ierrkls as the rnanufaeturer's written In-
structions specify. Automatic corrections
made by the measurement system without
operator Intervention or Initiation are allow-
able et any time. During the entire 168-hour
operational test period, record on the «-
ample sheet shown In Figure 2-i the values
given by tero and span gas pollutant con-
centrations before end after adjustment at
24-hour Intervals.
62 Field Test for Response Time.
6.3.1 Scope of Test. Use the entire continu-
ous monitoring system as installed, including
cample transport lines If used. Flow rates,
line diameters, pumping rates, pressures (do
not allow the pressurized calibration gas to
change the normal operating pressure In the
tample line), etc.. ahall be at the nominal
values for normal operation as specified in
the manufacturer's written instructions. U
the analyzer is used to sample more than one
pollutant source (stack), repeat this test for
each sampling point.
6.3.2 Response Time Test -Procedure. In-
troduce eero gas into the continuous moni-
toring system sampling Interface or as close
to the sampling interface as possible. When
the system output reading has stabilized.
srwitcb quickly to a known concentration of
pollutant gas. Record the time from concen-
tration switching to 95 percent of final (table
response. For non -extractive monitors, the
highest available calibration gas concentra-
tion shall be switched Into and out of the
sample path and response times recorded
Perform this test sequence three f 3) times
Record the results of each test on the
example sheet shown In Figure 3-6.
7. Calculations, Data Analysis and Report-
Ing.
7.1 Procedure for determination of mean
values and confidence Intervals.
.. T.1.1 The mean value at data eet Ir
calculated according to equation 3-1.
-1 Equation 2-1
where:
gjsrabsolute value of the measurements,
Xstum of the Individual values,
X=mean value, and
n= number of data point*.
7.1 J The 85 percent confidence Interval
(two-sided) 1s calculated according to equa-
tion 3-2:
C.I.,
Equation 2-2
75
KVB11-6017-1266
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Chapter 1Environmental Protection Agency
App.B
where:
3£x,=sum of all data points,
t.m = t,-a/2, and
C.J.|»=95 percent confidence interval
estimate of tbe average mean
value.
Values for '.975
0 '.875
t 12.706
I 4.J03
4 t 1C
« 1776
1K1
1. 2.M7
t. . 2. US
9 Z.W6
>0 2.262 -
11 2.2S8
12 1201
M 2.178
H 1180
U 1145 .
M 1U1
The Talues IB this table are already cor-
rected (or n-1 degrees of freedom, Use n
equal to the number of wimples as data
points.
7JJ Dtta Analysis and Reporting.
7.2.1 Accuracy (Relative). For each of tbe
Bine reference method test point*, determine
tbe average pollutant concentration reported
by tbe continuous monitoring system. These
average concentrations shall be determined
from tbe continuous monitoring system data v
recorded under 7.2.2 by integrating or aver-
aging tbe pollutant concentration! over eacb
of tbe time interval! concurrent with e»ch
reference metbod testing period. Before pro-
ceeding to tbe next step, determine tbe basis
(wet or dry) of tbe continuous monitoring
system data and reference metbod test data
concentrations. If the bases are not con-
sistent, apply a moisture correction to either
reference metbod concentrations or tbe con-
tinuous monitoring system concentrations
as appropriate. Determine tbe correction
factor by moisture tests concurrent with tbe
reference metbod testing periods. Report tbe
moisture test metbod and the correction pro-
cedure employed. For eacb of tbe Bine test
runs determine tbe difference for eacb test
run by subtracting tbe respective reference
method test concentration* (use average of
eacb set of three measurements for NO»)
from tbe continuous monitoring system Inte-
grated or averaged concentrations. Using
tbese data, compute tbe mean difference and
tbe 85 percent confidence Interval of tbe dif-
ferences (equations 3-1 and 3-3). Accuracy
U reported as the sum of tbe absolute value
of tbe mean difference and tbe 65 percent
confidence Interval of tbe differences ex-
pressed as a percentage of the mean refer-
ence metbod value. Us* tbe example sheet
abown in Figure 3-3.
/ 7.2.3 Calibration Error. Brag the data
from paragraph 6.1, subtract tb« measured
pollutant concentration determined under
paragraph 6.1.1 (Figure 3-1) from tbe value
shown by tbe continuous monitoring cyitem
tor «*cb of tbe five reading! at each con-
centration measured under 0.12 (Figure 3-3).
Calculate tbe mean of tbese difference-values
and the SI percent confidence Intervals ac-
cording to equations 3-1 and 2-2. Report tbe
calibration error (the sum of tbe absolute
value of the mean difference and tbe 95 per-
cent confidence Interval) as a percentage of
each respective calibration gas concentra-
tion. Use example sheet shown In Figure 3-3.
132 Zero Drift (2-bour). Using tbe zero
concentration values measured eacb two
hours during the field test, calculate tbe dif-
ferences between consecutive two-hour read-
Ings expressed In ppm Calculate the mean
difference and the confidence interval using
equations 2-1 and 2-2. Report tbe zero drift
as tbe sum of the absolute mean value and
tbe confidence Interval as a percentage of
spaa. Use example sheet shown In Figure
2-4.
7.3.4 Zero DrUt (24-bour). Using the zero
concentration values measured every 34
hours during tbe field test, calculate tbe dif-
ferences between the eero point after tero
adjustment and tbe zero value 34 hours later
Just prior to zero adjustment. Calculate the
mean value of tbese points and the confi-
dence interval using equations 3-1 aad 3-3.
Report the zero drift (tbe rum of the abso-
lute mean and confidence Interval) u a per-
centage of span. Use example tbeet shown In
Figure 3-4.
7J2.5 Calibration Drift (2-hour). Using
the calibration values obtained at two-hour
intervals during tbe field test, calculate the
differences between consecutive two-hour
readings expressed as ppm. Tbese values
should be corrected for the corresponding
zero drift during that two-hour period. Cal-
culate the mean and confidence interval of
these corrected difference values using equa-
tions 3-1 and 2-2. Do not use tbe differences
between non-consecutive readings. Report
the calibration drift as tbe sum of the abso-
lute mean and confidence interval as a per-
centage of span. Use example sheet shown In
la Figure 3-4.
7.2.6 Calibration Drift (34-bour). Using
the- calibration values measured every 34
hours during tbe field test, calculate tbe dif-
ferences between tbe calibration concentra-
tion reading after zero and calibration ad-
justment, and tbe calibration concentration
reading 34 hours later after zero adjustment
but before calibration adjustment. Calculate
the mean value of tbese differences and tbe
confidence interval using equation* 3-1 and
3-3. Report the calibration drift (the rum of
the absolute mean and confidence Interval)
u a percentage of spaa. Us* tbe example
aheet shows in Figure 2-6.
7.3.7 Response TUae. Using tbe charts
from paragraph 8J, calculate tbe time Inter-
val from concentration switching to 95 per-
cent to the fl«*' (table value for all upscale
and downscale tests. Report the mean of the
three upscale test times and the mean of the
three downscale test times. TB» two aver-
age times should not differ by more than IB
percent of the slower time. Report the alowar
76
KVB11-6017-1266
-------
App.B
Tifle 40Prelection of Environment
time as the system response time. Use the ex-
ample sheet shown in Figure 3-4.
7.2.8 Operational Test Period. During tb*
168-hour performance and operftllon&l test
period, the continuous monitoring system
shall not require any corrective maintenance,
repair, replacement, or adjustment other than
that clearly specified as required Is the op-
eration and maintenance manuals as routine
and expected during a one-week period. IX
the continuous monitoring system operates
wjtbla the specified performance parameters
and does not require corrective maintenance,
repair, replacement or adjustment other than
M specified above during the 168-hour test
period, the operational period will be success-
lull; concluded. Failure ol the continuous
monitoring system to meet this requirement
anal] call for a repetition of the 168-hour test
period. Portions of the test which were satis-
factorily completed oeed cot be repeated.
failure to meet any performance specifica-
tions shall call for a repetition of the one-
week performance test period and that por-
tion of the testing which is related to the
fa'Jed specification. All maintenance and ad-
justment* required shall be recorded. Out-
put readings shall be recorded before and
after all adjustments.
a. References.
8.1 "Monitoring Instrumentation for the
Measurement of Sulfur Dioxide In Stationary
Bource Emissions," Environmental Protection
Agency, Research Triangle Park, N-C, Feb-
ruary
3 "Instrumentation for the Detennlua*
tlon of Nitrogen Oxides Content of Station-
ary Source Emissions," Environmental Pro-
tection Agency, Research Triangle Part, N.C.
Volume 1, APTD-OB47. October 1871; Vol-
ume 2, APTD-0942, January 1972.
8.3 "Experimental Statistics," Department
of Commerce, Handbook 01. 1863. pp. 8-31.
paragraphs 3-3.1,4.
8.4 "Performance Specifications for Bta-
tlonary-Source Monitoring Systems for Dues
and Visible Emission*," Environmental Pro-
tection Agency. Research Triangle Park, N.C,
£PA-fl50/2-74-013, January 1874.
»u*>-fa*»» fw? CiUbftti*" ttt JMctun
M. *»l/i1i rf tolltntta bl Mnirat
77
KVB11-6017-1266
-------
Chapter IEnvfremmenlafTrolecHon Agency
App.B
Calibration Cat Mixture Data (Fran Figure 2-1)
*1d (50Z) ppq High (90S) ppa
~ Calibration Has ."' Measurement Systen
?un I Concentration,gyre Reading, ppn
Differences, ppa
15
Hid High
Kean difference
Confidence Interval
C«libration error »
Mean Difference* + C.T.
Average Calibration Gas Concentration
x 100
Calibration gas concentration - measurement systea reading
Absolute value
figure 2-2. Calibration Error Ptterafnation
78
KVB11-6017-1266
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App.fi
Title 40Protection of Environment
itflrtntt Aftno4 b**tpltl 1
Oitt SO, », 1C.
'«{ »*e Sw'l 1 Sanpft 1 Sup!
He. TIM (WE) (M«) <»P"
1
7
1
a
1
1
7
1
I
tin rtftrtncc* acthotf ' Nun
.lit Tilut (SO-) trit
fcl CBftfldmtt Inttnrllt *
«kn of tnt «iff«r,nc«i ,
caraclts .... ^tn rlitrtnct ^,1^
' Upliln and riport MtKM u»< W Murcfni Int
Flgurt 2-3. Accu
Jiu .
Stt T1K {ere
.0. ... Ie;1n Em! Oitt tudlti
1
i
,
1
i '
« ' '
7
«
,
18
11
1?
1]
11
IS
Jer* Orlft [rl**n 2(re Orlft*
Ulltritlon Drift (Ntin JH" brUt*
«*»Ulut« ValM. - '
rijur. M. 2cre i
J M IK Su«lt *Mt;»r 1-Hour Glfftrtnci
j (we) { <»pi?' »J" P«, "l^""8.
1 1
.1 -
*
i
!
,
-i ..
lf«r«nce VthoJ N»n of "
ilut (DO ) tlw tlfftrtncti
>« (SO.) « « IK i )
,,\u, i iw 1 IJOj) 1 {*aft
ier >«r»lMtlon (S02 »nd «I)
Orlft S»«n Drift Drift
(iZero) (M«ng <
. - - -
t * ' ~
* CI litre) J « [Spin] 1 100 «
M alteration Drift (I Huir)
79
KVBll-6017-1266
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Chapter IEnvironmental Protection Agency
App.B
Date Zero Span Calibration
and Zero Drift Reading Drift
Tine Reading (aZero) (After zero adjustment) (dSpsn)
Zero Drift « [Mean Zero Drift*
C.I. (Zero)
« [Instrument Span] x 100 « _ .
Calibration Drift - [Mean Span Drift* _ + C.I. (Span)
« [Instrument Span] x 300
* Absolute value
Figure 2-5. Zero and Calibration Drift (24-hour) ''.'.,
80
KVB11-6017-1266
-------
App.B
Title 40Prolec
c/M
Date of Test
Span Cas Concentration PP
Analyser Scan Setting Pf
i " '
1 se
'Upscale 2 , .*e
3 se
Average upscale respo
1 tt
Downsealt 2 . , , se
S se
; -- /iverjge downscale res
System average response time (slower tin
Idevtatlon from slower . [averaoe upsca
system average response |_ -
\r1*' figure 2-6. Res
P»rfnrm«n(:e. .£??£! 2 C&HSB. * Perfonnme
pec in cations ana specification test prooe
i
n
:onds
:onds
:onds
tit seconds
:ond$
rands
conds
pens* seconds
e) » seconds.
le minus average downscale | ' 1rrnT
slower time - J J _ x -, '
ponse Time
i as spaa gm*- *°r oxygen aaalyzers, if tJ
pan Is higher than 31 percent Op amble
durti for monitors of CO, tad O, from sta
Gentry touroei.
1. Principle mnd Applicability.
U Principle. Effluent gases are continu
ously sampled and are analyzed for carbo i
dioxide or 017gen by a continuous monitor
Ing system. Test* of tbe syitem are performei
during a minimum operating period to deter
mine ivero drift, calibration dttlft, and
ponse time cbaracterLrtlcs.
U Applicability. Toll performance spec!
flcation Is applicable to evaluation of eon
tiouous monitoring systems for measurement
of carbon dioxide or oxygen. Tbese specific*
tlons contain test procedures, Installation
quirements, and data computation prooe
dures for evaluating tbe acceptability of "
continuous monitoring syitems subject
Approval by tbe Administrator. BunpUnb
Bay Include either extractlTe or non-extrai
UT« (tn-altu) procedure*.
9. Apparatus.
3J Continuous Monitoring System
Carbon Dlortde or Orygcn.
93 Calibration Oas Mixtures. Mixture
known concentrations of carbon dioxide
oxygen In nitrogen or air. Uldrange and
percent of span carbon dioxide or oxygeo
concentration* are required. Tbe 60 pereetjt
Of span fmi mixture is to be used to set
check tbe analyzer spaa and is referred
fcr
tr
an 3
to
ion of Environment
air may be -used la place of tbe 60 perosnt of
pan calibration (as mixture. Triplicate
analyses of tbe gas mixture (except ambient
air) shall be performed within two weeks
prior to use using Reference Method S of
tbis part.
as Zero Gas. A pas containing leas than 100
ppm of carbon dioxide or oxygen.
3.4 Data Recorder. Analog chart recorder
or otber suitable device with Input voltage
range compatible wltb. analyzer system out-
put. Tbe resolution of tbe recorder's data
output shall be sufficient to allow completion
of tbe test procedure* within tt>u gpeeiflca-
tion.
S. Definitions.
S.1 Continuous Monitoring System. Tbe
total equipment required for tbe determina-
tion of carbon dioxide or oxygen in a given
source effluent. Tbe sy»tem consists of tbree
major subsystems:
1.1.1 Sampling Interface. That portion of
tbe continuous monitoring system that per-
forms one or more of tbe following opera-
tions: Delineation, s*cquialtlon, transporta-
tion, and conditioning of a sample of tbe
Knirc* effluent or protection of tbe analyser
from tbe hostile aspects of the cample or
source environment.
81
KVB11-6017-1266
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Chapter IEnvironmental Protection Agency
App. B
3.1.3 Analyzer. Tint portion of tbe con-
tinuous monitoring *ystem which lease« tbe
pollutant gu and generate* a signal ontput
that 1* a function of the pollutant concen-
tration.
3.13 Dsta Recorder, That portion of the
continuous monitoring system that provide*
a permanent record of tbe output signal in
termi of concentration unit*.
as Span. Tbe value of oxygen or carbon di-
oxide concentration at which tbe continuous
monitoring system la ast tbat produce* tbe
maximum data display output. For tbe pur-
pose* of this method, tbe ipan shall be set
no less than 1.5 to 2.6 times tbe normal car-
bon dioxide or normal oxygen concentration
in tbe stack gu of tbe affected facility.
8.3 Mldrange. Tbe value of oxygen or car-
bon dioxide concentration tbat U representa-
tive of tbe normal condition* In tbe stack
gat of tbe affected facility at typical operat-
ing rates.
8.4 Zero Drift. Tbe change la tbe eoattn-
uou* monitoring system output over a stated
period of time of normal contlnuou* opera-
tion wben tbe carbon dioxide or oxygen con-
centration at tbe time for tbe measurements
1* zero.
3.6 Calibration Drift. Tbe change In the
continuous monitoring system output OTCT *
stated time period of normal contlnuou* op-
eration wben tbe carbon dioxide or oxygen
continuous monitoring syitem U measuring
tbe concentration of ipaa gw.
8.6 Operational Test Period. A mlnknnm
period of time over which the contlnuou*
monitoring system is expected to operate
within certain performance specifications
without unscheduled maintenance, repair, or
adjustment.
3.7 Response time. Tbe t1mi> Interval from
a step change in concentration at the Input
to the contlnuou* monitoring syitem to the
time at which 95 percent of the correspond-
ing final ralue Is displayed on the continuous
monitoring system data recorder.
4. Installation Specification.
Oxygen or carbon dioxide continuous mon-
itoring systems shall be Installed at a loca-
tion where measurement* are directly repre-
sentative of the total effluent tram tbe
affected facility or representative of the some
effluent aampled by BO, or NO, contlnuou*
monitoring syitem. This requirement shall
be complied with by use of applicable re-
quirement* in Performance Specification 3 of
this appendix u follows:
4.1 Installation of Oxygen or Carbon Di-
oxide Continuous Monitoring Syitem* Not
Used to Convert Pollutant Data. A sampling
location shall be selected la accordance with
tbe procedures vntlrr paragraphs 4.2.1 or
4.3.3. or Performance Specification 9 of this
appendix. . . . -
4.9 Installation of Oxygen or Carbon Di-
oxide Contlnuou* Monitoring Systems Used
to Convert Pollutant Continuous Monitoring
System Data to 0nlU of Applicable Stand-
ard*. Tbe diluent continuous monitoring sys-
tem (oxygen or carbon dioxide) shall be la-
stalled at a sampling location where measure-
ment* that can be made are representative of
the effluent gase* (sampled by tbe pollutant
contlnuou* monitoring system(»). Conform-
ance with *N« requirement may be accom-
plished In any of tbe following ways:
4 J.I The sampling location for the diluent
system shall be near tbe sampling location (or
the pollutant continuous monitoring system
such that the same approximate polat(s)
(extractive systems) or path (in-*lttt sys-
tem*) In the cross section Is sampled or
viewed.
423 Tbe diluent and pollutant continuous
monitoring systems may be instilled at dif-
ferent locations II the effluent gases at both
sampling locations are nonstratlfied as deter-
mined under paragraphs 4.1 or 4.8, Perform-
ance Specification 3 of this appendix and
there 1* no In-leakage occurring between tbe
two sampling locations. If tb* effluent gases
are stratified at either location, tbe proce-
dures under paragraph 4.3.2, Performance
Specification 3 of thl* appendix shall be used
for initalllng contlnuou* monitoring system*
at that location.
6. Continuous Monitoring System Perform-
ance Specifiestloas.
The continuous monitoring «ystem shall
meet tbe performs nee specifications la Table
8-1 to be considered acceptable under **«*
method.
6. Performance Specification Test Proce-
dure*. .- - -
The following test procedures shall be used
to determine conformanc* with the require-
ments of paragraph 4. Due to the wide varia-
tion existing in analyzer design* and princi-
ple* of operation, these procedures sun not
applicable to all analyzers. Where this occurs,
alternative procedures, subject to tbe ap-
proval of tbe Administrator, may be em,
ployed. Any such alternative procedure*) must
fulfill the same purposes {verify response,
drift, and accuracy) as the following proce-
dures, and must clearly demonstrate con-
formance with specifications la Table 8-1.
4.1 Calibration Check. Establish a call ora-
tion curve for the continuous monitoring
system using zero, mldrange, aad span con-
centration gaa mixtures. Verify that the re-
sultant curve of analyzer reading eotnparad
with tbe calibration gu value is consistent
with the expected response curve a* described
by the analyzer manufacturer. If tbe ex-
pected response curve Is not produced, addi-
tional calibration gas measurements) shall
be made, or additional steps undertaken to
verify the accuracy of the response curv* of
tbe analyzer.
t.2 Field Test for Zero Drift and Cali-
bration Drift. Install aad operate the eoa-
tlauous x&oaltorlaff system la
82
KVB11-6017-1266
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App. B
Title 40Protection of Environment
with the manufacturer'! written Instructions
and drawings a* followi:
S-l.Performance ipectfcattora
Parameter
Specification
1. Ztn drift (2 b)' <0.4 pet Oi or COi.
I. Zero drift (S4 b) i <0i pet Oi or CO«.
(. C»libntiOD drill (3 b) >. . <0 4 pet Oi or COu
4. CtUbniloc drift (24 b) >. <0.» pel OiOf CO*.
i. Operation*! period....... 166 b mlnlmom.
t. Response Ha*.. .- lOzolo.
< Expressed as suss of sbsolnl* mean value pins 15 pet
confidence Inter**! of» uries of lots.
6.2.1 Conditioning Period. Offset the tero
ettlng et least 10 percent of (pan to that
negatlva tero drift ma; be quantified. Oper-
ate the continuous monitoring *ystam for
an Initial 168-hour conditioning period In a
normal operational minner.
622. Operational Test Period. Operate the
continuous monitoring lystem for an addi-
tional 168-hour period maintaining the tero
offset. The system iball monitor the aource
effluent at all times except when being
uroed, calibrated, or backpurged.
8.2.3 Field Test for Zero Drift and Calibra-
tion Drift. Determine the values given by
tero and mldrange gas concentrations at two-
hour Intervals until 15 aets of data are ob-
tained. For non-extractive continuous moni-
toring systems, determine the tero value
given b; a mechanically produced tero con-
dition or by computing the tero value from
upscale measurement* using calibrated gas
cells certified b; the manufacturer. The mid-
range checks shall be performed b; using
certified calibration gas cells functionally
equivalent to less than 60 percent of span.
Record these readings on the example sheet
shown in Figure 3-1. These two-hour periods
need not b« consecutive but ma; not overlap.
In-situ CO; or O, analyzers which cannot be
fitted with a calibration gas cell ma; b« cali-
brated b; alternative procedures acceptable
to the Administrator. Zero and calibration
corrections and adjustment* are allowed
only at 24-hour interval* or at cueh shorter
intervals u the manufacturer'* written In-
structions tpectf;. Automatic corrections
made by the continuous monitoring system
without operator intervention or Initiation
are allowable at any time. During the en-
tire 168-hour test period, record the value*
flven by zero and span gas concentrations
before and after adjustment at 34-hour in-
terval* IB the example sheet shorn la Figure
1-3.
6.3 Field Test for Response Time.
6.3.1 Scope ef Tut.
This text shsl! be accomplished using the
continuous monitoring system a* Installed.
including sample transport line* if used.
Flow rates, line diameter*, pumping rates.
pressure* (do not allow the pressurized cali-
bration gas to change the normal operating
preaiure in the sample line), etc.. shall be
at the nominal values for normal operation
as specified in the manufacturer'* written
Instructions. If the analyzer is used to (ample
more than one source (stack), this tect shall
be repeated for each sampling point.
6.3.2 Response Time Test Procedure.
Introduce tero gas Into the continuous
monitoring system sampling Interface or u
close to the sampling Interface as possible.
When the system output reading bu stabi-
lized, switch quickly to a known concentra-
tion of gas at BO percent of span. Record the
time from concentration switching to 65
percent of final stable response. After the
system response has stabilized at the upper
level, switch quickly to a tero gas. Record
the time from concentration twitching to 85
percent of final stable response. Alterna-
tively, for nonextractive continuous monitor-
ing systems, the highest available calibration
gas concentration shall be switched Into and
out of the sample path and response times
recorded. Perform this test -sequence three
(3) times. For each test, record the rerulta
on the data sheet shown in Figure 3-3.
7. Calculations. Data Analysis, and Report-
Ing.
7.1 Procedure for determination of mean
values and confidence intervals.
7.1.1 The mean value of a data aet i* cal-
culated according to equation 3-1.
11 i~i Equation 3-1
where:
«,=absolute value of the measurements,
I=*um of the individual value*.
x = mean value, and
B = number of data point*.
7.2.1 The 95 percent confidence Interval
(two-sided) 1* calculated according to equa-
tion 8-2:
C.I.t
nVn-1
Equation 3-2
where:
2X=srum of all data point*.
-B75=t,-«/2, and
CJm=85 percent confidence Interval es-
timates of the average mean value.
for
13 ------------------------------- a. 301
83
KVB11-6017-1266
-------
Chapter IEnvironmental Protection Agency
App. B
Tbe values In tbLi table are already corrected
lor n-1 degrees of freedom. Die o equal to
tbe cumber of samples as data points.
7.2 Data Analysis and Reporting.
72.1 Zero Drift (2-hour). Using tbe zero
concentration values measured eaeb two
bouri during the field test, calculate tbe dif-
ferences between tbe consecutive two-hour
readings expressed In ppm. Calculate the
mean difference and the confidence Interval
using equations 3-1 and 3-2. Record tbe sum
of the absolute mean value and tbe confi-
dence Interval on the data abeet above in
Figure 8-1.
7.2.2 Zero Drift (24-hour). Cslng tbe eero
concentration values measured ever; 34
hours during tbe field test, calculate the dif-
ferences between the zero point after zero
adjustment and the zero value 24 hours
later just prior to zero adjustment. Calculate
the mean value .of these points and tbe con-
fidence Interval using equations 3-1 and 3-2.
Record the zero drift (tbe sum of the ab-
solute mean and confidence Interval) on tie
data sheet shown In Figure 3-3.
7.2.3 Calibration Drift (2-hour). Using the
calibration values obtained at two-hour In-
tervals during the field test, calculate tbe
differences between consecutive two-hour
reading! expressed aa ppm. These values
ahouid be corrected for the corresponding
zero drift during that two-hour period. Cal-
culate the mean and confidence Interval of
these corrected difference values using equa-
tions 3-1 and 3-3. Do not use the differences
between non-consecutive readings. Record
the sum of the absolute mean and confi-
dence Interval upon the data abeet ah own
tn Figure 3-1.
7.2.4 Calibration Drift (34-hour). Using the
calibration values measured ever? 34 hour*
during tbe field test, calculate the differ-
ences between the calibration concentration
reading after zero and calibration adjust-
ment and the calibration concentration read-
lug 24 hours later after zero adjustment but
before calibration adjustment. Calculate the
mean value of these differences aad tbe con-
fidence interval using equation* 3-1 and J-2
Record the aum of the absolute zoeaa and
confidence interval on the data abeet ahown
In Figure 8-2.
7.2.6 Operational Test Period. During tbe
166-hour performance and operational test
period, the continuous monitoring cvttem
ahall not receive any corrective maintenance.
repair, replacement, or adjustment other
than that clearly specified as required la tbe
manufacturer's written operation and main-
tenance manuals as routine aad expected
during a one-week period. If the continuous
monitoring system operates within the speci-
fied performance parameters and does cot re-
quire corrective maintenance, repair, replace-
ment or adjustment other than as specified
above during tbe 168-hour test period, tbe
operational period will be successfully con-
cluded. Failure of tbe continuous monitoring
system to meet this requirement shall nil
for a repetition of the 168 hour test period.
Portions of the test which, were satisfactorily
completed need not be repeated. Failure to
' meet any performance specifications ahall
call for a repetition of the one-week perform-
ance test period and tbat portion of the test-
Ing which Is related to the failed specifica-
tion. All maintenance and adjustments re-
quired ahall be recorded. Output readings
abali be recorded before *nd after all ad-
justments.
7.2.6 Response Tim*. Using the date devel-
oped under paragraph 6J, calculate the time
Interval from concentration twitching to 65
percent to the final stable value for all up-
scale and dowascale teats. Report the mean of
tbe three upscale test times and tbe mean of
the three downseale teat times. Tbe two av-
erage times ahouid not differ by more than
16 percent of the alower time. Report the
lower time as the system response time. Re-
cord the results on Figure 1-8.
B. References.
8.1 "Performance Specifications for Sta-
tionary Source Monitoring Systems for Oaaes
and Visible Emissions," Environmental Pro-
tection Agency, Research Triangle Park, K.C,
rPA-650/3-74-013, January 1B74.
8.3 "Experimental Statistics," Department
of Commerce. National Bureau of Standards
Handbook. 91, 1903, pp. 8-J1, paragraphs
S-fl.1.4,
84
KVB11-6017-1266
-------
App. B
Title 40Protection 'of Environment
uu
-------
Chapter IEnvironmental Protection Agency App. B
)4te Zero Span Calibration
ind Zero Drift Reading Drift
Time Reading (aZero) (After zero adjustment) (iSpan)
Zero Drift « [Hean Zero Drift* + C.I. (Zero) 3
:a11bration Drift - [Mean Span Drift*
+ C.I. (Span)
Absolute value
Figure 3-2. Zero end Calibration Drift (24-hour)
86
KVBll-6017-1266
-------
App.C
Title 40Protection of Environment
Oatt of Test
Span Gas Concentration
Analyzer Span Setting
1.
Upscale 2.
3.
. PP<"
ppm
seconds
seconds
seconds
Average upscale response
seconds
Downscalc
1.
2.
3.
.seconds
_seconds
seconds
Average downscsle response
seconds
seconds
System average response time (slower'tire) »
S, £« an exlsUni
facility resulted In an increase ID the emission rat* to tb*
atmosphere. Tbe metbod used Is the Btndent't f lest,
commonly used to make inferences from "*" (ample*.
2.1 Each emission test thai! consist of runs (osoallT
three) which produce * emission rates. Tbos two acts of
mission ratrs are f enerated, on* before and on* afur tb*
chance, the two sets betni of equal site.
2.2 when using manoal emission tests, eioept as pro-
Tided In i 60.8(0) of this pan, the reference methods of
Append!* A totals part shall be used In accordance with
the pncedores specified In tb* applicable stibpart both
before and afier the chan|e to obtain the data.
U When usnt continuous monitors, tbf faeilllf lhallb*
operated as U a ininuul emission test wrra belnt per-
formed. Valid data uslnc the averadnf time which would
be rronirvd I' ' rraTjal emission test wen btlaf con-
docua aball be ta,e, for
taeh an of data oUnj EqnaUoo L
«
^^^
^^j
amended »t 42 FR 6937,
(1)
ween:
A-KznJUon rate for tb* f th ran.
nombe- of nans
U Calculate the aample rarlanaa, S>, (or cmcli aet of
data nsini Eqoatioa 2.
s (*i-»)«
-, «-l
n-1
n-1
(2)
1.4 Calrabte tb* poolad cKlmata, £,, ostnt Sqoa-
tJoo S.
(3)
r(n.-l) g.'-r(n>-l) S.'
'"L n.+n,-2 J
OalctuaUU»ttittuaitic,<.asU«XquiIoD4.
87
KVB11-6017-1266
-------
APPENDIX E
RESULTS OF PREVIOUS TESTS AT SITE 6
88 KVB11-6017-1266
-------
DATA SUMMARY
Test No.58
Category
Furnace Type
Fire Tube
Fuel Type Natural Gas
_ . 9
Region
Burner Type
Location 5
Capacity
8
Ring
Unit No. 248-1 Owner Norton Air Force Base' CA
Comments
ki/hr
1. Test No.
2. Test Load (k*/hr)
3. Type of Test
A . Control
5. Water Content (% vol.)
6. Excess Oxygen (%)
7. Total Nitrogen Oxides 1 NOx (ppm)
8. Nitric Oxide } NO (opm)
9. Nitroqen Dioxide \ NO., (ppm)
10. Carbon Dic:-ica, CO,, (;)
11. Carbon Monoxide, CO (ppm)
12. Total Hydrocarbon, HC (pern)
13. Sulfur Trioxide, SO., (ppm)
'" o
14. Sulfur Dioxide, S0_ (pom)
15. Total Particulate (lb/i-3tu)
16. Overall Efficiency (%)
58-2
6.4
Baseline
Auto
15
11
70
68
2
5
0
18
-
-
0.0036
58-5
1.6
Low Load
Hand
15
15
55
21
34
2.
0
170
-
-
-
58-8
6.4
Low Air
Hand
15
3.2
45
37
8
9
> 2000
240
-
-
-
Reported as dry at 3% excess oxygen.
89
KVB11-6017-1266
-------
i A r; 10 x 10 TO THC INCH 46 O782
H *>"*'* 7 X I'' I'JCI'I <, '*( IN
-------
Of HTNI THI ni Ol X Ol
-------
Test Unit No.
K VB. INC.
INDUSTRIAL BOILER FIELD TEST DATA
1. Location;
2.
Date
3.
4.
5.
6.
7.
8.
9.
10.
11.
"»2.
13.
14.
15.
16.
17.
18.
19.
20.
21.
22.
23.
24.
Unit
Descrptn.
Fuel
Burners
Furnace
Boiler
POO &&£ . . Serial No. A/g£6&
Installation Date "" ; Gross Output
kw
8370 /7Btu/hr; Steam Output £
Ib/hr
Amount
Ib/hr
Arrangement
Overfire?
Recirculation?
Preheat?
're
Pressure
Superheat
psig; Temperature
°F Reheat
Air System
Control, Primary
Control, Secondary
Comments
26.
92
KVBll-6017-1266
60-7
-------
For Fui.-i.er Information Please Contact:
Norman Hclgeson
Glen Cato or
Carlo DeVivo at . \
Telephone: (714) 832-9020
Enclosure (1)
LA APCD Permit No.
Test No.
>^«ner/0perator
Person Contacted
Date
(I)
ltl£>
Location
Future Contact
63 AB&
i-i CQ(-
Water Tube
Tube
Fuel
Date Installed
Product (hot water /steam; $"'<>*%*-..'- J ~? *-: 1' U :((£-.
±ier(iManufacturer\Model,Spec."Features}'
.9 "iO 6 O
Gas Only
Oil Only
Gas/Oil Combination
Approxinate Date's~Used-
Gas
, Oil
OIL BURI3ERS
Number
GAS-BUpl'JERS
Nujnbcr
Manufacturer (Date)
Manufacturer (Date)
Model
Fuel Usage Rate(gpm)
Other
Fuel Usage Rate(SCFM)
Other
93
KVB11-6017-1266
-------
Sheet
of
K V B, INC.
CONTROL ROOM DATA
.1 Mumber_
illnit Number_
JPuel
Sg
Date
-7?'
Owner
tf f f
Location
Capacity (KS/hri
rJ'urnace Type
')JO
Identification
Burner Type
1. Test Number
2. Load (kt/hr) ^
3.
4.
5. Oxygen (%)
6.
7, Feedwater Flow (Klb/hr)
3. Superheat Temp (°F/°C)
9. AH Gas Temp. (°F/°C) (In/Out)
D. FD Fan
JL. ID Fan
1 Flow (lb/hr) (gal/hr)
3. Air Flow
/*, > ->
4. Fuel Pressure (osig) sr/2>'f,: ,-
-z. Atomizing Steam Press. (osig)
3. SteanA'ater Flow (Klb/hr)
1. Steam/^**-?- Press, (usig)
3. Smoke Meter
.9. Register Settincr
J. Register Settino
f~.' '(. C r N" 1. ,
1. { v "''"V-'"V-' sL
:. /'/, /^.- A />. -' r--'. /-
N2 in fuel (%)
*
:.
*
..
-
' 2Z- /
/ -~>'- : v
.
^^
,- - -
.
_
,
-
_
"Z.O
__ .
/z.z
. .
A7/?"-'
fivTO
S'Z-Z.
*'>:-,
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~_
A 2S-
-
'2 -
-
/V?/tfA/
t/rv
,c ^
v5^-2
^ <5 /&
/
, ^7
/ z ^
_
/--; ; - -
X" " '
, '^
r/- ^?
^ "> ^ ,
''--.
--
/ /. j
/;^V'»
- X- -
2 0 V^
/'
/'
-------
Test No.
to
r2"est Number
LDnit
-Fuel
K VB. INC.
MOBILE LABORATORY DATA
Date
Test Engr.
: Number /
.cit
.ace
t^/t-'-T
y (k#/hr) ^ O
> Type A C £{,'/*//. "-" S-
x: x7
Owner A/ e? / 'cX/ - -
-5 . Atmos. Temp. (F°/C°) '
-6. Dew Point Temp. (F°/C°)
7. Atmos. Pressure (in. Hg)
/
79
v,~;>
£%3
£?
/,£f
-f?
7/^o?
/ -^
.5~,
&
/(,
;
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c^?
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y
f
f
ss?
i
r
3
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c=J
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^^
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t\/6/£ t Ptct^^ t< /X/ /^x 7~
/ -7- j 95
j»
^^ %'
/sf
// ?
3<7
3?
J
6t
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y^
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r- <^
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C=J>
c^
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yc/
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x
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KVBll-6017-1266
O
f=>
LS
-------
Sheet
of
K V B, INC.
CONTROL ROOM DATA
1 lumber ; _>
JJnit Number i.' '- "" i
Date " -T- / ?- V :
Owner fJ''"'\' fJ I "";
vfcel Location /
^Capacity (KS/hr) >"""'-
furnace Type "\ ^ . ; - i . t-.i
Identification
. Burner Type
1. Test Number
2. Load (k#/hr) '
3.
4.
5. Oxygen (%)
6.
3. Superheat Tern? (°F/°C)
9. AH Gas Temp. (°F/°C) (In/Out)
.0. FD Fan
_1. ID Fan
L* 1 Flow (lb/hr) (gal/hr)
.3. Mr Flow
'/' -
4. Fuel Pressure (psig) s-r AX / ,-
!_5. Atomizing Steam Press. (psig)
i 5. StearaA'ater Flow(Klb/hr)
7. Steani/?»fe«: Press, (nsia)
3. Smoke Meter
3. Register Setting
3. Reaister Setting
_.'-.-- ' - -
:. , /'-,':
:. ; ' f- - -,". -, - -f
;. N2 in fuel (%)
i '
1 "* m
\
+
\
* 't'~
# "<-
^
_._
1,0
.
_,L _ -
//. '^
-
/".'\ ^ / ;
^ A" / i
no
" " !
f:-' :
' A
---
/3.0
.
..--
f'.u
>-> / h I J
/ Of
$?-?
Si ' .
/
/
/
/
.-
-
. 37
Zo
._ --
(A f~ ' J
f'/.l-r.
/oz
96
KVB11-6017-1266
60-2
-------
Test No.
s
&
to
Number
K VB. INC.
MOBILE LABORATORY DATA
Date
Test Engr ,
- x
Unit Number /
?uel fc> /v-/
Capacity (k#/hr) £V ^
furnace Type /'\<^ C*tJ S? /:/;£ s^
Owner fl/ s& -/^ -^
Location J) j&'f/**' A/S> c '- S^ f
^
Identification x^X* ^ ' I/"
/£££' " s Burner Type X^ /*_£.
.-1 ,
1. Test Number
2. Load (kff/hr) ^
3. Flue Diameter (ft)
4. Probe Position
5.
6.
7, Water Content (% vol.)
8. Oxygen (%)
9. NOxfhot line) readinq/@3% 0? (ppm)
.0. NO (hot line) reading/@3% 02^PPm^
,1. NO2(hot line) reading/@3% 02 (ppm)
2
^
^r*
J
S
^
<3"
%
'*2
^f &
/'
.
^/
^-> /
/x//
\g~
*7
£
y
^5
s
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.'
/
/
^
^
^
^
/
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r ^ *
*t,
/
£'
yy
y?
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3 -^~
x-'
^
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J'x^
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7-?
y*
^'s
Jxx
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^
^^
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x1"* *""
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, J
J
/
y
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te 9
'', *2
60-3
97
KVBll-6017-1266
-------
K V B. INC.
STACK DATA
Test No.
Engr . C^
Date
Load
Location Nl 0
0' >
Unit No.
Fuel
I, r % K#/hr or MBtu/hr Filter No.
Sample Box No. - Meter Box No. " Probe No. Probe Length ID' -lfj
Filter Heater Setting
Probe Heater Setting
Stack floisture
Ambient Temperature
Nozzle Diameter
Atmospheric Pressure
Weather
Stack Gas Pressure, Ps
Stack Gas Sp. Gravity, GIF
0F
in.
in.Hg
I
diam.
iwg
n.d.
fto
1
Remarks
-
~
Time
I=H:>
,c. -
",^ ,
:
^.030
2o4~>
^oso
iicc
2 ' 10
-2.115
Total
Avg.-'"
Vm
Meter
Volume
Reading
(CF)
-4^~;
Xt/(/}.'?
L24/?*/.?
2*/?V.2
2^3,^
2503.4
^5"/V- ?
-2J515.1
2-5j5.4
2.^5,?
3t5"^3
100
Vacuum
Gage
Reading
(iwg)
9
^
?.5"
9,^
9 5"
Q
Q
Q
Q
Q ry c*
.i,~T~ CfTT.
Pitot
Tube
Pressun
^ (iwg)
'.of »'
* f t;
:-"',
-------
K VB. INC.
Particulate Weight Calculations
Test No.
Engr.
-i
FILTER BEFORE TEST
Filter
1st wt, (gr)
2nd wt. (gr)
3rd wt. (gr)
4th wt. (gr)
Initial (gr)
Sample
Tare
Tare
No.
Comments
1st wt. (gr)
2nd wt. (gr)
3rd wt. (gr)
4th wt. (gr))
Final (gr)
,-,747
FILTER AFTER TEST
.:-- - 7 ;;
CONTAINER BEFORE TEST
Front End
No . /
Back End
No . 7,
Desicant
No . ^-
Tare
No . ' 3
Tare
No . V
1st wt. (gr)
2nd wt. (gr)
3rd wt. (gr)
4th wt. (gr)
Final (gr)
CONTAINER AFTER TEST
1st wt. (gr)
2nd wt. (gr)
3rd wt. (gr)
4th wt. (gr)
3,
Final
Test No.
Unit No.
(gr)
Date m//y/75 Location /jo^'ToA/ Engr.
Fuel G-fl 5 Load 35"CA. K#/hr..
MBtu/hr
99
KVBll-6017-126^ Q _i 1 ft
-------
Test No
K VB. INC.
COLLECTED LIQUID
Imp. 1
Final vol. (ml) /f j
Initial vol. (ml) /^ S ( CC ' '
Back
Contr.
No. I-
Tare Tare
Contr. Contr.
No. /g No. Z/7
2(^.701? 27.^ 12. 27.5*3^
Filter
No.
Front
No./
Back
No.
Increase (gr)
HH Tare (gr)
Part wt.
Filter Particulates
Front End Particulates
Back End Particulates
Total
PARTICULATE SUMMARY
0>
0. C I
gr
gr
gr
gr Mn=
,/ 0
milligrams
100
KVBll-6017-1266
60-11B
-------
KVB, INC.
EMISSION CALCULATIONS
Test No.
Test No. ~ Date lv//y/'73 Location
Unit No. / Fuel Cfi$ Load /?. ft Kf/hr
Engr.
MBtu/hr
Pitot Factor, Fs
0,$]
Total Liquid Collected, V1ff
Velocity Head, AP .. £7 iwg Stack Temperature, Ts
Sample Volume Vm /OQ ft3 stack Gas Pressure, Ps
Orfice Press. Diff , H 1*5*1 iwg Stack Gas Sp. Gravity, Gs /
Barometric Pressure, Pbar__B_l2__ in«H
-------
2 3
/& & c/
Fr / ,
0
8"
/t"
/6
/i
O
3
f
O
V*
Ts
7*
6,0*!
0.0$
0. (3 1
V. £>
*?
^ ^
. /es/
$3$
\
£3
102
KVBll-6017-1266
-------
APPENDIX F
TABULATION OF 15-MINUTE DATA
103 KVBll-6017-1266
-------
********** *******************************************************«**,, ***** *********
**
**
**
**
**
**
DATE
** 8/ 5/80
** 8/ 6/80
** 8/ 7/80
** 6/ 8/80
** «/i2/eo
** 8/13/80
** 8/ia/60
* 8/15/80
** 8/18/80
** 8/19/80
«* 8/20/80
** 8/21/80
** 8/22/80
** 8/25/60
* 8/26/80
*» 8/27/80
* 8/28/80
*« 8/29/80
** 9/ 2/80
** 9/ J/80
* 9/ 4/80
** 9/ 5/80
»* 9/ 8/80
9/ 9/80
*« 9/10/80
** 9/11/80
TIME
LOAD
MWTH
******
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
DRY
02
VOLX
MEAS
m** * **i
8.3
8.4
6.3
6.2
8.6
7.2
6.4
6.8
7.4
8.1
7.5
7.7
6.9
7.4
6.5
7.6
5.6
5.6
9.5
7.6
5.8
5.9
6.2
8.4
9.7
8.4
24 HOUR DATA
STACK GAS CONCENTRATION
C02
VOLX
MEAS
CO
PPMV
MEAS
NO
PPMV
MEAS
CO
PPMV
3X02
NO
PPMV
3X02
CO
NG/J
NO
NG/J
**
**
**
**
**
**
*****************************************************
7.4
7.3
6.4
8.6
6.5
7.5
8.1
7.8
7.4
6.6
7.3
7.3
7.6
7,2
8.0
6.9
8.8
8.7
5.7
7.0
8.6
8.6
8.5
6.7
6.0
6.9
20
31
37
81
21
27
28
24
32
30
27
18
26
27
23
35
73
22
57
107
89
49
99
370
197
544
****************************
58
57
51
59
39
40
43
42
39
38
40
41
43
39
43
40
49
50
37
37
46
47
48
42
39
43
28
44
45
96
30
35
34
30
42
42
36
24
33
35
28
47
85
25
89
143
105
58
120
531
313
781
82
81
62
71
56
52
52
53
51
53
53
55
55
51
53
53
57
58
58
49
54
56
58
60
62
61
*******************
9
14
15
32
10
11
11
10
13
13
11
8
11
11
9
15
28
8
29
47
34
19
39
175
103
258
44
44
33 '
38
30 -
28 -
28
28
27-
28 '
29 -
30 <
29 '
28 -
29 <'
29 -
31
31
31
26-
29
30 '
31 '
32-
33 '
33 /
**
**
**
**
**
**
**
**
**
**.
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
******************
104
KVB11-6017-1266
-------
ft*******************************************************
**
**
**
**
**
*»
DATE
TIME
02
LOAD VOCX
HWTH ME*S
15 MIN. DAT*
DRY STACK GAS CONCENTRATION
C02 CO NO CO
VOtX PPMV PPHV PPMV
MEAS MEAS MEAS 3X02
NO
PPMV
3X02
CO
NGXJ
**
**
**
NO ACUDE **
NGXJ **
**
******************************************************************************************
**
**
**
**
**
**
**
*«
**
**
**
**
**
**
**
**
ft*
ft*
ft*
**
**
ft*
ft
ft*
**
ft
ft*
**
«
*
**
**
ft*
**
**
**
**
*
**
*
**
ft*
**
ft*
**
**
OX
OX
OX
OX
OX
OX
OX
OX
OX
OX
OX
OX
OX
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
8X
8X
ex
«<:
ex
8X
a/
ex
ex
ex
ex
ex
ex
ex
e/
ox o
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
5X80
sxeo
sxeo
5X80
5X80
5X60
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
830
845
900
915
930
905
1000
1015
1030
1005
1100
1115
1130
1145
1200
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
0
.0
-.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
**************************
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
6.2
6.1
7.2
7.2
8.0
8.0
8.0
6.4
8.0
8.5
6.7
8.7
8.6
8.7
8.8
****
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
8.6
8.6
8.2
8.2
7.5
7.5
7.5
7. a
7.5
7.4
7.2
7.2
7.5
7.2
7.1
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
37
39
28
28
21
21
22
18
18
17
18
18
18
17
18
*******************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
48
48
52
52
52
51
52
54
53
54
55
53
55
54
56
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
45
47
36
36
29
29
30
25
24
24
26
26
26
24
26
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
58
58
67
67
72
70
72
77
73
77
60
77
60
79
62
****************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
1«
15
12
12
9
9
10
8
8
8
6
8
8
6
6
********
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
31
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
ft*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
31 **
36 **
36 **
39 **
38 **
39 **
41 **
39 **
42 **
43 **
42 **
43 **
42 **
44 **
*****************
105
KVB11-6017-1266
-------
ft**********************************************
*******************
**
**
**
**
**
**
DATE
TIME
LOAD
MWTH
15 WIN. DATA
DRY STACK GAS CONCENTRATION
02 C02 CO NO CO
VQLX VOLX PPMV PPMV PPMV
MEAS MEAS MEAS MEAS 3X02
NO
PPMV
3X02
CO
NCXJ
NO ACODE
NGXJ
**
**
**
**
**
**
It*****************************************************************************************
**
**
**
*»
**
**
**
**
**
**
**
**
**
**
**
**
**
**
*»
*»
**
**
**
**
**
**
**
**
**
**
**
**
*»
*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
8X
ex
ex
ex
8X
ex
ex
ex
ex
8/
8X
8/
ex
8/
a/
e/
»/
ex
8X
ex
8X
ax
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ox
ox
ox
ox
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
SX80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
5X80
OX 0
OX 0
OX 0
OX 0
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
22«5
2300
0
0
0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
o
8.8
8.7
8.6
8.7
8.7
8.8
8.8
8.9
6.8
8.7
8.7
8.6
8.5
8.5
8.5
e.4
8.5
8.5
8.6
8.4
8.3
8.4
8.3
8.3
8.7
8.6
8.6
8.7
8.5
8.6
8.5
8.5
8.5
8.4
8.4
8.4
8.4
8.3
8.3
8.3
8.2
8.2
8.2
8.3
.0
.0
.0
.0
7.1
7.2
7.2
7.2
7.2
7.1
7.1
7.0
7.1
7.2
7.2
7.2
7.4
7.4
7.4
7.4
7.4
7.4
7.2
7.3
7.4
7.3
7.4
7.«
7.2
7.3
7.3
7.2
7.4
7.3
7.4
7.4
7.4
7.3
7,3
7.3
7.3
7,4
7,«
7.4
7.4
7.4
7.4
7.4
.0
.0
.0
,0
18
17
17
18
18
17
17
16
17
18
18
18
20
20
20
20
20
20
17
19
19
19
20
21
20
20
21
20
20
20
20
20
20
20
20
20
21
21
21
22
21
22
22
22
0
0
0
0
58
59
59
58
60
60
60
62
61
62
63
63
62
62
62
61
62
63
64
60
61
60
59
60
62
61
60
61
62
63
63
63
62
63
63
63
62
61
63
59
58
57
56
56
0
0
0
0
****************************************************
26
24
24
26
26
25
25
23
25
26
26
26
28
28
28
28
28
28
24
27
26
27
28
29
29
29
30
29
28
29
28
28
28
28
23
28
30
29
29
31
29
31
31
31
0
0
0
0
******
85
86
85
85
88
88
88
92
90
90
92
91
89
89
89
87
89
90
93
85
86
85
83
85
90
88
87
89
89
91
90
90
89
90
90
90
88
86
89
83
81
80
78
79
0
0
0
0
8
8
8
8
8
8
8
7
8
8
8
8
9
9
9
9
9
9
e
8
8
8
1
9
9
9
9
9
9
9
9
9
9
10
9
10
10
10
0
0
0
0
46
46
46
46
47
48
48
50
48
49
50
49
48
48
48
47
48
49
50
46
47
46
45
46
49
48
47
48
48
49
49
49
48
48
48
48
48
47
48
45
44
43
42
43
0
0
0 »
0
**
**
**
**
**
**
**
**
**
. . **
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
'**
**
**
**
**
**
**
**
**
**
**
**
**
* *
**
**
**
********************************
106
KVB11-6017-1266
-------
************************
**
**
**
**
**
**
DATE
TIME
LOAD
MWTH
15 "IN, DAT*
DRY STACK GAS CONCENTRATION
02 C02 CO NO CO NO
VOIX VOLX PPHV PPMV PPMV PPMV
HEAS MEAS MEAS HEAS 3X02 3X02
CO
NG/J
**
**
**
NO ACODE **
NGXJ **
**
******************************************************************************************
*»
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
OX
OX
OX
O/
OX
OX
OX
OX
OX
OX
OX
OX
OX
ox
ox
ox
ox
ox
ox
ox
8X
ex
ex
8X
ex
ex
ox
ox
ox
ox
ox
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ex
ox o
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
6X80
6/80
6X80
6X80
6X80
6X80
OX 0
OX 0
OX 0
OX 0
OX 0
6XBQ
6X80
6xeo
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
** 8X 6/80
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
545
600
615
630
0
0
0
0
0
600
815
830
845
900
915
930
905
1000
1015
1030
1015
1100
1115
1130
1115
1200
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
8.8
8.9
9.0
'.1
7.5
7.6
.0
.0
.0
.0
.0
8.5
e. a
8.5
8.6
8.7
8.7
8.8
8.8
8.9
8.8
8.8
8.3
8.1
8.3
8.0
8.3
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
7.1
7.0
7.0
6.9
8.1
7.8
.0
.0
.0
.0
.0
7. a
7.«
7.4
7.2
7.2
7.2
7.1
7.1
7.0
7.1
7.1
7.4
7.1
7.4
7.3
7.«
.0 8. a 7.3
*********************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
20
19
20
20
18
20
0
0
0
0
0
20
21
21
23
30
29
30
30
30
28
28
23
25
2«
24
23
23
*******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
58
59
59
59
65
66
0
0
0
0
0
55
56
56
55
55
55
54
54
53
53
53
55
56
56
56
57
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
29
28
30
30
24
26
0
0
0
0
0
28
30
30
33
44
42
44
44
44
41
41
32
34
34
34
32
57 32
*****************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
85
88
88
89
86
88
0
0
0
0
0
79
80
80
80
80
80
79
79
79
78
78
78
78
79
80
80
81
*****
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
9
9
9
10
7
e
0
0
0
0
0
9
9
10
1!
14
14
14
14
14
13
13
10
11
11
11
10
10
* * * * *
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
**
**
**
**
»*
**
**
**
**
- **
**
**
**
**
**
**
**
**
**
**
46 **
47 **
48 **
48 **
47 **
48 **
0 **
0 **
0 **
0 **
0 **
43 **
43 **
43 **
43 «*
43 **
43 **
43 **
43 **
42 **
42 **
42 **
42 **
42 **
43 **
43 **
43 **
44 **
******************
107
KVB11-6017-1266
-------
****************************************j
**
**
**
**
**
** DATE
TIME
LOAD
MWTH
15 MIN. DATA
DRV STACK GA3 CONCENTRATION
02 C02 CO NO CO
VOLX VOLX PPMV PPMV PPMV
MEAS MEAS MEAS MEAS 3X02
NO
PPMV
3X02
CO
NGXJ
NO ACOOE
NGXJ
**
**
**
**
**
**
******************************************************************************************
** 8X
ft» 8X
ft 8X
** 8X
** 6X
** 8X
** 8/
** 6X
ft* a/
* 8X
** sx
** 8/
»* 6X
** 6X
** 8X
** 8X
** 8X
** 8/
** OX
** 8/
ft* 8/
* 8/
** 8/
** 8/
** 8/
** 8/
** 8X
** 8X
ft« 8X
** e/
*» 8/
** 8/
ft* 8/
** 8/
** 8X
** 8X
** ex
** 8X
** BX
ftft ex
** ex
** ex
** 8X
** ex
** ox
** ox
** ox
*» ox
6X60
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X60
6X80
6X60
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
6X80
OX 0
OX 0
OX 0
OX 0
1215
1230
1245
1300
1315
1330
1345
1000
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
5100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
8.4
8.1
8.2
8.1
8.0
7.8
7.9
7.7
7.6
7.7
7.8
7.9
7.8
7.7
7.6
7.5
7.5
7.6
7.6
7.8
7.9
7.9
fl.o
8.0
6.7
8.7
8.9
9.0
9.1
9.1
9.2
'.1
9.0
9.2
9.3
9.3
9.1
9.0
8.9
8.5
8.3
6.3
8.2
8.3
.0
.0
.0
.0
7.3
7.1
7.4
7.1
7.5
7.7
7.6
7.7
7.8
7.7
7.7
7.6
7.7
7.7
7.8
7.9
7.9
7.6
7.7
7.7
7.6
7.6
7.5
7.5
7.4
7.4
7.0
7.0
6.9
6.9
6.9
6.9
7.0
6.9
6.8
6.8
6.9
7.0
7.0
7.4
7.4
7.4
7.4
7.4
.0
.0
.0
.0
22
20
22
22
23
41
35
37
39
37
38
39
28
29
30
29
29
31
41
39
40
42
40
39
29
29
35
37
38
38
38
36
37
36
39
41
40
37
32
30
31
35
32
30
0
0
0
0
56
60
60
56
61
63
63
62
63
62
60
55
57
57
58
54
56
56
57
58
58
57
58
59
55
56
55
55
55
56
55
55
56
55
55
56
56
57
57
58
58
59
60
61
0
0
0
0
31
27
31
30
31
56
48
50
52
50
51
53
38
39
40
38
36
41
56
53
55
57
55
54
42
42
52
55
57
57
58
57
55
55
60
63
60
55
47
43
44
49
45
42
0
0
0
0
83
83
84
78
84
66
86
84
84
84
61
75
77
77
78
72
74
75
77
79
79
78
80
81
80
82
82
82
63
64
64
83
84
84
84
86
84
85
85
83
82
83
84
86
0
0
0
0
10
9
10
10
10
18
15
16
17
16
17
17
12
12
13
12
12
13
18
17
16
19
16
17
14
14
17
18
19
19
19
19
18
18
19
20
20
16
15
14
14
16
14
14
0
0
0
0
45
45
45
42
45
46
47
45
45
45
44
41
42
41
42
39
40
40
42
42
43
42
43
44
43
44
44
44
45
46
45
45
45
45
46
46
46
46
46
45
44
45
45
47
0 #
0
0
0 »
**
**
**
**
ft*
ft*
ft*
**
**
.**
ft
ft*
ft*
**
**
ft*
ft*
ft*
**
**
**
ftft
ft*
**
**
**
ft*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
ft*
**
**
**
**
**
108
KVB11-6017-1266
-------
**
**
**
**
**
**
DATE
TIME
LOAD
MXTH
15 MIN, DATA
DRY STACK GAS CONCENTRATION
02 C02 CO NO CO
VOCX VOU PPMV PPMV PPMV
MEAS MEAS MEAS MEAS 3x02
NO
PPMV
3X02
CO
NGXJ
***************************************************************************
**
**
**
**
*»
**
**
**
**
**
**
»*
»*
**
**
ft*
ft
**
**
**
**
**
*»
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
OX
OX
OX
OX
ox
ox
ox
ox
ox
ox
ox
ox
o/
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
8X
8X
ex
ex
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
7X80
7X80
7X80
7X80
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
1115
1130
1145
1200
*****************
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
6.5
6.5
6.6
6.8
.0
.0
.0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
8.1
8.1
8.0
7.9
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
18
36
33
29
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
51
53
55
49
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
22
44
41
36
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
63
65
68
62
***************************************************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
7
14
13
12
**
**
**
NO ACODE *»
NGXJ **
**
***************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
o
0
0
0
0
0
o
o
0
0
0
0
o
0
0
0
o
o
o
0
0
o
0
0
0
**
**
**
**
**
**
**
* A
*»
**
**
**
**
**
**
**
**
**
**
**
**
*
**
**
**
**
**
**
**
**
**
**
**
**.
**
**
**
**
**
**
**
**
**
**
34 **
35 **
37 «*
33 **
t**********************
109
KVBll-6017-1266
-------
**
**
**
**
**
**
*****
** ex
** ex
** 8X
** 8/
** ax
** ax
** a/
** ex
** a/
** a/
** ax
** ex
** ax
** ex
** ex
** ex
** ax
** ax
** ax
** ex
** ax
** ax
** ax
** ex
** ex
** ex
* ax
** ax
** ex
** 8X
** ex
** ex
** ex
** ex
** ex
** ex
** ax
** ex
** ex
** ex
** ex
** ex
** ex
** ex
** ox
** ox
** ox
** OX
-----"""-""»»-»"'«"'<'""'*»»«»«»»*«********************lHKk«*»******»***»»l(,
15 MIN. DATA
DRY STACK GAS CONCENTRATION
DATE
****»*!
7X80
7X80
7X80
7X60
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X60
7X80
7X60
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X80
7X60
7X80
7X60
7X80
7X80
7X80
7X80
7X80
7X80
7X80
OX 0
OX 0
OX 0
OX 0
.TIME
*******
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
0
LOAD
MWTH
****** 1
.0
tO
.0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
02
VOLX
MEAS
k ****** i
6.3
6.6
6.5
5.8
5.4
6.4
6.1
5.9
6.4
6.4
6.3
6.4
6.5
6.3
5.8
6.1
6,8
6.9
7.3
e.4
7.0
7.2
7.4
6.9
7.0
6.2
6.3
6.6
6.5
5.7
5.9
6.2
5.6
6.0
6.4
6.7
6.6
6.3
5.4
5.1
5.0
5.2
5.5
5.5
.0
.0
.0
.0
C02
VOLX
MEAS
t******i
8.2
8.0
7.3
8.6
8.8
8.3
8.4
8.6
8.2
8.3
6.3
e,4
8.3
«.3
e.a
e.6
8,1
e.o
7.8
7.5
7.8
7.9
7.9
8.2
6.1
6.7
8.6
8.5
6.4
8.9
8.9
8.8
9.0
8.8
8.6
8.5
8.5
8.7
9.2
9.4
9.4
9.4
9.1
9.1
.0
.0
.0
.0
CO
PPMV
MEAS
k * * * * * ifci
38
24
16
66
68
25
50
34
20
45
22
63
55
52
50
31
24
24
36
73
25
22
28
40
26
30
25
66
53
75
32
32
35
38
11
25
25
25
48
40
40
42
41
28
0
0
0
0
NO
PPMV
MEAS
t******(
58
60
61
50
53
53
55
59
58
52
51
52
52
53
, 57
58
48
48
46
45
48
43
42
48
58
53
51
50
51
50
49
53
50
51
51
50
51
52
53
50
55
51
53
53
0
0
0
0
CO
PPMV
3X02
t ****** 1
46
30
22
78
78
30
60
40
24
55
26
77
68
63
59
37
30
30
47
104
32
28
37
51
33
36
30
82
65
88
38
38
40
45
13
31
31
30
55
45
45
47
47
32
0
0
0
0
NO
PPMV
3X02
********
71
76
75
59
61
65
66
70
71
64
62
64
64
64
67
70
60
61
60
64
61
56
55
61
74
64
62
62
63
58
58
64
58
61
62
63
63
63
61
56
61
58
61
61
0
0
0
0
CO
NG/J
k******<
15
10
7
25
25
10
19
13
8
IB
8
25
22
21
19
12
10
10
15
34
10
9
12
16
11
12
10
27
21
29
12
12
13
15
4
10
10
10
16
14
14
15
15
10
0
0
0
0
NO ACODE
NG/J
>************!
38
41
41
32
33
35
36
38
38
34
33
34
35
35
36
38
33
33
32
34
33
30 -
30
33
40
35
33
33
34
31
31
35
31
33
34
34
34
34
33
30
33
31
33
33
0
0
0 »
0 *
»***
**
* «
**
**
**
**
***
**
**
**
**
**
**
**
**
**
**
**
**
**
**
*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
* *
**
**
**
**
**
**
**
**
**
********<
110
KVBll-6017-1266
-------
******************************************************************************************
**
**
**
**
**
** DATE
A A A A A
** ox
** ox
** ox
** ox
** ox
** ox
* ox
** ox
** ox
** ox
** ox
** ox
** ox
** ox
** ox
** ox
*» ox
** ox
** ox
** ox
«* ex
** 8X
** 8X
** BX
** 8X
** ex
** 8X
** 8X
** 8X
** 8X
** ex
«* 8X
** ex
** ex
** ex
** ex
** 8X
** BX
** 8X
** 8X
** 8X
** BX
** ex
** ex
** ex
** 8X
** BX
** ex
*****
x w m m K n
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
8/80
8X80
8X80
8X80
8X80
8X8Q
8X80
8X80
8X80
8X80
8X80
8X80
8X80
8X80
8X80
8X80
8X80
8X80
8X80
8X80
8X80
8X80
8X80
8X80
8X60
8X80
8X80
8X80
TIME
A A A A A A
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
545
600
615
630
645
700
715
730
745
800
815
830
845
9flO
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
*************
LOAD
MWTH
A A A A A
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
*****
15 MIN. DATA
DRY STACK CAS CONCENTRATION
02 C02 CO NO CO
VOL* VOL* PPMV PPMV PPMV
MEAS
tt A A A A
7
6
4
3
4
4
4
4
4
4
4
4
5
6
6
6
6
5
6
5
6
6
5
5
5
5
6
5
*****
H w w J
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.8
.1
.1
.3
.2
.5
.0
.5
.4
.8
.7
.8
.5
.8
.5
.2
.4
.6
.2
.8
.1
.2
.7
.9
.9
.7
.1
.9
MEAS
1 A A A A A
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
7.7
e.7
io!o
9.7
9.5
9,8
9.5
9.6
9.4
9.5
9.4
9.0
8.3
8.4
8.4
8.4
8.9
8.6
8.8
6.5
8.5
8.8
8.7
8.7
8.8
8.6
8.5
*********
MEAS MEAS
kAAlkAAAAAAAA
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
16
17
296
493
341
286
369
270
290
207
211
208
181
53
74
5
29
16
10
56
24
65
20
7
93
7
10
63
************
H <« H K
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
53
57
63
67
62
62
64
62
62
60
60
60
56
54
50
48
50
53
54
56
57
58
54
52
54
56
58
58
****
3X02
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
21
20
315
501
365
312
39Q
294
314
230
233
231
210
67
91
6
35
IB
12
66
29
79
23
8
110
8
12
75
****** *
NO
PPMV
3X02
' A A A A A A
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
72
68
67
68
66
67
67
67
67
66
66
66
65
68
62
58
61
62
65
66
68
70
63
62
64
65
70
69
*******
CO
NGXJ
tAAAAAAl
o
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
7
6
104
165
120
103
129
97
103
75
76
76
69
22
30
2
11
6
4
21
9
26
7
2
36
2
3
24
*******
**
**
**
NO ACODE **
NGXJ **
**
AAAAAAA^A * * * * * *
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
..
**
**
**
**
**
**
»*
**
**
**
**
**
**
**
**
**
**
**
**
39 **
37 **
36 **
36 **
36 **
36 **
36 **
36 **
36 **
36 **
35 **
36 **
35 «*
37 **
33 **
31 «*
33 **
33 «*
35 **
36 **
37 **
38 **
34 **
33 **
34 **
35 **
36 **
37 **
****************
111
KVB11-6017-L266
-------
**
**
**
**
»*
**
* *
**
**
**
**
**
**
**
**
»*
**
»*
**
**
**
**
»*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
»*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
DATE
t A A Ik
a/
8/
8/
e/
8/
a/
a/
8/
a/
a/
a/
a/
a/
a/
a/
a/
a/
a/
a/
a/
a/
a/
a/
a/
a/
a/
8/
8/
a/
a/
a/
o/
o/
o/
o/
o/
o/
o/
o/
o/
o/
o/
o/
o/
o/
o/
o/
o/
******
if W m w W
6/80
8/80
8/60
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/60
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
O/ 0
O/ 0
O/ 0
O/ 0
O/ 0
O/ 0
O/ 0
O/ 0
O/ 0
O/ 0
O/ 0
O/ 0
O/ 0
O/ 0
O/ 0
O/ 0
O/ 0
HKHO HHKHMHMMMXX
LOAD
TIME MWTH
n yt * -m n
02
VOLX
MEAS
*****************************
15 MIN. DATA
DRY STACK GAS CONCENTRATION
C02 CO NO CO
VOLX PPMV PPMV PPMV
MEAS MEAS MEAS 3X02
********
NO
PPMV
3X02
******
CO
NG/J
****************
**
**
**
NO ACUOE **
NG/J **
* *
**************** *********************»***************jmaa**********************
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
19/45
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
**************
.0
.0
.0
.0
.0
.0
.0
iO
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
******
6.0
6.1
5.9
6.0
6.0
6.2
6.0
5.8
5.4
5.6
5.5
5.5
5.7
6.0
6.1
6.5
6.3
6.8
6,9
7.0
6.7
7.0
6.4
10.0
6.8
7.2
8.4
8.7
8.1
7.0
8.5
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
*****
8.
8.
8.
8.
8,
8.
8.
9.
9^
9,
9.
8,
8.
8.
8.
8.
8.
8.
6.
8.
8.
7.
5.
8.
7.
6.
6.
7.
8.
6.
t
,
t
,
,
.
.
,
,
,
,
*
,
,
*****
5
6
9
9
9
7
6
0
2
0
1
1
9
7
7
5
6
3
2
1
3
0
0
4
2
9
9
7
2
0
9
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
53
64
74
27
50
13
10
44
16
45
15
61
15
1
3
33
47
20
20
19
19
14
32
42
25
19
32
31
0
17
13
0
0
0
0
0
0
0
0
0
o
0
0
0
0
0
0
0
************
59
60
61
63
66
67
69
73.
77
68
62
64
64
65
65
67
68
68
68
68
67
67
66
55
62
59
51
47
43
43
36
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
63
77
88
32
60
15
12
52
18
52
17
70
17
1
3
41
57
25
25
24
23
16
45
68
31
24
45
45
0
21
16
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
70
72
72
75
79
81
82
86
88
79
72
74
75
78
78
83
83
66
86
87
64
86
94
90
78
77
73
68
60
55
51
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
********************
21
25
29
10
19
5
3
17
6
17
5
23
5
0
1
13
19
8
8
8
7
5
15
22
10
8
15
15
0
7
6
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
38
39
39
41
43
44
44
46
48
43
39
40
40
42
42
45
45
46
47
47
45
46
51
48
42
41
39
37
32
30
as
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
* *
**
**
* *
**
* *
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
* *
**
**
**
**
**
* *
**
**
**
**
**
**
**
**
**
**
**
**
**
* *
**
**
* *
**********************
112
KVB11-6017-1266
-------
*******************************<
t*******************************
**
**
**
**
**
** DATE
AAAAAAAAAAA
** ox ox o
»* OX OX 0
*» OX OX 0
»* OX OX 0
** OX OX 0
** OX OX 0
*« OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
»* OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
*'* OX OX 0
** OX OX 0
** OX OX 0
*» OX OX 0
*» OX OX 0
«* 6X12X80
** 6X12X80
** 8X12X80
** 8X12X80
** 8X12X80
** 8X12X80
** 8X12X80
*» 6X12X80
** 8X12X80
** 8X12X80
*» 8X12/80
** 8X12X80
»» 6/12/60
** 6/12X80
*« 8X12X80
** 8X12/80
** 8/12/80
** 8X12X80
** 8X12/80
** 8/12/80
** 8/12/80
** 8/12/80
** 8X12X80
*» 8X12/80
** 8/12/80
******** ***
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
A A A A A A A
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
600
615
630
645
700
715
730
745
800
815
830
845
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
*******
LOAD
MWTH
A A A A A
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
*****
02
VOLX
MEAS
AAAAAAAA
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
6.5
7.3
7.7
7.1
10.0
7.3
7.9
6.6
6.7
-1.0
-1.0
-1.0
-1.0
6.3
9.8
11.1
6.1
7.0
9.1
6.8
8.1
6.6
7.8
6.5
9.8
********
C02
VOLX
MEAS
AAAAAAAA
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
8.3
7.4
7.8
5!5
7."
7.2
8.1
7."
-1.0
-1.0
-1.0
-1.0
7.3
4.3
4.9
7.5
7.5
5.9
6.0
6.8
8.1
7.1
8,2
4.9
********
CO
PPMV
MEAS
A A A A A A
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
36
60
It
12
23
24
20
34
47
-1
-1
-1
-1
27
11
11
30
31
14
26
8
28
7
27
6
******
NO
PPMV
MEAS
A A A A A A A
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
52
52
50
53
48
50
50
44
44
-1
-1
-1
-1
46
42
45
53
41
37
46
45
52
52
58
49
*******
CO
PPMV
3X02
A A A A A A A
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
44
78
14
15
37
31
27
43
59
0
0
0
0
33
17
20
41
39
21
33
11
35
9
33
9
*******
NO
PPMV
3X02
A A- A A A A A !
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
64
68
67
66
78
65
68
55
55
0
0
0
0
56
67
62
74
52
56
58
62
65
71
72
79
CO
NG/J
' A A A A A A :
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
14
26
4
5
12
10
9
1 1
19
0
0
0
0
10
5
6
13
13
7
10
3
H
3
11
3
**
**
**
NO ACOOE **
NG/J «*
**
lAAAAAAAAAAAAAAAA
o **
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
**
**
**
**
**
**
**
**
**
»*
**
**
**
**
»*
**
**
**
**
**
**
**
35 **
37 **
36 **
37 «*
42 **
35 **
37 **
30 **
30 **
0 C **
0 C **
0 C **
0 C **
30 **
36 **
44 **
40 **
28 «*
30 *»
31 **
34 *»
3S **
38 **
39 **
42 **
*******************************
113
KVB11-6017-1266
-------
II***********,
**
**
**
**
**
** DATE
wwAftftftftA&ikjt;
** 8/12/80
** 8/12/80
** 8/12/80
** 8/12/80
** 8/12/80
** 8/12/80
»* 8/12/80
»* 8/12/80
** 8/12/80
«* 8/12/80
** 8/12/80
*« 8/12/80
*« 6/12/80
*« 8/12/80
** 8/12/80
** 8/12/80
** 8/12/80
** 8/12/80
** 8/12/80
** 8/12/80
** 8/12/80
»* 8/12/80
** 8/12/80
** 8/12/80
** 8/12/80
** 8/12/80
** 8/12/80
** 8/12/80
** 8/12/80
AA 8/12/60
** 8/12/80
** 8/12/80
AA 8/12/80
** 8/12/80
*» 8/12/80
* 8/12/80
*» 8/12/80
** 8/12/80
*A 8/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 8/12/80
*» 8/12/flO
* 6/12/80
*« O/ O/ 0
** O/ O/ 0
* O/ O/ 0
15 MIN. DATA
DRT STACK GAS CONCENTRATION
TIME
fe ft ft A A * *
1215
1230
1215
1300
1315
1330
1305
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1615
1830
1645
1900
1915
1930
19<(5
2000
2015
2030
2045
2100
2115
2130
21«5
2200
2215
2230
2245
2300
2315
0
0
0
LOAD
MWTH
02
vou
MEAS
C02
VOLX
MEAS
CO
PPMV
MEAS
NO
PPMV
MEAS
CO
PPMV
3X02
NO
PPMV
3X02
CO
NG/J
NO ACUDE
NG/J
**
**
**
**
AA
**
************************ *AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
6,3
7.9
6.5
6.9
6.7
1.0
"1.0
1.0
1.0
6.8
-1.0
8.9
6.7
7.5
6.8
8.8
6.7
9.9
9.7
8.9
10.7
10.5
9.2
11.1
9.4
10.4
10.8
8.9
10.0
10.1
7.5
10.6
8.5
9.4
10.1
9.5
9.1
9.1
9.2
8.0
9.2
7.9
9.1
9.0
9.8
.0
.0
,0
6.9
6.9
8.1
8.0
6.3
-1.0
1.0
1.0
1.0
. 8.0
1.0
6.5
6.1
7."
6.0
*.«
6.1
5.1
5.8
6.3
4.8
4.5
6.6
«.3
5.7
5.3
1.6
6.3
4,9
5.6
7.4
4.8
6.6
5.7
5,3
5.9
6.2
6,4
6.2
7.3
t.3
7.4
6.4
6.5
5,7
.0
.0
.0
21
13
26
33
32
-1
-1
1
-1
36
-1
12
29
4
19
12
16
37
38
-1
7
21
6
15
38
5
42
0
20
0
26
12
42
17
30
14
11
28
0
21
4
20
37
11
19
0
0
0
60
49
21
38
40
1
1
1
1
33
1
34
41
36
42
37
42
30
33
34
29
28
35
27
34
31
29
34
29
32
39
30
36
32
32
34
36
36
36
40
36
40
36
36
35
0
0
0
29
17
32
42
40
0
0
0
0
45
0
17
36
5
24
17
20
60
60
1
12
36
9
27
59
8
74
0
32
0
34
20
60
26
49
21
16
42
0
29
6
27
56
16
30
0
0
0
85
67
26
48
50
0
o
o
o
41
0
50
51
50
53
54
52
46
52
50
50
48
53
49
52
52
51
50
47
53
52
52
51
49
53
53
54
5«
55
55
55
55
54
54
56
0
0
0
9
5
10
13
13
0
o
o
o
15
o
5
12
1
7
5
6
19
20
0
4
H
3
9
19
2
24
0
10
o
11
6
20
8.
16
7
5
14
0
9
2
9
18
5
10
0
0
0
46
36
14
26
27
0 C
Or
\i
Or
\f
0 C
V V
22 - - _
0 C
27
28
27
28
29
28
26
28
27 0
27
26
29
26
28
28
27
27
25
28
28
28
28
27
26
28
29
29
29
30
29
29
29
29
30
0 *
0 »
0
**
A A
**
AA
**
A A
£ £
A A
A A
**
A A
A A
A*
A A
AA
A A
A A
A A
AA
A A
AA
* A
A A
A A
A A
A A
AA
A A
A A
A A
A A
A A
A A
AA
A A
A A
A A
A*
A *
AA
A A
A A
A A
A*
* *
A*
A A
AA
kAAAAAAAA* 1
(AAAAAAAAAAAAAAAAAAAAAAAA
114
KVBll-6017-1266
-------
************
**
**
**
**
**
«* DATE
AAAAAAAAAAA'
»» ox ox o
** OX Of 0
** OX O/ 0
** OX OX 0
»* O/ O/ 0
* OX O/ 0
** O/ OX 0
** ox o/ o
** OX OX 0
** OX OX 0
** ox ox o
»* OX OX 0
** OX OX 0
*« OX OX 0
*« ox ox o
** OX OX 0
** ox ox o
** ox ox o
** OX O/ 0
** ox ox o
** ox ox o
** OX OX 0
*« OX OX 0
** 8X13X80
** 8X13X60
** 8X13X80
** 8/13X60
** 8X13/80
** 8/13/80
** 8/13/80
** 8/13/80
*» 8/13/80
** 8/13/80
* 8/13/80
** 8/13/80
** 8/13/80
»* 8/13/80
** 8/13/80
«* 8/13/80
** 8X13X80
** 8X13X80
** 8X13X80
** 8/13/80
* 8/13/80
*« 8/13X80
** 8X13X80
** 8/13/80
* 8X13/80
t*************************************************************'
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
600
615
630
645
TOO
715
730
745
800
815
830
645
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MWTH
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
tO
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
***********************
02
VOLX
MEAS
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
7.1
7.3
7.3
7.0
6.8
6.6
7.1
6.5
6.9
7.0
7.1
6.7
6.9
6.7
6.6
6.7
6.5
6.2
6,«
6.3
6.7
6.8
6.5
6.8
6.8
C02
voux
MEAS
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
0
.0
.0
.0
tO
.0
.0
8.2
a.i
8.1
8.2
8. a
8.6
8.2
6.6
8.3
8.4
8.2
.3
.0
.2
.3
.2
.3
8.6
8. a
8.5
8.2
8.1
8.3
8.0
8.0
**************
CO
PPMV
MEAS
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
54
26
18
27
14
66
17
4
25
14
4
75
48
54
29
41
8
22
29
20
28
28
56
41
24
********
NO
PPMV,,
MEAS
kAAAAAAA
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
43
03
43
44
44
44
44
44
44
44
44
43
42
42
42
42
42
43
42
42
42
42
42
42
42
********
CO
PPMV
3X02
It It It It 1t It '
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
70
36
23
34
17
62
22
4
31
18
5
94
61
68
36
51
9
26
35
24
35
35
69
52
30
******
NO
PPMV
3X02
1 A A A A A A '
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
55
56
56
56
55
55
57
54
56
56
57
54
53
52
52
52
52
52
51
51
52
53
52
53
53
*******
CO
NG/J
' A A A ft A A i
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
23
12
7
11
5
27
7
1
10
s
i
31
20
22
H
17
3
8
11
8
11
11
22
17
10
*******
****************
**
**
**
NO ACODE **
NGXJ **
**
********^********
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
30 **
30 **
30 **
30 **
30 **
29 **
30 **
29 **
30 **
30 **
30 **
29 **
29 **
28 **
28 **
28 **
28 «*
28 **
28 **
27 **
28 **
28 **
28 **
28 **
28 **
*****************
115
KVBll-6017-1266
-------
O***************************
**
**
**
**
**
** DATE
***********^
** 6/13/80
»* 8/13/60
*« 8/13/80
** 8/13/80
** 8/13/80
** 8/13/80
»« 8/13/80
** 6/13/80
** 6/13/80
8/13/80
** 8/13/60
*« 8/13/80
** 8/13/80
* 8/13/80
** 6/13/80
*» 8/13/80
** 8/13/80
** 6/13/80
** 8/13/80
** 8/13/80
** 8/13/80
*» 8/13/80
* 8/13/80
»» 8/13/80
** 8/13/60
* 8/13/80
** 8/13/80
«* 8/13/80
** 6/13/80
** 8/13/80
** 8/13/80
** 6/13/80
** 8/13/80
* 8/13/80
** 6/13/80
** 8/13/80
«* 8/13/80
** 8/13/80
** 8/13/80
** 8/13/80
** 8/13/80
** 8/13/80
** 8/13/60
** 6/13/80
* O/ O/ 0
*» O/ O/ 0
*» O/ O/ 0
** O/ O/ 0
15 MIN, DATA
DRY STACK GAS CONCENTRATION
TIME
i******
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1600
1615
1630
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
0
LOAD
MWTH
* * * 4r* * 4
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
02
VOLX
MEAS
>******!
6.9
6.8
6.7
7.0
7.0
7.1
6.7
6.6
6.9
6.9
6.6
6.8
6.8
6.8
6.6
6.4
6.4
6.5
6.4
6.4
6.6
8.6
.1
.6
.3
.8
.1
.4
7.3
9.3
7.2
8.4
6.9
6.3
6.9
6.9
6,9
9.3
6.7
8.1
7,0
7.9
6.7
10.1
.0
.0
.0
.0
A******************************,
C02
VOLX
HEAS
********
6.0
6.0
8.0
7.7
7.8
7.6
7.6
8.0
9.7
7.7
7.9
7.8
7.8
7.8
7.8
7.8
7.9
7.7
7.8
7,8
7.6
5.5
5.6
5.5
6!s
5J9
7.0
5.3
7.2
6.0
7.4
7^4
7.4
7.4
5.1
7.5
6.2
7.3
7,1
7.4
4.4
.0
.0
.0
.0
k ******* j
CO
PPMV
HEAS
»**»»*
36
25
27
68
91
93
95
94
23
30
57
7
20
33
23
15
14
17
16
18
15
22
30
33
36
2
23
13
11
38
8
0
7
4
6
7
5
32
6
2
9
8
7
1
0
0
0
0
NO
PPMV
MEAS
********
42
42
42
39
40
40
40
42
67
37
36
38
40
42
42
31
11
43
43
43
42
34
36
54
34
37
36
36
40
34
41
36
41
37
41
41
41
33
41
37
42
42
41
31
0
0
0
0
CO
PPMV
3X02
********
46
31
34
87
117
120
119
117
29
38
71
a
25
41
28
18
17
21
19
22
18
32
45
48
55
2
32
18
,14
58
10
0
8
5
7
6
6
49
7
2
11
11
8
1
0
0
0
0
NO
PPMV
3X02
*****
53
53
52
50
51
51
50
52
85
47
47
48
50
53
52
38
13
53
53
53
52
49
54
49
52
50
50
51
52
52
53
51
52
52
52
52
52
50
51
51
54
57
51
51
0
0
0
0
CO
NG/J
********<
15
10
n
28
38
39
39
38
9
12
23
2
8
13
9
6
5
6
6
7
6
10
15
15
18
0
10
6
4
19
3
0
2
1
2
2
2
16
2
0
3
3
2
0
0
0
0
0
NO
NG/J
*******
29
28
28
27
27
28
27
28
46
25
25
26
27
26
26
20
7
28
28
28
28
26
29
26
28
27
27
27
28
28
29
27
28
28
28
28
28
27
2fl
28
29
31
28
27
0
0
0
0
*****************************************
**
**
**
ACOOE **
**
**
**********
**
**
**
**
**
**
**
**
**
**
*»
**
**
**
**
**
**
**
**.
**
**
**
**
**
*»
**
**
**
**
**
**
**
* *
**
**
* *
**
**
**
* *
**
**
**
**
**
* * *
* *»
**
**********
116
KVB11-6017-1266
-------
****************************************4
**
**
**
**
**
** DATE
****** *****!
** 8/14/80
** 8/14/80
** 8/14/80
»* 8/14/80
** 8/14/80
** 8/14/80
** 8/14/80
** 8/14/80
** 8/14/80
** 8/14/80
** 8/14/80
* 8/14/80
** 8/14/60
** 8/14/80
** 8/14/80
** 8/14/80
** 8/14/80
«* 8/14/80
** 8/14/80
** 8/14/80
«* 8/14/80
** 8/14/80
** 8/14/80
** 8/14/80
*« 8/14/80
* 8/14/80
** 8/14/80
** 8/14/80
** 8/14/80
** 8/14/80
«* 8/14/80
** 8/14/80
* 8/14/80
** 8/14/80
** 8/14/80
** 8/14/80
** 8/14/80
*» 8/14/80
** 8/14/80
** 8/14/80
«* 8/14/80
** 8/14/80
** 8/14/80
** 8/14/80
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
******* **«*T
15 WIN. DATA
DRY STACK GAS CONCENTRATION
TIME
IT******
1215
1230
1245
1300
U15
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
22«5
2300
0
0
0
0
LOAD
MWTH
*******
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
02
VOLX
MEAS
l******1
6.1
5.9
6.4
6.4
5.9
6.1
6.2
6.2
6.1
6.3
6.0
6.5
6.2
6.5
6.2
6.6
6.2
6.3
6.2
6.2
6.1
6.6
6.3
6.5
6.5
6.3
6.2
6.5
6.2
.3
.2
.7
.0
.8
.6
6.7
6.8
7.0
7.0
7.0
6.9
7.1
6.8
6.9
.0
.0
.0
.0
C02
VOLX
MEAS
i******
8.4
8.5
8.2
8.2
8,6
8.3
8.4
8.4
8,4
8.2
8.5
6.1
8.2
8.0
8.2
.1
,3
.3
.3
.3
8.4
8.1
8.3
8.0
8,1
8.2
8.3
8,2
8.3
8.3
8.3
8.0
7.6
7.9
8.0
8,0
7.9
7.8
7.8
7,6
7.8
7.8
7.9
7.8
.0
.0
.0
.0
CO
PPMV
MEAS
********
8
100
17
66
20
8
62
25
7
79
79
61
48
42
49
44
39
34
9
25
40
22
29
22
15
13
36
40
34
49
16
38
14
14
10
10
11
12
10
12
14
2
11
13
0
0
0
0
NO
PPMV
MEAS
>*«»***
45
45
44
45
45
44
44
45
44
45
45
44
44
44
50
45
46
45
45
45
45
45
45
44
45
43
44
44
45
44
44
43
43
45
43
43
44
43
44
43
43
43
43
43
0
0
0
0
k***« ************************************
CO
PPMV
3X02
********
9
119
20
81
23
9
75
30
8
96
94
75
58
52
59
55
47
41
10
30
48
27
35
27
18
15
43
49
41
60
19
47
16
17
12
12
13
15
12
15
17
2
13
16
0
0
0
0
NO
PPMV
3X02
t * *** ** **
54
53
54
55
53
53
53
54
53
55
54
54
53
54
60
56
56
55
54
54
54
56
55
54
55
52
53
54
54
53
53
54
55
57
53
54
55
55
56
55
54
55
54
54
0
0
0
0
****************
CO
NG/J
******
3
39
6
26
7
3
24
10
2
31
31
25
19
17
19
18
15
13
3
10
15
9
11
9
6
5
ia
16
13
19
6
15
5
5
4
4
4
5
4
5
5
0
4
5
0
0
0
0
NO
NG/J
******
29
29
29
30
29
28
29
29
28
29
29
29
29
29
33
30
30
29
29
29
29
30
29
29
30
28
29
29
29
29
29
29
30
30
29
29
30
30
30
30
29
30
29
29
0
0
0
0
********** *
**
**
**
ACODE **
**
**
********** *
**
**
**
**,
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
.. - **
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
* *
**
**
**
**
**
**
» **
**
* **
» **
***********
117
KVBll-6017-1266
-------
*»*********,
**
**
**
**
**
»* DATE
************
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
«* ox o/ o
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
»* O/ O/ 0
** o/ o/ o
*» O/ O/ 0
** O/ O/ 0
** O/ O/ 0
*» O/ O/ 0
** O/ O/ 0
*'« O/ O/ 0
* O/ O/ 0
** 6/14/80
** 8/14/eo
*» 8/14/flQ
** 8/i4/eo
** a/14/80
** 8/14/80
** 8/14/80
*» 8/14/80
** 8/14/80
** 8/14/80
*» 8/14/80
«» 8/14/80
** 8/14/80
** 8/14/60
*» 8/14/80
** 8/14/80
«* 8/14/80
«* 8/14/80
** 8/14/80
** 8/14/80
** 8/14/80
«* 8/14/80
*» 8/14/80
** 8/14/80
* 8/14/80
** 8/14/80
* 8/14/80
** 8/14/80
k*************************************************************4
15 MIN. DATA
DRY STACK GAS CONCENTRATION
.TIME
*******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
545
600
615
630
645
700
715
730
745
800
815
830
845
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1105
1200
LOAD
MHTH
*******
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
02
VOLX
MEAS
>****»*<
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
9.6
8.5
6.8
5.9
6.2
6.3
5.9
6.0
5.6
5.9
5.6
5.7
5.8
6.0
6.0
6.2
5.8
5.7
6.2
6.2
6.2
6.3
6.4
5.9
5.8
5.9
6.1
6.0
C02
VOLX
MEAS
>**»***<
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
0
.0
,0
.0
.0
fl.e
6.2
7.5
8.2
8.0
6,0
8.S
9.3
8.4
8.3
8.«
8.4
8.2
8.1
8.1
8.0
8.3
8.4
7.9
7.9
8.0
8.3
8.3
8.6
8.6
8.6
8.4
8.5
CO
PPMV
MEAS
k*******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
22
23
33
25
62
9
17
5
7
19
11
24
11
0
31
32
2
41
30
42
39
57
11
15
17
11
31
56
**********************************************
NO
PPMV
MEAS
******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
31
37
41
43
42
42
44
44
44
44
44
44
44
44
44
44
44
45
44
43
44
44
53
45
44
45
45
45
CO
PPMV
3*02
NO
PPMV
3X02
*************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
34
33
41
29
75
11
20
6
8
22
12
28
13
0
37
38
2
48
36
51
47
69
13
17
20
13
37
67
**************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
49
53
52
51
51
51
52
52
51
52
51
51
52
52
52
53
52
52
53
52
53
53
65
53
52
53
54
54
* ** * *
CO
NG/J
k*** *************
**
**
* *
NO ACODE **
NG/J **
**
*************************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
11
10
13
9
24
3
6
1
2
7
4
9
4
0
12
12
0
15
12
, 16
15
23
4
5
6
4
12
22
**<>*****<
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
26 **
28 **
28 «*
27 *«
27 **
27 «*
28 **
28 **
27 **
28 **
27 **
28 **
28 **
28 **
28 **
29 **
26 **
28 **
29 **
28 **
29 **
29 **
35 **
29 **
28 **
29 **
29 **
29 **
t****************
118
KVBll-6017-1266
-------
k******************************
**
**
**
**
**
«* DATE
15 WIN, DATA
DRY STACK GAS CONCENTRATION
02 C02 CO NO CO
TIME
LOAD
HWTH
VOLX
MEAS
VOLX
MEAS
PPMV
MEAS
PPMV
MEAS
PPMV
3X02
NO
PPMV
3X02
CO
NG/J
**
**
**
NO ACODE **
NG/J **
**
**************************************************** **************************************
«* 0/0/0
** O/ O/ 0
*» O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
*« O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
* O/ O/ 0
«* O/ O/ 0
** O/ O/ 0
*« O/ O/ 0
*« O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** 6/15/60
«» 8/15/80
** 8/15/80
** 8/15/80
** 8/15/80
** 8/15/80
** 8/15/80
»* 8/15/80
*« 8/15/80
** 8/15/80
** 8/15/80
** 8/15/60
«* 8/15/80
** 8/15/80
*« 8/15/80
** 8/15/80
** 8/15/80
** 8/15/80
** 8/15/80
«* 8/15/80
*« 8/15/80
** 8/15/80
* 6/15/80
** 8/15/60
** 6/15/80
** 8/15/80
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
545
600
615
630
645
700
715
730
715
800
815
830
845
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
.0
.0
0
.0
.0
.0
.0
.0
.0
.0
.0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
6.8
5.5
5.8
*.3
6.1
6.5
6.1
6.0
6.1
s.'
5.6
6.0
5.9
6.4
5.8
5.3
5.2
1.9
5.9
6.5
6.3
5.9
6.6
6.8
6.3
6.4
*******************************
iO
.0
.0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
8.0
9.0
«.7
8.5
8.5
8.3
8.5
8.7
6.6
8.7
6.9
8.6
8.7
8.4
8.7
6.9
9.0
<>,1
6.5
6.2
a. a
6,5
8,1
7.9
8.3
8.2
******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
57
27
14
10
28
57
1
15
9
25
20
6
10
58
16
35
37
43
24
19
32
8
5fl
59
65
5fl
*******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
43
46
42
45
45
43
43
45
45
45
46
45
46
45
45
44
45
45
43
43
44
4U
44
43
43
44
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
72
31
16
12
33
70
1
18
10
29
23
7
11
71
18
40
42
48
28
23
39
9
67
74
79
71
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
54
53
49
55
54
53
52
54
54
53
53
54
54
55
53
50
51
50
51
53
53
52
55
54
52
54
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
23
10
5
4
U
23
0
5
3
9
7
2
3
23
6
13
13
15
9
7
12
3
22
24
26
23
******************************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
o
o
o
0
0
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
»*
**
**
**
29 **
29 **
27 **
29 **
29 **
28 **
28 **
29 **
29 **
29 **
29 **
29 **
29 **
30 **
28 **
27 **
27 **
27 **
27 **
28 **
29 **
28 **
29 **
29 **
28 **
29 **
****************
119
KVB11-6017-1266
-------
***********
**
**
**
**
**
** DATE
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
LOAD
HWTH
02
VOLX
HEAS
C02
VOLX
HEAS
CO
PPHV
MEAS
NO
PPMV
MEAS
CO
PPMV
3X02
NO
PPMV
3X02
CO
NG/J
NO ACODE
NG/J
******************************* ********** ******* * * * *** ********«*********************,*
** 6/15/80
** 8/15/80
** 8/15/80
** 8/15/80
** 8/15/80
** 8/15/80
** 8/15/60
*» 8/15/80
*» 8/15/80
** 6/15/80
** 8/15/80
** 8/15/80
** 8/15/80
** 8/15/80
** 8/15/80
«* 8/15/80
** 8/15/80
* 8/15/80
** 8/15/80
** 8/15/80
** 8/15/80
** 6/15/60
** 6/15/80
** 8/15/80
** 8/15/80
*« 8/15/80
*» 8/15/80
** 8/15/80
** 8/15/80
*« 6/15/80
** 8/15/80
** 8/15/80
** 8/15/80
** 8/15/80
** 8/15/80
** 8/15/80
»* 8/15/80
** 8/15/80
*« 8/15/80
** 8/15/80
** 8/15/80
»* 8/15/80
** 8/15/80
** 8/15/60
«* O/ O/ 0
** O/ O/ 0
** O/ O/ 0
»* O/ O/ 0
1215
1330
1245
1300
1315
1330
1315
1000
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
19«5
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
0
*****************
.0
.0
.0
0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
5.5
5.6
b.4
6.2
6.8
7.0
6.6
8.2
8.4
9.1
7.3
6.5
6.7
6.7
6,6
6.9
6.9
8.5
6.6
7.3
8.4
9.2
9.8
9.8
6.6
8.4
6.7
8.6
7.2
7.0
6.7
6.8
6.6
6.6
6.9
6.8
6.8
6.9
7.0
7.0
6.9
6.8
6.9
7.1
.0
.0
.0
.0
6.8
8.7
8.2
8.2
7,9
7,8
8.0
6.6
6.5
5.6
7.7
7.9
8.0
7.9
8.0
7,7
7.7
6.4
6.4
7,4
6,6
5,6
5.5
5,2
7.8
6.4
7.8
6,3
7.5
7.7
7.9
7.8
8,0
7.9
7.8
7,9
7.9
7.8
7.8
7.8
7.9
7,9
7.8
7.7
.0
.0
.0
.0
10
30
36
20
35
16
17
26
41
46
32
18
23
14
13
16
15
29
32
15
32
40
3
47
13
28
14
6
16
15
14
in
13
17
15
13
21
24
24
23
30
27
18
13
0
0
0
0
46
46
45
46
45
44
45
39
39
35
43
44
45
44
45
44
44
39
39
43
39
34
35
33
43
37
43
38
42
42
42
42
42
42
43
43
43
43
43
43
40
43
43
42
0
0
0
0
1 1
35
4
-------
t*******************
**
**
**
**
*»
** DATE
***********
** OX OX 0
»* OX OX 0
»« OX OX 0
** OX OX 0
** OX O/ 0
** OX O/ 0
** OX O/ 0
** OX OX 0
** ox ox o
** OX O/ 0
** OX OX 0
* OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** Of O/ 0
** OX O/ 0
** o/ o/ o
"* OX O/ 0
** OX O/ 0
** ox ox o
** 8X18X80
** 8XJ8X80
** 8X18/80
** 8X18X80
** 8X18/80
** 8X18X80
** 8X18X80
** 8X18X80
** 8X18X80
** 8X16X80
** 8X18/80
** 8X18X80
** 8X18X60
»* 8X18X80
»* 8X18/80
*« 8X18/80
** 8X18X80
** 8X18X80
*» 8/18/80
* 8/18/80
«* 8/18/80
** 8/18/80
»* 8/18/80
»* 8/18/80
** 8/18/80
** 8/18/80
** 8X18/80
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
*******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
530
545
600
615
630
645
700
715
730
745
800
815
830
845
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MWTH
********
.0
.0
.0
.0
.0
0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
**************************
02
VOLX
MEAS
*****
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
e.o
6.6
6.7
6.8
6.5
"1.0
-1.0
"1.0
5.8
3.8
5.5
6.1
6.1
6.1
6.«
6.7
6.9
7.0
6. S
7.0
7.6
6.8
6.9
6.7
6.3
6.3
6.9
C02
VOLZ
MEAS
*******
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
7.4
8.2
8.0
8.1
8,0
-1.0
-1.0
1,0
e.4
9.7
8,9
8,6
8.6
8.6
8.2
8.0
7,8
7.7
7.9
7.8
7.2
7.9
7,8
8.0
8.2
8.2
7.7
************
CO
PPMV
MEAS
*******,
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
5
13
11
36
0
-1
-1
"1
303
1
27
3
16
30
10
55
62
45
82
48
2
32
46
82
97
49
64
NO
PPMV
MEAS
»*** ***i
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
40
11
40
42
43
-1
-t
1
43
46
44
43
42
43
42
42
41
42
42
42
40
42
42
43
44
44
42
CO
PPMV
3*02
********
0
0
0
0
0
0
0
.0
0
0
0
0
0
0
0
0
0
0
0
0
0
6
16
13
45
0
0
0
0
406
1
31
3
19
36
12
69
79
57
104
61
2
40
58
103
118
60
81
**********************
NO
PPMV
3*02
******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
55
51
50
53
53
0
0
0
50
48
51
52
50
52
51
52
52
54
53
54
53
53
53
54
53
53
53
****** i
CO
NGXJ
********
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
2
5
4
15
0
0
0
0
13"
0
10
1
6
11
4
22
26
19
34
20
0
13
19
34
39
J9
27
>***»**<
**
**
**
NO ACODE **
NGXJ **
**
*****************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
* *
**
**
**
**
**
JO **
27 **
27 **
28 **
28 **
0 C **
0 C **
0 C **
27 «*
26 **
27 **
28 **
27 **
28 **
28 **
28 **
28 **
29 **
28 **
29 **
29 **
28 **
29 **
29 **
29 **
29 **
29 **
t*** *************
121
KVB11-6017-1266
-------
************************
A********************************************,********************
**
**
**
**
**
** DATE .
************
** 8/18/80
** 8/18/80
** 6/18/80
** 6/18/80
** 6/18/80
* 6/18/80
** 6/18/80
»* 8/18/80
*» 6/18/80
** 8/16/80
*» 8/18/80
*« 8/18/80
*« 8/18/80
** 8/18/80
** 8/18/80
»* 8/18/80
** 8/16/60
** 8/18/80
** 6/18/80
** 8/18/80
** 8/18/80
** 8/18/80
** 8/18/80
** 6/18/80
** 8/18/80
** 8/18/80
** 6/18/80
** 6/18/80
** 8/18/80
** 6/18/80
*« 8/18/80
** 8/18/80
** 8/18/80
** 8/18/80
*« 6/18/80
** 8/18/80
*» 6/18/80
** 8/18/80
«» 8/18/80
** 8/18/80
** 6/18/80
** 8/18/80
** 8/18/80
** 8/18/80
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
t******
1215
1230
1205
1300
1315
1330
1345
1100
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1905
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
22U5
2300
0
0
0
0
LOAD
MWTH
*******
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
02
VOLX
MEAS
t*******
7.3
7.3
7.6
7.7
7.5
7.7
7.4
7.3
7.2
7.4
7.4
7.3
7.0
9.3
7.6
9.5
9.0
9,7
10.9
10.7
9.0
9.2
11.4
9.1
10.5
9.4
8.6
7.1
7.1
7.0
6.9
6.5
6.6
6.4
6.5
6.9
6.5
6.9
6.5
7.0
6.7
6.7
6.7
6.7
.0
.0
.0
.0
C02
VOLX
MEAS
*******
7.4
7,4
7,3
7.1
7,3
7.1
7.3
7.4
7.5
7.2
7,4
7.4
7.6
5.6
7,1
5.5
5.8
5,2
4.1
«.l
6.0
5.7
3.4
5.9
4.5
5.4
6.2
7.5
7.*
7,7
7.8
8.0
8.0
8.1
8.0
7.8
8.0
7.9
8.1
7.9
8.0
8.0
8.0
7.9
.0
.0
.0
.0
CO
PPMy
MEAS
*******<
26
36
40
25
33
32
28
25
23
23
30
24
23
33
22
3
26
12
6
20
9
32
20
11
26
20
21
23
34
3
54
15
8-
32
22
1
10
10
12
20
30
11
10
16
0
0
0
0
NO
PPMV
MEAS
»******<
41
41
42
42
42
42
42
41
42
41
41
42
42
35
41
35
34
32
28
28
35
34
27
34
29
32
36
39
40
39
m
m
«
.
V
.
.
0
0
0
0
CO
PPMV
3X02
t ****** i
3«
50
53
33
44
43
37
32
30
30
39
31
29
50
29
4
39
19
10
35
13
48
37
16
an
31
30
29
44
3
69
18
10
39
27
1
12
12
14
25
37
13
12
20
0
0
0
0
NO
PPMV
3X02
t********
53
53
56
56
56
56
55
53
54
54
54
55
54
54
55
54
51
51
50
49
52
52
50
51
-------
******************************
**
15 HIM. DATA
DRY STACK GAS CONCENTRATION
**************
**
**
**
**
**
** DATE
'TIME
LOAD
MWTH
0?
VOLX
MEAS
*******************************
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** O/ OX 0
** O/ O/ 0
** OX O/ 0
** OX O/ 0
** OX O/ 0
** O/ OX 0
*» O/ O/ 0
** OX O/ 0
** OX O/ 0
** OX O/ 0
*« O/ OX 0
»* OX OX 0
** OX OX 0
»* OX OX 0
** OX OX 0
«* OX OX 0
** ox ox o
* OX OX 0
*» OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** ox ox o
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** 8X19X80
** 8X19X80
** 8X19X80
** 8X19/80
** 8X19/80
** 8X19X80
** 8X19/80
*» 8/19/80
** 8/19X80
** 8X19X80
** 8/19/80
** 8/19/80
** 8/19/80
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
6.4
6.5
6.5
6.6
6.«
6.5
6.3
6.6
6.4
6.5
6.3
6.5
».3
C02
vou
MEAS
*********
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
8.1
8,0
e.o
8.0
8.1
e.i
8.2
8.1
8.3
8.1
8.1
6.0
6.6
CO
PPMV
MEAS
NO
PPMV
MEAS
CO
PPMV
3X02
NO
PPMV
3X02
CO
NG/J
* »
NO ACODE **
NG/J **
**
**************************************************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
53
41
46
51
37
13
52
46
67
54
35
31
54
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
45
45
45
46
45
46
45
46
47
47
46
47
42
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
65
50
57
63
45
53
63
57
82
67
42
38
76
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
55
55
55
57
55
57
55
57
58
58
56
58
59
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
21
16
18
21
15
17
21
19
27
22
1«
12
25
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
o
o
o
o
o
o
o
o
0
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
30 **
30 **
30 **
31 **
30 **
31 **
29 **
31 **
31 **
31 **
30 **
31 **
32 **
******************************************************************************************
123
KVB11-6017-1266
-------
»AftAA*AAAAA**AAA**A*A*A**AAA*AAAAA*AAA**AAA***A*
**
**
**
**
**
»* DATE
*********A*5l
** 6/19/ao
*« 8/19/80
«* a/19/80
** 8/19/80
** 6/19/80
** 8/19/80
** 8/19/80
** 6/19/80
** 8/19/80
** 8/19/80
** 8/19/80
** 6/19/80
** 8/19/80
* 8/19/80
*« 6/19/80
** 8/19/80
»* 6/19/80
»* 6/19/80
** 8/19/80
»* 8/19/80
** 8/19/80
** 6/19/80
»* 8/19/80
** 8/19/80
*» 8/19/80
** 6/19/80
** 6/19/80
** 6/19/80
«* 8/19/80
** 8/19/80
*« 8/19/80
*» 8/19/80
** 8/19/80
* 8/19/80
** 8/19/80
** 8/19/80
** 8/19/80
»* 8/19/80
** 8/19/80
** 8/19/80
»* 8/19/80
** 8/19/80
** 8/19/80
** 8/19/80
*A O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
»**A*A*AAAAi
15 WIN. DATA
DRY STACK GAS CONCENTRATION
TIME
tit Hit Hit It
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
0
*******
LOAD
MWTH
A* * * * It 1
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
***** *!
02
VOL*
HEAS
t******4
6.7
6.4
-1.0
-1.0
-1.0
-1.0
6.2
6.8
8.7
8.3
6.3
7.9
6.7
7.9
9.7
8.6
6.6
7.«»
6.7
6.8
6.8
8.6
11.2
9.2
10.6
10.9
10.6
10.9
10.3
".1
9.2
'.3
10.2
8.5
8.7
6.8
9.8
8.7
7.2
8.7
8.4
6.5
7.1
8.4
.0
.0
.0
.0
>******!
C02
VQLX
MEAS
t&AAftltAi
6.0
8.0
-1,0
-1.0
-1.0
-1.0
8.2
7,8
6.2
6.4
6.1
6.9
7.8
6.8
5.3
6.1
7.9
6.8
7.8
7.8
7.8
6.2
3.6
5.7
«.3
3.6
4.7
3.6
5.1
5.8
5.7
5.4
4.8
6.3
6.1
6.0
5.1
6.1
7.5
6.2
6.5
6.4
7.6
6.5
.0
.0
.0
.0
»******:
CO
PPHV
MEAS
29
26
-1
-1
-1
-1
19
21
33
8
21
32
19
31
43
38
21
32
19
19
17
30
18
55
30
24
30
25
34
4
It
40
25
36
6
34
22
26
18
9
32
28
19
29
0
0
0
0
I******;
NO
PPMV
MEAS
t&A&'ft&ftJ
46
45
-1
-1
-1
-1
45
44
38
34
43
40
42
38
33
36
43
38
42
42
42
35
26
34
30
26
31
26
33
35
35
32
32
36
36
35
32
36
42
36
38
38
42
37
0
0
0
0
»*****Al
CO
PPMV
3X02
k******^
36
32
0
0
0
0
23
26
48
11
25
44
23
42
68
55
26
44
23
24
21
43
33
84
52
42
52
44
57
6
16
61
41
51
8
50
35
38
23
13
45
40
2«
41
0
0
0
0
»******<
NO
PPMV
3X02
t ***** *
57
55
0
0
0
0
54
55
55
48
52
55
52
52
52
52
53
52
52
53
53
50
47
52
52
46
53
46
55
53
53
49
53
51
52
51
51
52
54
52
54
54
54
52
0
0
0
0
>4* AAAA
CO
NG/J
***$***!
12
10
0
0
0
0
7
8
15
3
6
14
7
14
22
18
8
It
7
7
7
14
10
27
17
14
17
14
18
2
5
20
13
17
2
16
11
12
7
4
15
13
8
13
0
0
0
0
******* 3
NO ACODE
NG/J
fr*A***A*ft***&
31
30
0 C
0 C
0 C
0 C
29
30
30
26
28
29
28
28
28
28
29
28
28
28
28
27
26
28
28
25
29
25
30
28
29
26
29
28
28
28
27
28
29
28
29
29
29
28
0 *
0
o
0
>************
**
**
**
**
**
**
A * * A
**
**
**
A*
**
**
**
**
»*
**
**
**
**
**
**
**
**
**
**
**
* *
**
**
**
Aft
**
**
*A
**
**
**
* *
**
**
**
**
**
A*
**
A A
**
A*
A A
A *
* *
A*
A A
AA
AA A A
124
KVBll-6017-1266
-------
A***********************)
**
**
**
**
**
**
DATE
TIME
LOAD
MWTH
k***************************** ************<
15 MIN. DATA
DRY STACK GAS CONCENTRATION
02
VOLX
MEAS
C02
VULX
MEAS
CO
PPMV
MEAS
NO
PPMV
MEAS
****************************************************
**
**
**
**
**
**
**
**
**
**
**
**
*»
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
»*
**
**
**
*»
**
**
OX OX 0
OX OX 0
OX O/ 0
OX OX 0
OX OX 0
OX OX 0
OX OX 0
OX OX 0
OX O/ 0
O/ OX 0
OX OX 0
OX OX 0
OX OX 0
OX OX 0
OX OX 0
OX OX 0
OX OX 0
OX OX 0
OX OX 0
OX OX 0
8X20X80
8X20X80
8X20X80
8X20X80
8X20X80
8X20X80
8X20X60
8X20X80
8X20X80
8X20X80
8X20X80
8X20X80
8X20X80
6X20X80
8/20X80
8X20X80
8X20X80
8/20X80
8X20X80
8X20X80
8X20X60
8X20X80
8X20X80
8X20/80
8/20X80
8X20X80
8X20/80
8X20X80
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
515
600
615
630
645
700
715
730
705
800
815
830
845
900
915
930
945
1000
1015
1030
1005
1 100
1115
1130
1 145
1200
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
,0
.0
.0
.0
.°
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
6.0
6.2
5.3
4.4
a. 6
4.6
5.6
«.3
5.4
5.3
5.2
5.0
5.9'
5.9
5.8
6.1
5.9
6.5
"1.0
6.6
6.6
6.9
6.9
6.3
8.4
7.1
6.9
6.9
.0
.0
.0
o
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
8.7
8.1
9.0
9.4
9.4
9.0
8.B
">.5
',1
9.0
9.1
9.2
8.7
8.7
8.8
8.5
8.7
8.2
-1.0
8.1
8.1
7.8
7.9
8.2
6.6
7.6
7.8
7.7
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
6
28
52
32
9
52
138
6
12
28
34
31
6
6
22
30
39
50
-1
69
59
35
38
53
30
28
18
19
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
46
45
47
47
47
48
45
48
47
47
47
47
46
46
46
44
46
44
-1
43
42
41
42
42
37
41
42
42
CO
PPMV
3XU2
*********
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
7
34
59
34
9
57
161
6
13
32
38
34
7
7
26
36
46
62
0
86
73
44
48
64
42
36
23
24
NO
PPMV
3X02
*******
CO
NGXJ
************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
55
54
53
50
51
52
52
51
54
53
53
52
54
54
54
53
54
54
0
53
52
52
53
51
52
53
53
53
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
2
11
19
11
3
te
53
2
4
10
12
11
2
2
8
11
15
20
0
28
24
H
16
21
14
11
7
8
**********
NO ACO
NGXJ
*********
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
29
29
29
27
27
28
26
28
29
29
29
28
29
29
29
28
29
29
0 C
29
28
28
29
27
28
28
29
29
**
**
**
**
**
**
*******
**
**
**
**
**
**
**
* *
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
* *
**
**
**
* *
**
**
**
**
**
**
* *
**
* *
* *
**
**
* *
**
* *
* *
**
******************************************************************************************
125
KVB11-6017-1266
-------
****************************************
**
** DRY STACK
**
**
**
** DATE
TIME
LOAD
MWTH
02
VOL2
MEAS
C02
VOU
MEAS
A**************************
15 MIN. DATA
GAS CONCENTRATION
CO
PPMV
MEAS
NO
PPMV
MEAS
CO
PPMV
3102 .
NO
PPMV
3X02
t* **********************
**
**
CO
NG/J
A*************************************************************************
** 6/20/80
** 8/20/30
** 6/20/80
** 8/20/80
»* 8/20/80
** 8/20/80
** 8/20/80
** 6/20/60
** 8/20/80
** 8/20/80
** 8/20/80
** 8/20/80
** 8/20/80
«* 8/20/80
** 6/20/80
** 6/20/80
*« 8/20/80
** 8/20/80
** 6/20/80
** 6/20/80
** 8/20/80
** 8/20/80
** 6/20/80
** 8/20/80
** 8/20/80
** 8/20/80
** 8/20/80
** 8/20/60
** 8/20/80
** 8/20/80
** 8/20/80
** 6/20/80
** 8/20/80
** 6/20/80
** 8/20/80
*» 8/20/80
** 6/20/80
** 8/20/80
** 6/20/80
** 8/20/80
** 6/20/8Q
** 8/20/80
** 6/20/80
** 8/20/80
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
***********
1215
1230
1205
1300
1315
1330
1345
1400
1415
1430
1045
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
i9is
1930
1945
2000
2015
2030
2045
2100
2115
2130
21«5
2200
2215
2230
2245
2300
0
0
0
0
******
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
*******
7.0
6.9
7.1
8.8
8,4
6.0
8.7
8.9
10.1
10.0
7.0
9.6
8.4
9.5
6.8
8.1
7.0
6.8
10.6
6.8
7.4
9.4
7.1
11.3
9.2
10.6
9.8
10.7
9.5
10.2
8.9
8.6
10.2
9.8
8.2
6.9
7.7
7.8
7.3
7.4
7.4
7.3
7.3
7.7
.0
.0
.0
.0
7.7
7.8
7.6
6.1
6.5
6.7
6,4
6.7
5.2
5.3
7.7
5.6
6,5
5.7
7.9
6,9
7.8
7.9
4.7
7.8
7,5
5,7
7.6
3.8
6.2
4.4
5.7
«.2
5.9
5.5
6.3
*,5
5.1
5.5
6.8
*,2
7.3
7.2
7.6
7.5
7.5
7.5
7.6
7.4
.0
.0
.0
.0
****************
18
24
18
37
12
19
26
24
30
32
12
42
38
50
11
24
9
12
22
14
21
27
12
5
28
23
30
It
27
33
22
22
43
36
25
19
15
12
11
13
13
14
16
11
0
0
0
0
42
41
39
34
36
39
39
39
34
34
42
35
38
36
44
40
44
44
32
44
43
35
42
28
37
30
34
27
33
32
36
36
32
32
37
36
40
40
40
40
40
40
40
40
0
0
0
0
23
30
23
54
17
26
38
35
49
52
15
66
54
78
13
33
11
15
38
17
27
42
15
<»
42
39
48
19
42
55
32
32
71
58
35
28
20
16
14
17
17
18
21
14
0
0
0
0
54
52
50
50
51
54
57
58
56
55
54
55
54
56
55
55
56
55
56
55
57
54
54
52
56
52
54
47
51
53
53
52
53
51
52
53
54
54
52
53
53
52
52
51
0
0
0
0
A*************************,
7
10
7
18
5
8
12
11
16
17
5
21
17
25
4
11
3
5
12
5
9
13
5
3
14
13
15
6
13
18
10
10
23
19
11
9
6
5
4
5
5
6
6
a
0
0
0
0
NO ACUDE
NG/J
**
**
**
**
t****************
29
28
27
27
27
29
31
31
30
30
29
30
29
30
30
30
30
30
30
30
30
29
29
28
30
28
29
25
28
29
29
28
29
27
28
29
29
29
28
28
28
28
28
29
0
0
0 »
0 »
********************
**
**
**
**
**
**
**
* *
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
* *
* *
* *
**
* »
* *
**
**
****
126
KVB11-6017-1266
-------
*********
15 HIM. DATA
DRY STACK GAS CONCENTRATION
****************************
**
**
**
** DATE
TIME
LOAD
MWTH
**************************
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** o/o/o
** o/ O/ 0
** o/ O/ 0
** O/ O/ 0
** o/ O/ 0
*« O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** o/ O/ 0
** 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
»* 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
*» 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
** 6/21/80
** 8/21/80
** 8/21/80
** 8/21/80
* 8/21/80
** 8/21/80
** 8/21/80
*************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
545
600
615
630
645
700
715
730
745
800
815
830
845
900
915
930
945
1000
1015
1030
1045
1 100
1115
1130
1145
1200
******
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
*******
02
votx
MEAS
****
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
6.7
7.2
6.4
4,7
5.2
5.3
4.9
5.0
5.3
5.7
5.9
6.2
6.3
6.8
6.8
7.3
7,1
7.1
7.0
7.0
6.6
6.9
7.1
8.5
7.9
7.6
6.5
8,0
****
C02
VOLX
MEAS
»*******<
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
8.1
7.8
8,3
9,2
»!o
9.2
9.1
9.0
8.8
8.6
8.6
8,5
8.2
8.1
7.8
8.0
7.9
7.9
7.9
8.1
8.0
7.8
6.6
6.8
7.5
8.1
6,9
CO
PPMV
MEAS
*********
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
24
9
3
0
7
15
0
1
0
12
12
12
12
16
57
45
28
30
36
15
24
15
14
0
18
13
16
36
*****************
NO
PPMV
MEAS
******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
43
43
44
45
45
46
47
47
46
46
45
45
45
44
43
42
44
43
44
44
44
44
43
38
40
43
44
39
******
CO
PPMV
3X02
******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
30
11
3
0
7
17
0
1
0
14
14
14
1
-------
***********<
**
ft*
**
**
**
»* DATE
15 MIN, OAT*
DRY STACK GAS CONCENTRATION
-TIME
ft*****************
*» e/21/80
** 6/21/80
*ft 6/21/80
«ft 6/21/60
** 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
** 8/21/80
» 8/21/80
** 6/21/80
** 8/21/80
** 8/21/80
«* 6/21/80
** 6/21/80
** 6/21/80
** 8/21/80
* 8/21/80
** 8/21/80
*« 8/21/80
** 8/21/80
*» 8/21/80
** 8/21/80
** 6/21/60
** 8/21/80
** 8/21/80
** 8/21/80
»* 6/21/80
** 8/21/80
ft* 8/21/80
** 8/21/80
** 8/21/80
8/21/80
** 8/21/80
8/21/80
** 8/21/80
* 8/21/80
8/21/80
** 8/21/80
** 6/21/80
** 8/21/80
** 8/21/80
** 8/21/80
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
ft* O/ O/ 0
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1905
2000
2015
2030
20«5
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
0
LOAD
MWTM
*******
0
.0
o
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
02
VOLX
MEAS
>******<
6.5
6.2
6.6
8.6
9.9
-1.0
8.2
9.0
10.0
8.8
8.3
6,4
6.3
8.0
6.2
8.3
7.6
8.8
8.6
9.6
8.5
10.0
9.7
7.1
6.5
8.2
8.3
7.0
7.4
9.3
11.4
10.9
6.8
8.6
8.7
9.0
8.6
8.7
7.2
8.8
7.1
8.9
7.«
9.0
.0
.0
.0
.0
C02
VOLX
MEAS
»******<
8.1
6.9
8,0
6,5
5.2
1,0
6.7
6.2
5,6
6.1
6.7
8.1
8.2
6.9
8.3
6,7
7.1
6.1
6,4
5.7
6.6
5.0
5,8
7.8
8.2
6.7
7.1
8.0
7.9
6,5
4.6
4.6
6.6
6,6
6,5
6.2
6.6
6.5
7.8
6.6
7.9
6.6
7.8
6.5
.0
.0
.0
.0
CO
PPMV
MEAS
(****»*)
15
32
16
35
11
"1
36
0
37
6
28
16
9
32
10
20
22
8
24
24
27
38
0
12
6
18
14
15
11
18
11
16
13
16
26
4
1
8
8
28
13
35
9
25
0
0
0
0
NO
PPMV
MEAS
i******)
44
40
43
38
33
-1
38
41
38
40
42
46
47
43
47
40
40
38
39
36
39
32
37
44
44
39
40
43
42
36
31
30
36
36
36
35
37
38
42
38
42
38
43
39
0
0
0
0
CO
PPMV
3X02
t***»**i
18
45
20
50
17
0
50
0
60
a
39
19
11
44
12
28
30
11
34
38
38
62
0
15
9
25
19
19
14
27
20
28
19
23
38
6
1
11
10
41
16
52
11
37
0
0
0
0
NO
PPMV
3X02
k******i
54
56
53
55
53
0
53
61
62
59
59
56
57
59
57
56
54
56
56
57
56
52
59
57
54
54
56
55
55
56
58
53
53
52
52
52
53
55
54
56
54
56
57
58
0
0
0
0
CO
NG/J
>******<
6
14
6
16
5
0
16
0
20
2
13
6
3
14
4
9
9
3
11
12
12
20
0
5
3
8
6
6
H
9
6
9
6
7
12
1
0
3
3
13
5
17
3
12
0
0
0
0
*****************
**
**
NO
NG/J
!*****(
29
30
29
29
29
0
29
33
33
32
32
30
31
32
31
30
29
30
30
30
30
28
32
30
29
29
30
30
30
31
31
29
28
28
28
28
29
30
29
30
29
30
30
31
0
0
0
0
**
ACODE **
**
**
********** *
**
**
**
**
**
C **
**
* *
**
**
**
**
**
**
**
**
**
**
**
* *
**
**
**
**
**
**
**
**
ft*
**
* *
**
**
**
**
**
* *
**
* *
**
**
* *
**
**
0 **
**
* **
**
128
KVBll-6017-1266
-------
******************************************************************************************
**
**
**
**
**
** DATE
15 HIM. DAT*
DRY STACK GAS CONCENTRATION
TIME
*******************
** O/ OX 0
** OX OX 0
** OX OX 0
** O/ OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** 8/22X80
*» 8X22X80
*» 8X22X80
*« 8/22X80
** 8/22X8Q
** 8/22/80
*« 8/22/80
*» 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
*» 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 6/22/80
** 8/22/80
* 8/22/80
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
545
600
615
630
645
700
715
730
745
800
815
830
815
900
915
930
9«5
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MWTH
02
votx
MEAS
C02
votx
MEAS
CO
PPMV
MEAS
NO
PPMV
MEAS
CO
PPMV
3X02
NO
PPMV
3X02
CO
NG/J
*******************************************************
.0
.0
.0
.0
.0
.0
tO
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
9.7
6.8
6.)
5.2
6.2
5.7
5.0
5.4
5.6
6.3
5. a
5.1
5.6
5.6
5.3
5.1
5.5
5.6
6.1
6.2
6.3
6.2
6.2
6.2
6.4
6.5
6.6
6.5
.0
.0
.0
,0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
5.6
8.0
8.5
9.0
8.0
8.7
9.2
9.0
8.9
8.0
9.0
9.0
8.7
6.6
8.8
8.7
8.7
8.6
6.2
8.3
8.2
8.2
8.2
8.2
8.0
8.0
7.8
8.0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
6
39
26
31
3
15
10
9
14
18
10
09
15
26
20
10
38
16
57
53
09
44
56
39
36
23
20
24
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
38
46
49
51
49
49
49
50
50
49
51
45
45
oa
40
40
40
44
02
43
03
43
43
40
43
42
42
42
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
9
49
31
35
3
17
11
10
16
22
11
55
17
30
22
11
44
18
68
64
60
53
6fi
47
00
28
30
29
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
60
58
59
58
59
57
55
57
58
60
58
50
52
51
50
50
51
51
50
52
52
52
52
53
53
52
52
52
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
3
16
10
H
1
5
3
3
5
7
3
18
5
10
7
3
14
6
22
21
19
17
22
15
10
9
9
9
**
**
**
NO ACODE **
NG/J **
**
****************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
32 **
31 **
32 **
31 **
32 **
31 **
29 **
31 **
31 **
32 *«
31 **
27 **
28 **
27 **
27 **
27 **
27 **
27 **
27 **
28 **
28 **
2b **
28 **
29 «*
28 **
28 **
26 **
28 **
A************************************it***************************************
129
KVB11-6017-1266
-------
** 15 MIN. DATA
** DRY STACK 6A3 CONCENTRATION
/*
**
**
** DATE
************
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/60
** 8/22/80
** 8/22/80
** 8/22/80
«* 8/22/80
** 8/22/80
** 8/22/80
*» 8/22/80
** 8/22/80 ,
** 8/22/60
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/60
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
*» 6/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
«* 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
«» 8/22/80
** 6/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** 8/22/80
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** Q/ O/ 0
TIME
******
1215
1230
1205
1300
1315
1330
1305
1400
1415
1«30
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1
-------
*************************************************************************
** 15 KIN. DATA
** DRY STACK GAS CONCENTRATION
**
** 02 C02 CO NO CU NO CO
**
** DATE
TIME
LOAD
MWTH
**************************
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** O/ O/ 0
** OX O/ 0
** OX O/ 0
** OX O/ 0
** OX OX 0
»* OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
* OX OX 0
*« OX OX 0
«* OX OX 0
** OX OX 0
** 8X25X80
** 8/35X80
** 8X25X80
*» 8X25/80
** 8X25/80
** 8X25X80
** 8/25/80
** 8/25X80
** 8X25X80
* 8X25/80
*« 8/25/80
*» 6/25/60
** 8/25/80
«* 8/25/80
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
885
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
*****************
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
********
VOL%
MEAS
VOLX
MEAS
I************
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
6.5
7.8
6.3
6.4
6.4
6.6
6.3
t>.«
6.3
6.3
6.2
7.9
7.6
7.9
*****
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
8.1
7.0
8.2
6.1
8.1
8.1
8.3
«.t
8.2
8.2
8.2
7.0
7.2
<>.<>
PPMV
MEAS
PPMV
MEAS
***************
0
b
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
20
02
18
20
17
20
17
20
20
20
17
24
28
25
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
«a
39
C4
43
44
45
45
46
as
44
as
39
ao
39
**********************
PPMV
3X03
*******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
24
57
22
2«
20
25
20
24
24
24
20
33
37
34
*******
PPMV
3X02
******<
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
54
53
53
53
54
56
55
56
55
53
54
53
53
53
*******
NG/J
******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
8
18
7
8
6
8
6
8
8
8
6
10
12
11
******
*****************
**
**
**
NO ACODE **
NG/J **
**
*****************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
o
0
0
o
o
0
0
o
o
o
o
Q
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
* *
**
**
29 **
28 **
29 **
28 **
29 **
30 **
29 **
30 **
29 **
29 **
29 **
29 **
29 **
29 **
131
KVB11-6017-1266
-------
A****************************************************************************************
**
**
»*
**
**
** DATE
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
KIAO
MWTH
0?
VOLX
MEAS
C02
VOLX
MEAS
CO
PPMV
MEAS
NO
PPMV
MEAS
CO
PPMV
3X02
NO
PPMV
3X02
CO
NG/J
NO
NG/J
A*******************************************************************************
** 8/25/80
** 8/25/80
** 8/25/80
** 8/25/80
*» 8/25/80
** 8/25/80
** 8/25/80
** 8/25/80
** 8/25/80
** 8/25/80
** 8/25/80
»* 8/25/80
** 8/25/80
** 8/25/80
** 8/25/80
** 8/25/80
«* 8/25/80
** 8/25/80
** 6/25/80
*« 8/25/80
*» 8/25/80
** 8/25/80
** 8/25/80
** 8/25/60
** 6/25/80
** 8/25/80
** 8/25/80
** 8/25/80
** 8/25/80
** 6/25/80
** 8/25/80
** 8/25/80
«* 8/25/80
** 6/25/80
** 8/25/80
»« 6/25/80
*« 8/25/80
** 8/25/80
** 8/25/80
** 6/25/80
»* 8/25/80
** 8/25/80
** 6/25/80
** 8/25/80
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
***********
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
8.4
8.2
7.4
7.6
6.1
7.4
6.3
6.5
7.9
7.5
7.8
8.0
7.1
9.2
6.3
8.6
7.0
7.7
9.2
6.2
9.0
9.6
7.5
9.9
9.0
7.9
8.9
9.2
7.8
7.9
7.8
7.7
7.1
7.4
7.1
7.4
6.5
6.7
6.5
6.6
6.5
7.5
6.6
6.6
.0
.0
.0
6.4
6.6
7.3
7.2
6.2
7.2
6.1
8.0
6.9
7.3
6.9
6.8
8.2
6.0
7.9
6.2
7.5
6.8
6.1
6.1
5.8
5.3
7.1
4.9
5.9
6.7
6.0
5.6
6.7
6.7
6.6
6,8
7.3
7,2
7.2
7.6
7.9
7.8
8.0
7.9
8.0
6.9
8.1
7.9
.0
.0
.0
0 .0 .0 .0
*************£***********&*«
30
22
36
31
18
36
20
19
32
39
34
38
22
60
36
44
12
27
39
16
37
59
44
45
54
12
42
33
36
42
29
24
34
22
19
2 a
17
16
16
16
16
22
32
18
0
0
0
0
38
39
40
40
45
41
«5
45
40
41
39
39
40
37
40
36
40
36
36
44
34
32
36
30
33
36
34
33
36
37
38
37
38
38
38
41
41
41
42
41
41
37
42
42
0
0
0
0
* * * *r * ** * 4
42
31
47
41
21
47
24
23
44
52
46
52
28
91
44
64
15
36
59
19
55
95
58
73
81
16
62
50
49
57
39
32
44
29
24
31
21
20
19
20
19
29
40
22
0
0
0
0
E ******
54
54
53
53
54
54
55
55
55
54
53
54
51
56
49
52
51
51
55
53
51
51
48
48
49
49
50
SO
49
50
51
50
49
50
49
54
50
51
52
51
50
49
52
52
0
0
0
0
14
10
15
13
7
15
8
7
14
17
15
17
9
30
14
21
5
12
19
6
18
31
19
24
26
5
20
16
16
19
13
10
14
9
8
10
6
6
6
6
6
9
13
7
0
0
0
0
******
29
29
28
29
29
29
29
30
29
29
28
29
28
30
26
28
27
27
29
29
27
27
26
26
26
26
27
27
26
27
28
27
26
27
26
29
27
28
28
27
27
26
28
28
0
0
0
0
******
**
**
**
ACOOE **
**
**
***********
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
* *
**
**
**
**
* *
**
* *
**
**
**
**
**
**
**
* *
**
**
**
**
**
**
**
* **
* **
***********
132
KVB11-6017-1266
-------
***********************************************************<
*»
**
**
**
**
** DATE
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
LOAD
MKTH
02
VOLX
MEAS
a******************************,
** OX OX 0
** OX OX 0
** OX OX 0
** OX O/ 0
** OX O/ 0
** OX OX 0
** O/ OX 0
** O/ O/ 0
** O/ OX 0
** OX O/ 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
«* CX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** 8X26X80
** 8X26X80
** 8X26X80
*» 8X26X80
** 8X26X80
*« 8X26X80
** 8X26/80
** 8X26X80
** 8X26X80
** 8/26X60
** 8/26X80
** 8x26/80
** 8X26X80
** 8/26/80
«* 8/26/80
** 8/26X80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8X26X80
** 8X26X80
** 8X26X80
** 8X26X80
** 8X26X80
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
515
600
615
630
645
700
715
730
705
800
815
830
805
900
915
930
945
1000
1015
1030
1005
1100
1115
1130
lias
1200
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
8.5
6.8
5.2
a. 9
4.8
«.7
«.3
4.4
fl.8
5.0
fl.8
5.2
5.8
5.9
5.7
6.6
5.9
6.1
5.8
5.8
5.9
5.8
5.7
5.6
5.9
6.0
6.0
7.S
C02
VOL*
MEAS
CO
PPMV
MEAS
NO
PPMV
MEAS
CO
PPMV
3X02
NO
PPMV
3X02
CO
NG/J
**
**
**
NO ACODE **
NGXJ **
**
***********************************************************
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
6.5
8.0
9.1
9.2
9.3
9.2
9.5
9.«
9.2
9.1
9.2
9.0
8.6
8,6
8,6
7.9
6.5
8.4
8.6
8.5
8.5
8.5
8.6
8.6
8.5
e.4
8,3
6.8
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
47
23
16
46
32
31
35
38
23
20
61
22
7
32
2
22
36
17
7
13
10
10
59
56
32
50
3a
30
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
41
47
52
51
52
51
51
52
51
50
50
50
48
48
48
44
46
46
47
46
46
lib
U6
45
46
45
45
40
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
67
29
18
51
35
34
37
41
25
22
67
25
8
38
2
27
42
20
8
15
11
11
69
65
38
60
40
40
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
59
59
59
57
57
56
54
56
56
56
55
57
56
57
56
55
54
55
55
54
54
54
54
52
54
54
54
54
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
22
9
6
16
11
11
12
13
8
7
22
8
2
12
0
9
1«
6
2
5
3
3
22
21
12
19
13
13
0
0
0
0
0
0
0
0
0
0
0
0
0
0
o
0
0
0
0
0
**
* *
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
32 **
32 **
32 **
30 *»
31 **
30 **
29 **
30 **
30 **
30 **
30 **
30 **
30 **
31 «*
30 **
29 **
29 **
30 **
30 **
29 **
29 **
29 **
29 **
28 **
29 **
29 **
29 **
29 **
**************************** ***********
************************************
133
KVB11-6017-1266
-------
*********************************************************** ************************** **** «
**
**
**
**
**
** DATE
15 MIN, DATA
DRY STACK GAS CONCENTRATION
TIME
LOAD
MWTH
02
VOLX
MEAS
C02
VOLX
MEAS
CO
PPMV
MEAS
NO
PPMV
MEAS
**************************ft*************************J
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/60
«* 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
«* 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 6/26/80
*» 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
*« 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
*» 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** 8/26/80
** O/ O/ 0
*» O/ O/ 0
** O/ O/ 0
** O/ O/ 0
************
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
***********
6.2
6.2
6.0
6.5
5.0
5.0
5.0
4.6
5.0
5,0
5.0
S.I
5.5
5.7
5.9
9.7
8.2
9.9
8.5
9.5
7.2
9.6
8.1
9.8
8.1
9.5
7.9
7.9
6.6
6.6
6.9
7.1
7.2
7.4
7.3
7.2
7.1
6.9
7.2
7.0
6.9
7.0
6.6
8.3
.0
.0
.0
.0
*******
8.2
8.2
8.2
8.0
9.0
8.9
8,0
9.3
9.0
8.9
9.0
8.9
8.7
8.5
8.4
4.8
6.7
4.8
5.9
4.9
7.6
5.2
6.4
5.0
6.6
5.3
6.8
6.8
8.0
8.0
8.0
8.0
8.0
7.9
7.9
8.0
7,9
8.1
8.0
8.1
8.2
8.0
8.1
6.9
.0
.0
.0
.0
*******
36
22
21
40
37
12
14
30
37
12
14
32
19
24
19
16
52
3
25
23
24
12
25
2
14
11
15
37
17
16
13
16
16
IS
16
16
17
20
20
"19
17
16
17
36
0
0
0
0
46
46
45
47
51
52
52
52
51
52
52
50
49
48
45
32
38
31
34
30
41
30
35
29
32
27
31
32
36
37
38
38
39
39
40
40
41
4i
41
41
42
41
41
38
0
0
0
0
CO
PPMV
3X02
t # * ft * * * d
43
26
25
49
41
13
15
32
41
13
15
36
22
28
22
25
73
4
36
36
31
19
34
3
19
17
20
50
21
20
16
20
20
19
21
20
22
25
26
24
21
20
21
51
0
0
0
0
NO
PPMV
3X02
>******«
56
56
54
58
57
58
58
57
57
58
58
56
56
56
53
51
53
50
49
47
53
47
48
46
44
42
42
44
45
46
48
49
50
51
52
52
53
52
53
52
53
52
52
55
0
0
0
0
CO
NG/J
!******<
14
8
8
16
13
4
5
10
13
4
5
11
7
9
7
8
24
1
11
11
10
6
1!
1
6
5
6
16
7
6
5
6
6
6
6
6
7
8
8
8
7
6
7
16
0
0
0
0
NO
NG/J
>*****<
30
30
29
31
31
31
31
30
31
31
31
30
30
30
29
27
29
27
26
25
29
25
26
25
24
22
23
23
24
25
26
26
27
28
28
28
28
28
29
28
29
2B
28
29
0
0
0
0
***************************************** *!
**
**
**
ACODE **
**
**
i**********
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
»*
**
**
* *
**
**
**
**
**
* *
**
**
**
* *
**
* *
» **
» **
» **
» **
***********
134
KVB11-6017-1266
-------
***************************
**
**
**
** 02
** LOAD VOtX
«* DATE TIHE MfcTH MEAS
******************************
** O/ OX 0 0 .0 .0
** OX OX 0 0 ,0 .0
** ox ox o o .0 ,0
** OX OX 0 0 ,0 .0
** OX OX 0 0 .0 .0
** OX OX 0 0 ,0 .0
** OX OX 0 0 .0 .0
** OX OX 0 0 .0 .0
** OX OX 0 0 .0 .0
** OX OX 0 0 ,0 ,0
** OX OX 0 0 ,0 .0
** OX OX 0 0 .0 .0
** OX OX 0 0 .0 ,0
** OX OX 0 0 ,0 ,0
** OX OX 0 0 ,0 ,0
** OX OX 0 0 .0 .0
** OX OX 0 0 ,0 ,0
** OX OX 0 0 ,0 .0
** ox ox o o .0 .0
** OX OX 0 0 .0 .0
** 8X27X80 515 .0 8.2
** 8X27X80 530 .0 7,3
** 8X27X50 545 ,0 5.6
** 8X27X80 600 ,0 5.7
** 8X27X80 615 ,0
** 8X27X80 630 .0 5.6
** 8X27x80 645 ,0 5.3
*» 8X27X80 700 .0 5.2
** 8X27X60 715 ,0 5,6
** 8X27X80 730 ,0 5.4
** 8X27X80 745 .0 5.7
** 8X27X80 800 .0 6.6
** 8X27X80 815 .0 6.7
*» 8X27X80 830 ,0
** 8X27X80 845 .0 6.4
** 8X27X80 900 ,0 6.2
** 8X27X80 915 .0 6,5
** 8X27X80 930 ,0
** 8X27X60 945 ,0 6.5
** 8X27X80 1000 .0 6.5
** 6X27X80 1015 .0 6,4
*» 8X27X80 1030 .0 7.1
** 8X27X80 1045 ,0 6.5
** 8X27X80 1100 ,0 6.7
** 8X27X80 1115 ,0 6.3
** 8X27X80 1130 .0 8.2
** 8X27X80 1145 .0 6.5
** 8X27X80 1200 .0 8.2
******************************
15 M1N. DATA
STACK GAS CONCENTRATION
C02 CO NO CO
VOLX PPMV PPMV PPMV
MEAS MEAS MEAS 3X02
***************************
********************************
**
**
**
NO CO NO ACODE **
PPMV NGXJ NGXJ **
3X02 **
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
7,5
7.9
'.1
9.0
8.8
9.0
9.2
9,3
9.0
9.0
".o
8.4
8.4
8.1
8.4
8.3
8.1
8.0
6.1
8.0
8.1
7.6
8.1
7.8
8.2
6.5
8.0
6.3
**********
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
8
1
169
30
12
4
54
53
35
7
31
7
14
19
50
40
39
34
34
35
36
40
39
37
45
65
35
77
******<
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
44
44
48
48
47
48
48
49
48
48
48
47
46
45
46
46
45
44
44
45
45
45
46
46
47
41
46
40
*******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
11
1
197
35
14
4
61
60
40
8
36
8
17
24
61
48
48
42
42
43
44
51
48
46
55
91
43
108
*******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
62
57
56
56
56
56
55
55
56
55
56
58
57
57
56
56
55
54
54
55
55
58
57
57
57
57
57
56
t ******!
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
3
0
65
11
4
1
20
19
13
2
12
2
5
8
20
16
16
13
13
14
14
17
16
15
16
30
14
35
»*** *
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
33
31
30
30
30
30
29
30
30
30
30
31
31
31
30
30
30
29
29
30
30
31
31
31
31
31
31
30
**********
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
* *
* *
* »
* *
**
********
135
KVBll-6017-1266
-------
******************************
**
**
**
**
**
** DATE
-
TIME
LOAD
MWTH
02
voux
MEAS
******************************
** 8/27/80
** 8/27/80
*» 8/27/80
** 8/27/80
** 8/27/80
*» 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
«» 8/27/80
*« 8/27/80
** 8/27/80
«* 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
»* 6/27/80
** 6/27/80
** 8/27/80
** 8/27/80
«« 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
»* 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
*« 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
** 8/27/80
** S/27/80
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
** 0/0/0 0
******************!
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
7.8
6.5
6.6
9.8
8.3
9.7
5.9
7.6
6.7
7.4
8.4
8.4
7.0
7.9
9.3
9.8
8.9
9.8
9.2
9.5
8.7
9.1
8.4
9.0
9.3
9.1
9.3
9.0
10.1
8.7
9.4
9.6
7.0
8.0
9.0
7.9
7.6
9.2
7.3
7.8
7.3
8.7
7.6
7.5
.0
.0
.0
.0
************************************
15 MIN. DATA
DRY STACK GAS CONCENTRATION
C02
VOLX
MEAS
CO
PPMV
MFAS
NO
PPMV
MEAS
A********************
6.7
7.9
8.0
5.0
6.3
4.9
8.5
6.8
7.9
7.3
6.3
6.2
7.2
7.0
5.2
6*,0
4.8
5.4
5.2
5.9
5.1
6.6
5.0
5.6
4,7
4.e
5.6
4.0
6.2
5.1
4.8
7.6
6,4
5.5
6,4
6.6
5.3
6.9
6.5
7.0
5.7
6.7
6.7
.0
.0
.0
18
48
37
66
6
27
26
43
22
37
24
53
38
1
69
26
a
51
62
4
6
8
67
53
39
70
24
22
24
16
56
70
30
15
28
22
24
67
4
15
31
69
58
4fl
0
0
0
.0 0
*************«*'
41
45
46
36
40
35
47
40
46
45
39
38
40
42
34
32
36
32
33
35
38
33
39
32
36
31
31
34
28
37
31
32
41
36
32
36
38
33
38
37
38
34
3B
38
0
0
0
0
CO
PPMV
3X02
*******
24
59
46
106
8
43
31
57
27
49
34
75
48
1
106
41
5
82
94
6
8
12
95
79
60
106
37
33
39
23
87
110
38
20
42
30
32
102
5
20
40
JO!
78
64
0
0
0
0
NO
PPMV
3X02
************************
**
**
CO
NG/J
*****************
56
55
57
58
56
55
56
53
57
59
55
54
51
57
52
51
53
51
50
54
55
50
55
48
55
47
47
51
46
54
48
50
52
49
48
49
51
50
50
50
50
49
51
50
0
0
0
0
********
8
19
15
35
2
14
10
19
9
16
11
25
16
0
35
13
1
27
31
2
2
4
31
26
19
35
12
10
13
7
28
36
12
6
13
10
10
33
1
6
13
33
25
21
0
0
0
0
*********
NO
NG/J
****
30
30
31
31
30
30
30
29
31
32
30
29
27
31
28
27
29
27
27
29
30
27
30
26
30
25
25
27
25
29
26
27
28
27
26
26
26
27
27
27
27
27
27
27
0
0
0
1)
* * * ft
**
ACODE **
**
**
***********
**
**
**
**
**
**
**
**
**
**
* *
**
**
**
**
_ **
**
**
**
**
**
**
**
**
**
**
* *
**
**
**
**
**
* *
**
*»
**
* *
* *
**
* *
* *
* *
* *
* *
t **
# **
« **
**
***********
136
KVB11-6017-1266
-------
ft******************************
**
*»
**
** 02
** ' LOAD VOLX
«* DATE
TIME
MWTH
ft*********************
** 0/0/0 0 .0
** o/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
* O/ O/ 0
*» O/ O/ 0
* O/ O/ 0
** O/ O/ 0
*» O/ O/ 0
** O/ O/ 0
** O/ O/ 0
»* O/ O/ 0
** O/ O/ 0
*« O/ O/ 0
** O/ O/ 0
»* O/ O/ 0
** O/ O/ 0
** 8/28/80
** 8/28/80
** 8/28/80
*« 8/28/80
«« 8/28/80
*« 8/28/80
** 8/28/80
** 8/28/80
«* 8/26/80
** 8/28/80
** 8/28/80
** 8/28/80
** 8/28/80
** 8/28/80
»* 8/28/80
** 8/28/80
*» 6/28/80
** 8/28/80
ft* 8/28/80
** 8/28/80
** 8/28/80
** 8/28/80
»* 8/28/80
** 8/28/80
** 8/28/80
** 8/28/80
** 8/28/80
** 8/28/80
*'***********
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
545
600
615
630
645
700
715
730
745
800
815
830
845
900
915
930
945
1000
1015
030
045
100
115
130
145
1200
.0
.0
.0
.0
.0
.0
.0
!o
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
********
MEAS
******
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
5.4
5.4
5.1
3.8
«.l
4.4
3.7
3.4
3.9
4.5
4.7
5.1
5.0
5.7
1.0
5.6
6.1
6.3
6.4
6.5
6.7
6.4
6.3
6.3
5.2
4.8
5.0
5.1
* * * * *
A**********************************************************
15 MIN. DATA **
DRY STACK GAS CONCENTRATION **
**
C02 CO NO CO NO CO NO ACODE **
VOLX PPMV PPMV PPMV PPMV NG/J NG/J **
MEAS
****,*****
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
6.8
6.7
8,9
9.6
9,4
9.2
9,6
9,8
9,5
9.2
9,2
8,8
8,9
8.5
-1.0
8,6
8.5
8.3
8.2
8.1
e.i
8.2
8.3
8.3
9,0
9.2
9, 1
MEAS MEAS 3X02
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
31
52
270
450
372
311
425
059
371
275
296
184
218
161
-1
16
63
50
45
16
38
26
48
23
3
23
28
9.0 2
******************
0 0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
48
08
49
51
51
51
52
53
53
52
52
51
50
49
-1
48
47
47
47
06
48
48
48
46
50
49
50
49
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
C
0
0
35
60
305
«71
396
337
442
469
390
300
327
208
245
189
0
18
76
61
55
19
47
32
58
28
J
25
31
2
3X02 **
***#********************'***'**'**
000
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
55
55
55
53
54
55
54
54
55
56
57
57
56
57
0
56
56
57
58
57
60
59
58
58
57
54
56
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
11
19
101
155
130
111
146
155
128
99
107
68
81
62
0
6
25
20
- 18
6
15
10
19
9
1
8
10
55 0
it *************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
o
0
o
o
**
* *
**
**
* *
**
**
**
**
**
**
* *
**
**
**
**
**
**
**
**
30 **
30 **
30 **
28 **
29 **
30 **
29 **
29 **
30 **
30 **
31 **
31 **
30 **
31 **
0 C **
30 **
30 **
31 **
31 **
31 **
32 **
32 **
31 **
31 **
30 **
29 **
30 **
30 *»
******************
137
KVBll-6017-1266
-------
***********
**
**
**
*A
**
*» DATE
********************************************************
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
LOAD
HWTH
**************************
** 6/28/80
** 8/28/80
*» 8/28/80
** 8/28/80
** 8/28/80
** 8/23/80
** 8/28/80
** 8/28/80
** 8/28/80
** 8/28/80
** 8/28/80
** 6/28/80
** 6/28/80
** 8/28/80
** 8/28/80
** 8/28/80
** 8/28/80
*» 8/28/80
** 8/28/80
*» 8/28/80
*« 8/28/80
** 6/28/80
** 8/28/80
** 8/28/60
** 8/28/80
** 6/28/80
** 8/28/80
** 8/28/80
** 8/26/80
*» 8/28/80
** 8/28/80
** 8/26/80
** 8/28/60
** 6/28/80
** 8/28/80
** 8/26/80
** 8/28/80
** 8/28/80
** 8/28/80
** 8/28/80
** 8/28/60
** 8/28/80
** 8/28/80
*» 6/28/80
** O/ O/ 0
*» O/ O/ 0
** O/ O/ 0
*» o/ O/ 0
**********
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1505
J600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
0
.0
.0
.0
.0
,0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
***************
02
VOLt
ME AS
******
5.0
5.0
5,1
5.0
5.5
-1.0
4.9
4.7
5.3
5.5
fl.e
5.9
5,6
5.5
5.4
5.6
5.5
5.9
5.6
5.8
5.7
5.6
5.6
5.5
5.7
5.8
6.0
6.1
6.3
6.2
6.6
6.4
6.5
6.6
6.3
6.4
6.5
6.7
6.6
6.6
6.4
5.9
6.2
5.9
.0
,0
.0
.0
C02
VOLX
MEAS
CO
PPMV
MEA3
NO
PPMV
HEAS
CO
PPMV
3X02
NO
PPMV
3%02
*******
CO
NG/J
******************************************
9.1
9.1
9.0
9.1
8,8
1,0
9.2
9,2
9.0
6.8
9.2
6.6
8,8
6,9
6.9
8,8
8.9
8.6
8,9
8.6
8.9
8.7
8,8
8.8
8,7
8,7
6.6
6,6
6,5
8,5
6,2
8.3
8.3
6.3
6.4
6.3
8.3
6,2
8.2
6,2
8.4
8.7
8.6
6.7
.0
.0
.0
.0
13
19
18
11
15
-1
8
15
11
9
15
23
20
10
15
36
21
25
37
25
9
31
18
19
23
7
26
9
3
32
30
32
28
42
25
18
35
14
15
23
22
23
41
31
0
0
0
0
50
50
50
49
50
-1
53
53
54
52
53
51
52
«9
50
50
50
49
50
50
50
50
51
49
49
50
48
49
49
46
46
47
46
46
47
47
48
48
48
48
48
50
50
50
0
0
0
0
14
21
20
12
17
0
8
16
12
10
16
27
23
16
17
42
24
29
43
29
10
36
21
22
27
6
31
10
3
38
37
39
34
52
30
22
43
17
18
28
27
27
49
36
0
0
0
0
56
56
56
55
58
0
59
58
61
4,0
58
60
60
56
57
58
58
56
58
59
58
59
60
56
57
59
57
59
60
56
57
58
57
57
57
56
59
60
60
60
59
59
60
59
0
0
0
0
*****************************************
4
7
6
4
5
0
2
5
4
3
5
9
7
5
5
13
6
9
14
9
3
12
7
7
8
2
10
3
1
12
12
13
11
17
10
7
14
5
6
9
6
-------
*************************
»»
**
**
**
**
** DATE
TIME
LOAD
MWTH
******
02
VOLX
MEAS
******************************
15 HIN. DATA
D«Y STACK GAS CONCENTRATION
C02 CO NO CO
VOL% PPHV
MEAS MEAS
******************************************
** OX OX 0
** OX OX 0
** O/ O/ 0
** O/ O/ 0
** OX O/ 0
** OX O/ 0
** O/ OX 0
** o/ O/ 0
** OX OX 0
*» OX OX 0
«* OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** 8X29X80
** 8X29X60
** 8X29X60
«* 8X29X80
** 8X29X80
** 8X29X80
** 8X29X80
** 8X29/80
*« 8X29/80
** 8X29X80
** 8X29X80
** 8X29/80
** 8X29X80
*« 6X29/80
*« 8X29/80
** 8/29/80
** 8/29/80
** 8/29/60
** 8/29/80
** 8/29/80
** 8/29/80
** 8/29/80
** 8/29/80
** 8/29/80
** 8/29/80
** 8/29/80
** 8X29X80
** 8X29/80
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
5S5
600
615
630
605
700
715
730
745
800
815
830
845
900
915
930
945
1000
1015
3030
1045
1 100
1115
1130
1145
1200
******************
.0
.0
.0
o
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
,0
.0
.0
.0
.0
lO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
*******
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
10.0
10. 0
».!
7.1
7.0
9.3
6.9
8.6
6.e
10.8
fe.fl
5.9
5.7
6.1
6.1
5.8
1.9
a. 8
4.7
5.0
5.1
4.9
4.8
5.1
0.9
a. 9
a. 9
5.2
* * * ft *
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,o
.0
.0
.0
5.7
5.1
6.1
6.0
8.0
6.0
8.0
6.7
8.1
4.5
8.6
8.8
8.6
8.7
6.7
8.8
9.2
9.2
9.2
9.
'.
0.
9.2
9.
9.
9.1
9.2
9.0
************
PPHV
MEAS
PPMV
3X02
*******************************
* *
**
* *
NO CO NO ACOOE **
PPMV NG/J NG/J **
3X02
**
************************************************
0
0
0
0
0
0
o
o
l>
p
b
r
0
0
0
0
0
0
0
0
44
29
59
1
17
1
17
30
11
6
9
32
20
13
13
0
0
39
33
47
0
9
0
10
14
10
0
0
**
0
0
0
0
o
d*
0
0
0
0
0
0
0
0
0
0
0
o-
0
0
39
36
41
50
50
HI
47
43
as
35
51
52
52
53
53
53
52
52
52
52
51
51
50
50
51
50
51
52
********
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
72
19
89
1
21
1
21
43
13
10
11
38
23
15
15
0
0
«3
36
52
0
10
0
11
15
11
0
0
*******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
64
61
62
64
64
63
60
62
60
62
62
62
61
6«
64
62
58
57
57
58
57
57
55
56
57
55
57
59
**********
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
23
16
29
0
7
0
7
1«
4
3
3
12
7
5
5
0
0
1«
12
17
0
3
0
3
5
3
0
0
*******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
o
0
o
**
**
**
**
**
**
**
**
**
**
**
A*
**
**
A*
**
**
**
**
**
34 **
33 **
33 **
35 **
34 **
34 **
32 **
33 **
33 *»
33 **
34 **
33 **
33 **
34 **
34 **
34 **
31 **
31 **
31 **
31 **
31 **
30 **
30 **
30 **
30 **
30 **
30 **
3
-------
*********** 8/29/80
** 8/29/80
** 8/29/80
** 6/29/80
** 6/29/80
** 8/29/80
** 8/29/80
** 8/29/80
** 8/29/80
** 8/29/80
** 8/29/80
** 6/29/80
** 8/29/80
** 6/29/80
** 8/29/80
** o/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
15 MIN, DATA
DRY STACK GAS CONCENTRATION
- TIME
ft ft it "it ft ft i
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1405
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
0
*****************
LOAD
MWTH
ft ft ft ft ft ft j
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
02
VDLX
MEAS
ft ft Jfc ft ft '
4.8
5.3
5. 1
5.3
1.7
4,8
4.6
5.4
5.3
5.3
5.1
5.2
5.3
5.1
5.0
4.7
4.6
5.3
4.8
5.3
5.3
5.2
a. 9
5.1
5.0
4.9
4.7
5.0
5.0
5.1
5.0
5.1
5.2
5.2
5.4
5.2
5.0
4.7
5.2
5.1
5.0
5.0
4.6
a.B
.0
.0
.0
.0
************ a
C02
VOLX
MEAS
tftftftftftftfti
9.2
8.9
9.1
9.0
9,3
9.2
9.3
8.8
6.9
6,9
9.0
8.9
8.9
9.0
9.2
9.2
9.3
8.9
9.2
8.9
8.9
6.9
9.1
9.0
9.1
9.1
9.2
9,1
9.1
9.0
9,1
9.0
9.0
9.0
8.9
9.0
9.2
9.2
9.1
9.0
9,2
9.1
9.3
9.3
.0
.0
.0
.0
CO
PPMV
MEAS
42
25
10
33
43
15
16
20
6
8
16
11
15
46
31
22
38
2
28
0
25
14
7
73
47
16
0
2
7
24
25
23
29
39
0
5
27
3
19
8
21
16
0
0
0
0
0
0
NO
PPMV
MEAS
52
51
52
51
54
54
56
53
54
53
53
52
52
50
52
52
53
51
52
51
51
50
50
51
51
50
51
51
51
51
51
51
51
50
50
50
51
52
50
50
50
50
52
51
0
0
0
0
CO
PPMV
3%02
ft ft ft ft ft :
46
28
11
37
47
16
17
23
6
9
18
12
17
52
34
24
41
2
31
0
28
15
7
62
52
17
0
2
7
27
28
26
33
uu
0
5
30
3
21
9
23
18
0
0
0
0
0
0
****&*****«*«******«**«&£**«
NO
PPMV
35(02
t A A ft ft A A1 '
57
58
58
56
59
60
61
61
61
60
60
59
59
56
58
57
58
58
57
58
58
57
55
57
57
55
56
57
57
57
57
57
58
57
57
57
57
57
57
56
56
56
57
56
0
0
0
0
**&«***
CO
NG/J
rftftftftftftftt
15
9
3
12
15
5
5
7
2
3
5
a
5
17
11
8
13
0
10
0
9
5
2
27
17
5
0
0
2
8
9
8
10
14
0
1
10
1
7
2
7
5
0
0
0
0
0
0
********
NO ACODE
NG/J
31
31
31
31
32
32
33
33
33
32
32
32
32
30
31
31
31
31
31
31
31
30
30
31
31
30
30
31
31
31
31
31
31
30
31
30
31
31
30
30
30
30
30
30
0 »
0 »
0 »
0 »
*************
**
**
* *
**
**
**
* * * *
**
**
**
**
**
**
* *
**
**
**
**
**
**
»*
**
**
**
**
* *
* *
**
**
**
**
**
* *
**
* *
* *
**
**
* *
* *
* *
* *
* *
**
* *
* *
*
*
*
*
*
*
*
* *
* *
*** *
140
KVBll-6017-1266
-------
**
**
**
**
**
**
DATE
TIME
LOAD
MWTH
02
VOLX
MEA3
15 MJN. OAT*
DRY STACK GAS CONCENTRATION
C02 CO NO CO
VOLX PPMV PPMV PPMV
MEAS MEAS HEAS 3X02
NO
PPMV
3X02
CO
NGXJ
**
**
**
NO ACOOE **
NGXJ **
**
******************************************************************************************
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
»*
**
**
**
**
**
**
**
**
**
**
OX
OX
OX
OX
OX
OX
OX
OX
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
ox
9X
9X
9x
9X
9x
9X
9x
9x
9X
9x
9X
9X
9X
9X
9X
9X
9/
9X
9X
9/
9X
9/
9X
9X
9/
9/
9/
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
ox o
2X60
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
2X80
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
545
600
MS
630
645
700
715
730
7a5
800
815
830
845
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
* 9/ 2/80 1200 .0
A******************)
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
13.6
14.2
10.8
8.5
7.2
6.9
6.6
7.0
6.9
8.2
7.3
7.2
6.9
6.9
7.0
7.0
8.7
9.6
7.3
7.1
7.5
7.2
8.9
7.4
6.8
7.1
8.5
9.1
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
2.1
1.7
5.3
6.8
7.8
8.1
8.3
8.0
8.0
6.7
7.9
7.8
8.0
6.1
8.0
7.9
fc.5
5.8
7.6
7.6
7.5
7.6
<>.3
7.5
7.9
7.7
6.6
6.0
i********
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
22
19
to
0
14
10
0
30
18
19
1
15
0
17
32
IB
38
16
23
42
50
45
62
42
42
42
61
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
26
24
38
44
48
50
50
50
49
43
49
49
50
50
51
50
45
42
50
46
42
42
38
43
42
42
39
57 37
****************i
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
53
50
17
0
18
12
0
38
23
26
1
19
0
21
41
23
55
25
30
55
66
58
92
55
53
54
88
86
k****i
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
63
64
67
63
62
63
62
64
62
60
64
64
63
63
65
64
66
66
65
60
56
54
56
57
53
54
56
56
»******<
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
17
16
5
0
6
4
0
12
7
8
0
6
0
7
13
7
18
8
"9
18
22
19
30
18
17
17
29
28
>*****<
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
34 **
34 _ **
36 **
34 **
34 **
34 **
33 **
34 **
33 **
32 **
34 **
34 **
34 **
34 **
35 **
34 **
35 **
36 **
35 **
33 **
30 **
29 **
30 **
3D **
28 **
29 **
30 **
30 **
k****** **********
141
KVB11-6017-1266
-------
******************************************************************************************
**
**
**
ft*
**
* DATE
4k4t&A&A&AftAfti
** 9/ 2/80
** 9/ 2/80
** 9/ 2/80
« 9/ 2/80
ft 9/ 2/80
»* 9/ 2/80
* 9/ 2/80
9/ 2/80
* 9/ 2/80
** 9/ 2/80
* 9/ 2/80
ft* 9/ 2/80
** 9/ 2/80
«* 9/ 2/80
** 9/ 2/80
* 9/ 2/80
* 9/ 2/80
* 9/ 2/80
** 9/ 2/80
* 9/ 2/80
* 9/ 2/80
*« 9/ 2/80
ft 9/ 2/80
ft 9/ 2/80
ft 9/ 2/80
* 9/ 2/80
** 9/ 2/80
* 9/ 2/80
** 9/ 2/80
ft 9/ 2/80
ft* 9/ 2/80
ft 9/ 2/80
ft 9/ 2/80
* 9/ 2/80
* 9/ 2/80
* 9/ 2/80
ft* 9/ 2/80
* 9/ 2/80
« 9/ 2/80
9/ 2/80
* 9/ 2/80
9/ 2/80
* 9/ 2/80
** 9/ 2/80
** O/ O/ 0
** O/ O/ 0
* O/ O/ 0
** O/ O/ 0
15 MIN. DATA
DRY STACK GAS CONCENTRATION
-
TIME
! A ft ft A £ A
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
0
LOAD
MHTH
it ft ft it ft ft 1
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
02
VOLX
MEAS
t ft ft ft A A ft 4
8.6
9.4
8.6
11.0
10.0
10.2
10.6
11.3
9.6
10.6
10.4
9.0
8.0
9.9
9.4
9,1
10.4
12.7
11.2
12.0
13.0
11.7
12.0
12.4
11.3
11.9
11.1
11.0
9.8
11.2
10.6
10.8
10.5
10.8
9.9
10.1
10.4
8.9
10.0
9.0
8.9
9.2
8.9
10.2
.0
.0
.0
.0
C02
VOLX
HEAS
r ft ft ft ft ft ft 4
6.4
5.6
6.3
4.0
«.«
5.1
4.6
3.7
5.8
«.7
4.5
6.4
6.6
5.3
5.8
6.1
4.8
2.6
3.6
3,«
2.3
4.0
3.4
3.0
«.7
3.6
4.4
4.2
5.4
4.2
4.4
5.0
4.8
4.4
5.1
5.5
4.9
6.3
5.3
6.1
6.2
5.9
6.2
5.0
.0
.0
.0
.0
CO
PPMV
MEAS
r ft ft ft ft ft ft ^
50
73
68
91
65
115
85
71
100
78
68
78
47
87
93
55
84
112
59
101
83
82
103
61
76
95
62
80
85
84
54
68
105
69
84
99
82
52
67
51
54
50
60
75
0
0
0
0
NO
PPMV
MEAS
t ft ft * ft ft ft ri
40
36
40
33
35
38
35
32
38
33
32
38
38
35
36
38
33
25
27
29
22
29
26
25
31
28
30
29
34
25
30
33
31
30
32
35
33
37
35
38
38
37
38
33
0
0
0
0
CO
PPMV
3X02
kftftftftftftl
72
113
98
164
106
192
147
132
158
135
115
117
65
141
144
83
143
244
108
203
188
159
207
128
141
188
113
144
137
155
93
120
180
122
136
164
139
77
110
76
80
76
89
125
0
0
0
0
NO
PPMV
3X02
r ft ft ft ft ft * j
58
56
58
59
57
63
60
59
60
57
54
57
52
56
56
57
56
54
49
58
49
56
52
52
57
55
5«
52
54
46
52
58
53
53
52
58
56
55
57
57
56
56
56
55
0
0
0
0
CO
N6/J
********
2«
37
32
54
35
63
48
43
52
44
38
38
21
46
47
27
47
80
35
67
62
52
68
42
46
62
37
47
45
51
30
39
59
40
45
5«
46
25
36
25
26
25
29
Ul
0
0
0
0
9
NO ACODE
NG/J
rftftftftftftftftftftftH
31
30
31
32
31
34
32
32
32
31
29
31
28
30
30
31
30
29
27
31
27
30 - -
28
28
31
30
29
28
29
25
28
31
28
28
28
31
30
29
31
31
30
30
30
29
0 *
0 »
0
0 »
**
**
**
**
**
**
'it * * *
**
**
**
**
**
**
**
**
**
. **
**
**
**
**
**
.**
**
**
«*
**
**
_. . »*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
142
KVBll-6017-1266
-------
*****
**
**
**
*
**
**
* ** * *
WWW"" H
** ox
** ox
** o/
** O/
** ox
** o/
** o/
** o/
** o/
** o/
* o/
** ox
** o/
** o/
** ox
** o/
** ox
** o/
* o/
** ox
** V
** 9X
** 9/
** 9x
** 9X
** 9/
** 9/
** 9/
** 9/
** 9/
** 9/
** 9/
** 9x
** 9/
** 9x
** 9/
** 9/
** 9X
** 9/
»* 9/
** 9/
** 9/
** 9/
** 9/
** 9/
** 9X
** 9/
** 9/
******
*******
-
******<
t*********i
DRY
k*********
15
STACK GAS
02 C02 CO
DATE
ft ft ft ft ft ft
O/ 0
O/ 0
O/ 0
O/ 0
OX 0
O/ 0
O/ 0
O/ 0
OX 0
O/ 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
3X80
3/80
sx«o
3X60
3X60
3X80
3X80
3X80
3X60
3X80
3X80
3X80
3X80
3X80
3X80
3X60
3/80
3/80
3X80
3/80
3/80
3X80
3/80
3/60
3/80
3/80
3/80
3/80
TIME
ft ft ft ft ft ft A
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
545
600
615
630
605
700
715
730
745
600
615
630
645
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MWTH
ft ft ft ft ft ft '.
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
. .0
.0
.0
.0
VOCX VOLX PPMV
MEAS MEAS NEAS
rftftftftftftftftftf"
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
6.6
6.8
4.5
5.2
0.9
5.1
4.5
4.e
4.6
a. 9
5.3
6.2
«>.2
6.6
6.8
6. a
WKWWKWWWW
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.0 0
.2 158
.1 149
.4 613
.0 426
.2 578
.1 508
.4 590
.2 519
.4 561
.2 425
.0 410
.5 275
.5 273
.2 201
.1 0
.3 12
6.2 8.2 7
6.2 8.2 18
6.2 6.2 18
6.4 6.1 52
6.5 8.0 32
6.9 7.7 23
6.3 8.1 23
6.5 8.0 19
6. a 8.0 17
6.5 7.9 18
8.0 6,7 18
7.9 6.7 20
*********<
MIN, DATA
>*****«
»******<
»»*****<
CONCENTRATION
NO
PPMV
MEAS
ftwftftftftftft ft'
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
06
46
51
48
49
49
50
50
50
SO
50
48
48
46
46
46
45
45
44
44
44
43
44
44
43
43
39
39
CO
PPMV
3102
! ft ft ft ft ft i
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
197
189
669
485
646
575
643
577
616
475
470
334
332
251
0
14
8
21
21
64
39
29
28
23
20
22
24
27
NO
PPMV
3X02
t ft ft ft ft ft ft '
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
57
58
55
54
54
55
54
55
54
55
57
58
56
57
58
56
54
54
53
54
54
54
53
54
53
53
54
53
CO
NG/J
[ ft ft ft ft ft ft '
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
65
62
220
160
213
190
212
190
203
157
155
110
109
83
0
4
2
7
7
21
13
9
9
7
6
7
8
9
*****************
**
**
**
NO ACODE **
NGXJ **
**
[ftftftftftftftftf1
0
0
0
0
0
0
0
0
0
0
o
0
0
o
o
0
0
0
0
0
*WWW*»W«iW
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
31 «*
31 **
30 *«
29 **
29 **
30 **
29 **
30 **
29 **
30 **
31 **
31 **
31 **
31 *
31 «*
30 **
29 **
29 **
29 *
29 **
29 **
29 **
29 **
29 **
28 **
28 **
29 «*
29 **
******************************************************************************************
143
KVBll-6017-1266
-------
**
**
**
**
»*
** DATE
************
*» 9X
9X
«* 9/
* 9X
* 9X
** 9X
* 9/
»* 9/
** 9X
* 9X
* 9/
** 9/
** 9/
** 9/
* 9/
« 9X
** 9/
*« 9/
** 9/
** 9/
** 9/
«* 9X
* 9/
*» 9/
** 9/
* 9/
** 9/
** 9X
** 9/
** 9/
** 9/
* 9/
** 9/
*« 9/
*« 9/
** 9/
** 9X
** 9X
** 9X
** 9X
»* 9X
** 9X
** 9X
** 9X
** OX
** OX
* O/
** OX
3X80
3/60
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3/80
3/80
3/80
3X80
3X80
3X80
3X80
3X80
3X60
3/60
3/80
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3X80
3X60
3X80
3X60
3/80
OX 0
O/ 0
OX 0
OX 0
TIME
' ** *** **
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1600
1815
1830
1845
1900
ms
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
0
LOAD
MWTH
* 1k * * * I
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
;o
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
15 MIN. DATA
DRY STACK GAS CONCENTRATION
02 C02 CO NO CO
VOLX VOLX PPMV PPMV PPMV
MEAS
' It * * * It * *
6.1
7.9
6.6
6.3
0.2
6.1
5.9
6.1
6.1
5.9
7.8
7.6
6.0
7.9
7.7
5.9
5.9
.4
.5
.7
.8
.3
.8
12.0
9.8
11.8
9.4
11.4
9.6
12.7
11.1
10.5
9.3
11.2
9.0
8.8
10.8
10.1
9.1
9.9
8.6
9.6
10.3
9.6
.0
.0
.0
.0
MEAS
6.2
6.7
7.8
8,0
8.2
6.2
8.4
8.2
8.2
8.3
6.8
6.8
8.2
6.5
T.2
8.3
8.2
7.9
7.9
5.7
6.0
5.0
5.1
2.8
4,9
2.7
5.4
3,7
4,9
2.3
4,0
4.1
5,8
3,7
5.6
5.9
3.6
4.8
5.9
5.1
6.1
5.2
4.3
5.2
.0
.0
.0
.0
MEAS
[ It * * * * * '
25
32
17
2
0
35
12
13
10
30
6
17
24
18
66
5
24
20
15
23
0
27
21
0
16
36
26
15
20
20
35
31
7
8
2
26
0
1
10
0
18
22
26
13
0
0
0
0
MEAS
[******'
45
39
43
44
44
44
44
44
43
42
38
37
41
36
38
41
42
40
38
32
32
27
27
20
25
19
25
23
25
IB
23
22
29
24
30
30
22
26
31
28
30
28
26
30
0
0
0
0
3X02
r * * ifc * * *
30
44
21
2
0
42
14
15
12
35
8
22
28
24
89
5
28
24
18
33
0
41
33
0
25
70
40
28
31
43
63
53
10
14
3
38
0
1
15
0
26
34
U7
20
0
0
0
0
NO
PPMV
3X02
It*** A **4
54
53
53
53
53
53
52
53
52
SO
51
49
49
49
51
46
50
49
47
46
47
41
43
40
40
37
38
43
39
39
42
37
44
44
45
44
38
43
47
45
43
44
43
47
0
0
0
0
CO
NGXJ
>******
9
14
7
0
0
13
4
5
3
it
2
7
9
6
29
1
9
6
6
11
0
13
11
0
8
23
13
9
10
14
21
17
3
a
0
12
0
0
5
0
8
11
15
6
0
0
0
0
**
»*
«*
NO ACODE **
NGXJ **
» *** ***
29
29
29
29
29
28
28
28
28
27
28
27
26
26
27
26
27
26
25
25
25
22
23
21
21
20
21
23
21
21
22
20
24
24
24
24
21
23
25
24
23
24
23
2S
0
0
U
0
**
**********
**
**
**
**
*»
**
**
«*
**
. **
**
e»
*k
**
**
»*
**
*
**
**
' **
**
*»
**
**
**
**
**
*»
**
**
**
**
- . **,
**
**
**
**
**
**
**
* *
**
* *
**
**
**
» **
144
KVB11-6017-1266
-------
******
**
**
**
**
*
15 MIN. DATA
DRY STACK GAS CONCENTRATION
02 C02 CO NO CO
*» DATE
******
* OX
** OX
** OX
** OX
** OX
** OX
O/
** O/
** OX
* O/
»* OX
** ox
* O/
** OX
«* ox
»* ox
** ox
** ox
** ox
*« ox
** 9X
** 9/
** 9X
** 9X
«* 9X
** 9X
** 9X
** 9X
** 9X
** 9x
** 9X
** 9/
** 9X
** 9x
** 9X
** 9X
** 9X
** 9X
** 9X
** 9X
** 9X
** 9X
** 9X
** 9X
** 9X
** 9X
** 9X
»* 9X
*****<
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
OX 0
4X80
4x80
4X60
4X80
4X80
4X80
4X80
4X80
4X80
4X80
4X80
4X80
4X80
4X80
4X80
4X80
4X80
4X80
4X60
4X80
4X80
4X80
4X80
4X80
4X80
4X80
4X80
4X60
TIME
*******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
545
600
615
630
645
700
715
730
745
800
815
830
845
900
915
930
945
1000
1015
1030
1045
1100
J115
1130
1145
1200
LOAD
MWTH
*******
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.«
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
VOLX
MEAS
(******<
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
6.2
5.8
4.4
«.6
4.<>
4.6
4.0
s.*
3.8
3.8
4.0
«.l
«.7
5.3
5.4
5.7
5.8
7.1
5.6
5.<»
6.0
5.6
5.2
5.6
5.5
5.8
5.8
5.8
VOLZ
MEAS
*******
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
8.4
8.7
9.4
.3
.1
.3
.6
.6
.7
.7
.5
.5
.2
8.9
8.9
8.7
8.6
7.7
8.5
8.5
8.4
8.7
8.9
fl.6
8.7
8.6
8.5
8.5
PPMV
MEAS
******<
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
3
0
554
399
142
10
616
588
600
547
540
564
0
11
36
33
7
16
a
34
0
4
42
13
14
11
17
63
PPMV
MEAS
*******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
41
42
45
44
44
44
46
46
46
46
46
46
45
43
44
44
43
45
45
46
46
47
47
47
46
45
44
43
PPMV
3X02
******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
3
0
601
438
158
10
652
619
628
572
571
600
0
12
41
38
8
20
4
40
0
4
47
15
16
13
?0
7«
********
NO
PPMV
3X02
********
CO
NG/J
***************
**
**
**
NO ACODE **
NGXJ **
**
*******************************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
49
49
48
48
49
48
48
48
48
48
48
49
49
49
50
51
50
58
53
54
55
54
53
54
53
53
52
50
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
1
0
19ft
144
52
3
215
204
207
189
188
198
0
4
13
12
2
6
1
13
0
1
15
5
5
u
6
2«
0
u
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
**
**
**
A*
**
ft*
**
**
**
**
**
**
**
**
**
**
**
**
*»
**
27 **
27 **
26 **
26 **
26 «*
26 *»
26 **
26 **
26 **
26 **
26 **
26 **
26 **
26 «*
27 **
28 **
27 **
31 **
28 **
29 **
29 **
29 **
29 **
29 **
29 **
28 **
28 **
27 **
******************
*************************************************************
145
KVB11-6017-1266
-------
A*******************************************
** 15 WIN. DAT*
** DRY STACK GAS CUNCENTRATION
**
**
**
LOAD
** DATE
**;***^****^
* 9/
** 9/
** 9/
** 9/
ft 9/
* 9/
ft* 9/
ft* 9/
* 9/
ft* 9/
** 9/
« 9/
*« 9/
** 9/
* 9/
ft 9/
* 9/
*. 9/
** 9/
* 9/
* 9/
** 9/
9/
9/
** 9/
** 9/
** 9/
ft* 9/
** 9/
ft* 9/
ft 9/
ft* 9/
** 9/
* 9/
ft 9/
9/
* 9/
ft 9/
« 9/
ft 9/
9/
ft 9/
9/
« 9/
* O/
O/
O/
* o/
4/60
4/80
4/80
4/80
4/80
4/80
4/80
4/80
4/80
4/60
4/80
4/80
4/60
4/80
4/80
4/80
4/80
4/60
4/80
4/60
4/60
4/80
4/60
4/80
4/80
4/80
4/80
4/80
4/60
4/60
4/80
4/80
4/60
4/60
4/60
4/80
4/80
4/60
4/80
4/80
4/60
4/80
4/60
4/60
O/ 0
O/ 0
O/ 0
O/ 0
TIME MWTH
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1615
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
0
m m w ** w m
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
02 C02
VOLX VOLX
MEAS MEAS
**************!
6.0 8.4
6.2 8.3
6.2 8.2
5.7 8.5
5.7
5.0
5.6
5.9
6.1
6.1
5.6
5.9
5.5
5.7
5.7
6.2
6.1
5.8
6.1
5.6
5.7
5.7
5.6
5.8
5.3
5.9
6.1
.6
.9
.7
.5
Is
.5
I?
.7
,6
.2
.3
.5
*
9
9
f
f
6.8 7.
6.8 7.
6.9 7.
6.4 8.2
7.1 7.7
6.8 8.0
7.1- 7,7
6.6 8,0
6.6 .1
6.7 .0
6.3 .2
6.5 .1
6.6 .2
6.6 ,1
6.2 8.4
6.4 6.2
6.5 8.2
.0 .0
.0 .0
.0 .0
.0 .0
CO
PPMV
MEAS
'******!
59
6
26
49
10
40
11
11
41
32
41
25
0
45
44
23
20
18
61
26
26
13
16
75
13
17
23
20
19
20
23
18
16
19
23
18
21
26
25
24
29
31
25
33
0
0
0
0
NO
PPMV
MEAS
r ****** 1
43
42
41
41
42
43
50
46
48
46
46
48
48
49
49
48
48
51
48
50
50
50
51
50
51
49
49
47
46
46
47
47
46
46
50
49
49
49
49
50
51
50
51
51
0
0
0
0
CD
PPMV
3XU2
********
70
7
31
57
li
45
12
13
49
38
48
29
0
52
51
26
24
21
73
30
30
15
21
68
14
20
27
25
24
25
28
23
22
24
28
22
26
34
31
30
36
37
30
41
0
0
0
0
NO
PPMV
3X02
*******
51
51
49
48
49
48
56
57
58
55
54
57
55
57
57
56
58
60
58
58
58
58
59
59
58
56
59
59
58
56
58
60
60
62
62
61
61
60
60
62
63
60
62
63
0
0
0
0
CO
NG/J
t*** * **
23
2
10
19
3
14
4
4
16
12
16
9
0
17
17
9
7
7
24
10
10
5
6
29
4
6
9
8
7
8
9
7
7
8
9
7
8
11
10
9
11
12
10
13
0
0
0
0
NO ACUOE
NG/J
A***********
26
27
27
26
26
26
31
31
31
30 _
29
31
30
31
31
31- - -
31
32
31
31
31
. -31
32
32
31
31
32
32
31
31
31
33
33
33 -
33
33
33
32
33
33
34
33
34
.34
0
0 »
0 »
0
**
**
**
**
**
at
t**
**
**
**
**
**
**
**
**
**
ft«
«*
ft*
**
**
**
*«
ft*
**
ft*
**
«*
ft
*
«*
ft*
**
**
**
**
ft*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
«*
146
KVBll-6017-1266
-------
**
**
**
**
**
** DATE
A/AAAAAAAAAA
** OX OX 0
** OX OX 0
* OX OX 0
** OX O/ 0
* OX O/ 0
* O/ OX 0
» O/ O/ 0
** OX OX 0
** OX OX 0
« OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
«* O/ OX 0
** OX OX 0
** OX OX 0
* OX OX 0
*« OX OX 0
»* OX OX 0
* 9X 5X80
«» 9X 5X80
** 9X 5X80
* 9X 5X80
»» 9X 5X80
* 9X 5X80
«* 9X 5X80
* 9X 5X80
« 9X 5X80
»» 9X 5X80
** 9X 5X80
** 9x 5X80
** 9X 5X80
» 9X 5X80
* 9/ 5X80
** 9X 5X80
* 9X 5X80
*» 9X 5X80
** 9X 5X80
«* 9X 5X80
** 9X 5X80
** 9X 5X80
* 9X 5X80
** 9X 5X80
** 9X 5X60
** 9X 5X80
*» 9X 5X80
** 9X 5X80
*«***»*****
J5 HIN. DATA
DRY STACK GAS CONCENTRATION
TIME
A A * A 4 *
r W W W W W
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
545
600
615
630
645
700
715
730
7as
800
815
830
805
900
915
930
945
1000
1015
1030
1015
1100
1115
1130
1145
1?00
******
LOAD
MWTH
A A A A A A^
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
*******
02
VOLX
MEAS
A A A A A A
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
. .0
.0
.0
.0
.0
.0
.0
.0
.0
.0
6.6
6.5
5.«
5.0
.8
.7
.9
.3
.4
.9
5.1
5.4
5.4
6.0
5.6
"1.0
5.8
6.0
6.1
5.8
5.4
5.4
5.2
5.9
5.3
5.7
4.8
5.3
C02
VOLX
MEAS
t A A A A A A i
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
8.2
B.a
.0
.2
.2
.«
.7
.5
.5
.2
.2
.9
.0
.6
.8
- .0
8.7
8.6
8.5
8.6
8.9
6.8
8.9
8.5
8.8
8.6
9.1
8,8
CO
PPMV
MEAS
' A A It A A A :
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
4
33
41
143
156
408
55
44
71
0
0
3
6
-1
60
29
76
96
139
15
80
21
72
11
105
150
NO
PPMV
MEAS
f A A A A 1t A '
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
51
56
55
56
56
57
59
58
59
57
57
56
56
54
55
1
52
47
47
47
46
48
50
48
49
49
49
46
CO
PPMV
3X02
r A A A A A A i
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
4
37
45
158
164
439
59
49
80
0
0
3
7
0
71
34
91
113
160
17
91
25
82
12
116
172
NO
PPMV
3X02
' A it A A It A i
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
63
69
63
63
62
62
62
62
64
63
64
64
64
64
64
0
61
56
56
55
55
55
57
57
56
57
54
55
CO
NGXJ
r A A A A A A :
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
1
12
15
52
54
145
19
16
26
0
0
1
2
0
23
11
30
37
53
5
30
8
27
4
38
56
**
**
**
NO ACODE **
NGXJ **
**
lAAAAAAAA^*
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
(HHWWWKH
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
34 **
37 **
34 **
34 **
33 **
34 **
33 **
33 **
34 **
34 **
35 «*
35 **
35 **
35 **
34 »*
0 C **
33 **
30 *
30 **
30 **
30 **
30 **
30 **
31 **
30 **
31 **
29 **
29 **
*****************************************************************
147
KVBll-6017-1266
-------
**
*
«*
**
**
** DATE
***********
** 9/ 5/80
** 9/ 5/80
«* 9/ 5/80
** 9/ 5/80
** 9/ 5/80
** 9/ 5/80
** 9/ 5/80
»* 9/ 5/80
* 9/ 5/80
* 9/ 5/80
* 9/ 5/80
** 9/ 5/80
** 9/ 5/80
* 9/ 5/80
** 9/ 5/80
** 9/ 5/80
»* 9/ 5/80
** 9/ 5/80
** 9/ 5/80
** 9/ 5/80
* 9/ 5/80
** 9/ 5/80
** 9/ 5/80
** 9/ 5/60
** 9/ 5/80
** 9/ 5/80
*« 9/ 5/80
** 9X 5/80
*« 9/ 5/80
** 9/ 5/80
* 9/ 5/80
» 9/ 5/80
** 9/ 5/80
** 9/ 5/80
*« 9/ 5/80
«* 9/ 5/80
** 9/ 5/80
** 9/ 5/80
«* 9/ 5/80
** 9/ 5/80
** 9/ 5/80
«« 9/ 5/80
*» 9/ 5/80
** 9/ 5/80
** O/ O/ 0
** O/ O/ 0
* O/ O/ 0
* O/ O/ 0
***********
15 MIN. DATA
DRY STACK GAS CONCENTRATION
02 CO? CO NO CO
LOAD VOLX VOtX PPMV PPHV PPMV
TIME
********
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
19flS
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
0
»*»*****
MWTH MEAS
************
.0 5.7
.0 5.7
.0 5.9
.0 5.9
,0 -1.0
.0 5.7
.0 5.6
.0 5.5
.0 5.8
.0 5.6
.0 5.7
.0 6.0
.0 S.7
.0 6.1
.0 5.9
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.1
.0
.0
.7
.0
.7
.8
.5
.6
.4
.3
.3
.4
.3
.2
.3
.3
.2
.8
.8
.9
.7
.0 7.0
.0 7.0
.0 7.0
.0 6.6
.0 6.5
.0 6,fe
.0 6.8
.0 .0
.0 .0
.0 .0
.0 .0
************
MEAS
F*******
8.6
8.6
8.5
8.4
-1.0
8.6
8.8
8.6
8,6
8.6
8.6
6.4
8.6
8.3
8.5
8.3
8.4
8.4
8.6
8.4
8.0
8.0
8.1
8,1
8.2
.4
.3
.3
.4
.4
.3
.2
.5
.2
.3
.2
.3
6.1
8.1
8.1
8.3
8.3
8.3
8.2
.0
.0
.0
.0
********
MEAS
I* ***** 1
17
10
10
37
-1
15
56
51
55
59
27
59
25
37
53
38
31
9
15
37
18
27
26
26
22
30
27
24
33
33
45
35
25
37
50
32
43
37
15
27
10
3
22
29
0
0
0
0
*******
MEAS
****** *1
49
48
48
47
1
47
48
46
46
46
47
46
46
44
44
44
44
42
43
44
45
45
44
44
45
43
43
43
43
43
43
42
43
42
43
43
43
43
44
U4
44
14
45
45
0
0
0
0
*******
3X02
»** *** * 1
20
11
11
44
0
17
65
59
65
69
31
70
29
40
63
45
37
10
17
44
22
34
32
32
27
36
33
29
40
40
55
42
30
46
63
40
54
47
19
34
12
3
27
36
0
0
0
0
»***»*»!
NO
PPMV
3X02
»******!
57
56
57
56
0
55
56
53
54
S3
55
55
54
53
52
53
52
50
50
52
56
57
54
55
55
52
52
53
52
52
52
51
52
53
54
54
54
55
56
56
55
54
56
57
0
0
0
0
»*****»
CO
N6/J
>*»****
6
3
3
14
0
5
21
19
21
22
10
23
9
14
20
15
12
3
5
14
7
11
10
10
8
12
10
9
13
13
18
14
10
15
20
13
17
15
6
11
4
1
9
12
0
0
0
0
»******!
NO ACODE
NG/J
***********
31
30
31
30
0 C
30
30
29
29
29
30
29
29
28
28
28
28
27
27
28
30
30
29
29
30
28
28
28
28
28
28
27
28
28
29
29
29
30
30
30
29
29
3U
30
0
0 0
0
0 «
t**********i
»«
fi*
*tt
««
e*
a*
*****
**
«
-------
**
**
**
**
**
** DATE
15 MIN. 0*TA
TIME
LOAD
MWTH
DRY STACK
02 C02
VOLX VOLX
MEAS MEAS
GAS
CO
PPMV
MEAS
CONCENTRATION
NO
PPMV
MEAS
CO
PPMV
3X02
NO
PPMV
3X02
CO
NG/J
**
**
**
NO ACUDE **
NGXJ **
**
******************************************************************************************
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
«* OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** 9X flXBO
** 9X 8X80
«* «X 8X80
* 9X 8X80
** 9X 8X80
** 9X 8X80
** 9X 8X80
** 9X 6X80
** 9X 8X80
** 9X 8X80
** 9X 8X80
** 9X 8X80
** 9X 8X80
** 9X 8X80
** 9/ axao
** 9x 8X80
** 9X 8X80
** 9X 8X80
** 9/ 8X80
** 9X 8X80
** 9X 8X80
** 9X 8X80
** 9X 8X80
** 9/ 8X80
** 9X 8X80
** 9X 8X80
** 9X 8X80
** 9X PXflO
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
505
600
615
630
645
700
715
730
745
800
815
830
80S
900
915
930
90S
1000
1015
1030
1045
1100
1115
1130
11«5
1200
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
*o
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
.0 .0
6.2 8.3
6.5
6.4
6.6
5.5
«.l
«.2
4.4
«.*
4.9
5.1
5.1
5.0
4.9
5.0
4.8
4.9
4.7
5.0
5.3
5.3
.2
.2
.1
.«
.6
.5
.4
.3
.2
*
9
9
*
.2
.2
.2
.1
.0
.9
5.5 8.8
5.3 8.9
5. a 8.8
5.8 8.7
5.9 8.6
5.8 8.7
6.1 8.4
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
4
3
33
33
4
531
516
362
121
327
237
202
369
319
331
287
310
251
306
254
176
125
30
197
23
32
21
4
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
47
47
46
46
49
51
52
51
51
51
51
51
51
52
52
52
52
53
51
49
50
49
49
49
48
4B
48
46
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
4
3
40
41
4
565
553
392
132
365
268
228
415
356
372
319
346
277
344
291
201
145
34
227
27
38
24
4
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
57
58
56
57
56
54
55
55
56
57
57
57
57
58
58
57
58
58
57
56
57
56
56
56
56
57
56
58
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
1
1
13
13
1
186
182
129
43
120
88
75
137
117
123
105
114
91
113
96
66
47
11
75
9
12
e
i
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
o
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
31 **
31 **
30 **
31 **
30 **
29 **
30 **
30 **
30 **
30 **
31 **
31- **
31 **
31 . **
31 **
31 **
31 **
31 **
31 **
30 **
31 **
30 **
30 **
30 **
30 **
31 **
30 **
31 **
A******.**************************************************.********************************
149
KVB11-6017-1266
-------
**
*»
**
**
*
ft*
**<
**
**
ft*
ft*
**
ft*
ft*
**
ft*
ft*
**
ft*
**
ft*
ft*
**
**
**
**
ft*
ft*
**
**
**
**
**
ft*
**
ft*
ft*
ft*
**
**
**
**
**
**
**
ft
ft*
**
**
ft*
**
**
ft*
**
**
DATE
t********J
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9X
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
9/
O/
O/
O/
8/60
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
8/60
8/80
8/80
8/80
6/80
6/80
8/80
8/80
8/80
8/80
8/80
8/80
8/80
B/80
8/80
O/ 0
O/ 0
O/ 0
TIME
1 A A A A A 4 A
1215
1230
1245
1300
1315
1330
1315
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1TOO
1715
1730
1745
1800
1615
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
231S
0
0
0
LOAD
M*TH
£ 6 A It It ft
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
«o
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
15 MINe DATA
OR? STACK GAS CONCENTRATION
02 C02 CO NO CO
VULX VOLX PPMV PPMV PPMV
MEAS
6.2
6.6
6.6
6.4
.3
.0
.0
.2
.5
.5
.6
.6
.3
.8
,4
.9
6.7
6.7
6e6
6.8
7.0
6.9
7.4
7.2
7.0
6.9
7.1
7.0
7.2
7.1
7.1
7.4
7.3
6.9
7.0
6.9
6.8
6.9
6.6
6.4
6.2
6.6
6.0
6.7
6.9
.0
.0
.0
MEAS
***.****,'
8.4
6.2
8. I
8.3
8.4
8.4
6.5
8,3
6.2
6.3
8.2
8.2
8.4
6.1
8.4
8.1
8.1
8,1
8.2
I,*
8.1
8.1
7.8
7.9
8.1
8.1
7.9
8.0
8,0
6.0
8.1
6.0
8.0
8.3
8.1
8.2
8.3
8.2
8.4
8.5
8,5
6.4
8.7
8.3
8.2
.0
.0
.0
MEAS
r 1i * 1t A A It 1
33
28
49
18
17
16
13
10
0
27
27
18
2
13
38
19
0
46
61
33
44
32
34
19
37
23
32
51
49
4
49
15
4
41
8
5
0
0
25
60
9
0
39
0
1
0
0
0
MEAS
r* *. * * A * 1
47
47
46
46
47
47
49
48
48
48
49
49
SO
49
49
49
50
49
50
46
46
47
47
47
46
47
48
48
49
49
49
48
49
49
49
49
50
49
49
49
49
50
50
49
50
U
0
0
3X02
r ******
40
35
6!
22
20
19
15
12
0
33
34
22
2
16
46
24
0
57
76
41
56
40
45
24
47
29
41
65
64
5
63
19
5
52
10
6
0
0
31
74
10
0
46
0
!
0
0
0
NO
PPMV
3%02
********
57
58
57
56
57
56
58
58
59
59
62
61
61
62
60
62
63
61
62
60
61
60
62
61
59
60
62
61
64
63
63
63
64
62
63
62
63
62
61
60
59
62
60
61
63
0
0
0
CO
NG/J
fr* ft*ft**
13
11
20
7
6
6
5
4
0
It
U
7
0
5
15
8
0
19
25
13
18
13
14
8
15
9
13
21
21
1
20
6
1
17
3
2
0
0
10
24
3
0
15
0
0
0
0
0
*e
**
*
NO ACODE **
NG/J e*
fc *****;
31
31
31
30
31
30
31
31
32
32
33
33
33
33
32
33
34
33
33
33
33
32
33
33
32
32
33
33
34
34
34
34
34
33
34
33
34
33
33
32
32
33
32
33
3«
0
0
0
*«********************************************************fi*********************j
ft*
k ft ********
««
ft
*e
ft*
**
**
ft*
**
**
ft
ft*
«*
*6
ft
ft*
ft*
tt*
ft*
ft
ft«
ft*
ftft
ft*
ft*
ft*
**
ft*
ft*
*«
e*
*c
ft*
**
**
ft*
ft
**
*ft
**
ft*
*
**
ft*
»*
* *
« **
e **
* **
k*********
150
KVB11-6017-1266
-------
**
**
**
**
**
** DATE
************
** OX OX 0
* OX OX 0
** 9/ OX 0
** OX OX 0
** OX OX 0
** O/ OX 0
*« O/ OX 0
** OX OX 0
*» OX OX 0
OX OX 0
** QX OX 0
*» OX OX 0
** OX OX 0
* OX OX 0
** OX OX 0
* OX OX 0
»* OX OX 0
** ox ox o
** OX OX 0
** ox ox o
** 9X 9X60
** 9X 9X80
** 9X 9/80
** 9X 9X80
** 9/ 9X80
** 9/ 9X80
** 9X 9/80
** 9X 9/80
** 9/ 9/80
* 9/ 9/80
** 9X 9X80
** 9X 9X80
** 9X 9X80
** 9X 9X80
** 9X 9/80
** 9/ 9/80
*» 9X 9X80
* 9X 9/80
** 9/ 9X80
*« 9X 9X80
* 9X 9X80
*» 9X 9X80
* 9X 9/80
** 9/ 9/80
** 9/ 9/80
** 9X 9X80
* 9X 9/80
** 9/ 9/80
15 HIN. DATA
DRY STACK GAS CONCENTRATION
02 C02 CO NO CO
TIME
******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
515
530
545
600
615
630
645
700
715
730
745
800
815
830
845
900
915
930
9«5
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MWTH
*******
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
,0
.0
0
.0
.0
.0
.0
.0
<0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
VOLX
MEAS
*******
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
6.0
6.5
5.3
2.8
2.<>
2.6
2."
2.4
2.4
a. 7
2.9
3.5
4.3
1.0
4.6
4.8
5.3
5.5
5.7
5.7
7.5
8.3
9.1
9.9
9.8
9.9
9.6
9.6
VOLX
MEAS
******^
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
8.9
8.6
S3
10.4
10.4
10.4
10,4
10.4
10.4
10.2
10.2
9.9
9.6
1.0
9.4
9.3
9.0
8.8
8.7
8.7
7.6
7.0
6.5
5.9
6.0
5.8
6.0
6.0
PPHV
MEAS
*******
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
198
38
562
2168
2276
2276
2275
2273
2274
2065
2019
1775
1063
-1
190
1348
1107
120
727
140
30
68
0
2
13
9
3
16
PPMV
MEAS
* * * * A * t
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
52
51
53
55
55
55
56
56
55
56
56
56
55
1
53
50
49
48
48
48
50
47
44
41
41
40
40
40
PPMV
3X02
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
237
47
644
2144
2226
2226
2201
2199
2200
2030
2007
1826
1146
0
208
1496
1270
139
856
164
40
96
0
3
20
14
it
?5
NO
PPMV
3X02
********
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
62
63
60
54
53
53
54
54
53
55
55
57
59
0
58
55
56
55
56
56
66
66
66
66
66
65
63
63
CO
NG/J
r*** A* A*
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
78
15
212
707
735
735
726
726
726
670
662
602
378
0
68
494
419
46
282
54
13
31
0
1
6
4
1
8
**
**
**
NO ACODE **
NGXJ **
**
***************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
o
0
o
o
o
0
**
**
**
**
**
**
**
**
**
**
**
»*
*»
**
*
**
**
**
«*
**
33 **
34 . **
32 **
29 *
29 **
29 «*
29 *
29 . _ **
28 *
29 *
30 «»
31 **
32 **
0 C **
31 «*
30 *«
30 **
30 **
30 *«
30 -**
36 **
36 **
36 **
36 **
35 **
35 **
3« **
34 **
k************
151
KVBll-6017-1266
-------
ft*
**
**
** DATE
********ftftfti
«* 9/ 9/80
** 9/ 9/80
** 9/ 9/80
** 9/ 9/80
** 9/ 9/80
** 9/ 9/80
*» 9/ 9/80
ft* 9/ 9/80
ft 9/ 9/80
** 9/ 9/80
** 9/ 9/80
** 9/ 9/80
** 9/ 9/60
*« 9/ 9/80
* 9/ 9/80
** 9/ 9/80
** 9/ 9/80
** 9/ 9/80
** 9/ 9/80
** 9/ 9/80
ft 9/ 9/80
«* 9/ 9/80
ft* 9/ 9/80
** 9/ 9/80
* 9/ 9/60
** 9/ 9/80
9/ 9/80
* 9/ 9/80
** 9/ 9/80
** 9/ 9/60
9/ 9/80
* 9/ 9/60
** 9/ 9/80
** 9/ 9/80
** 9/ 9/60
ft* 9/ 9/60
** 9/ 9/60
ft* 9/ 9/80
* 9/ 9/80
ft* 9/ 9/80
** 9/ 9/80
* 9/ 9/80
** 9/ 9/60
* 9/ 9/80
*« O/ O/ 0
** O/ O/ 0
O/ O/ 0
O/ O/ 0
IS MIN, DATA
DRY STACK GAS CONCENTRATION
TIME
k A A A A A A
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1600
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
0
0
0
0
LOAD
MhTH
A A A A A A 4
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
02
VOL%
MEAS
tAAAAAA4
9.8
9.9
9.6
10.3
10.0
10.3
9.8
10.1
10.3
10.1
9.9
10.3
9.8
to.i
10.3
10.4
10.5
10.4
10.5
10.6
10.4
10.3
10.6
10.8
10.4
10.6
10.3
10.4
10.3
10.5
10.4
10.3
10.3
10.4
10.6
10.2
10.1
10,2
10.4
10.3
10.1
10.2
10.2
10.5
.0
.0
.0
.0
C02
VOU
MEAS
KAAAAAA4
6.0
5.7
6.0
5.3
5.6
5.3
5.8
5,5
5.3
5.6
5.8
5.5
5.9
5.5
5.4
5.2
5.1
5.1
5.2
5.1
583
5.4
5.2
4.9
5.4
5.2
5.4
5.4
5.4
5.2
5.4
5.4
5.4
5.4
5.3
5.6
5.7
5.6
5.4
5,5
5.6
5.5
5.6
5.2
.0
,0
,0
.0
CO
PPMV
MEAS
k A A AA A Al
31
44
0
3
24
16
15
23
13
5
6
2
14
4
25
24
14
14
14
24
23
13
14
12
15
12
16
15
14
12
13
18
14
15
12
14
14
14
14
26
16
21
16
41
0
0
0
0
NO
PPMV
MEAS
b A A A A A A 4
41
40
43
36
39
37
40
36
37
38
39
37
40
39
38
36
37
37
37
35
38
38
37
34
38
37
39
39
38
39
39
39
40
38
39
40
40
40
38
38
40
40
40
3d
0
0
0
0
CO
PPMV
3% (12
t**ft ***i
«9
71
0
5
39
27
24
38
21
8
9
3
22
6
42
40
24
23
24
41
39
21
24
21
25
20
30
25
23
20
22
30
23
25
20
23
23
23
23
47
26
35
26
70
0
0
0
0
NO
PPMV
3X02
t*fi***ft*
66
65
68
60
64
62
64
62
62
62
63
62
64
64
64
61
63
63
63
60
64
64
64
60
64
64
65
66
64
67
66
65
67
64
6?
66
66
66
64
64
66
66
66
65
0
0
0
0
CO
NG/J
ifi*****i
16
23
0
1
13
8
7
12
7
2
3
1
7
2
13
13
7
7
7
13
12
7
6
7
8
6
10
8
7
6
7
10
7
8
6
7
7
7
7
15
8
11
8
23
0
0
0
0
NO ACUDE
NG/J
»******«**«
35
35
36
32
34
33
34
34
33
34
34
33
34
35
34
33
34
34
34
32
35
34 .-.
34
32
35
34
35
36
34
36
36
35
36
35
36
36
35
36
35
34
35
36
36
35
0 »
0
0 e
0 *
«e
fie
*
a
ftfi
*«
«*
ft*
&&
*e
a*
a ft
fie
ft*
»»
e*
«
ft*
«
Oft
*
«
ft*
*
*«
**
«
fift
e
*
*
*
.**
**
ee
*
**
**
*
«
*
«
*«
«*
**
**
*e
*s
**
«
»*
152
KVBll-6017-1266
-------
**
**
*»
**
**
** DATE
*****A*£***4
** ox ox o
* O/. O/ 0
** OX O/ 0
** OX OX 0
** OX O/ 0
** O/ OX 0
*« O/ O/ 0
* OX O/ 0
** OX O/ 0
** OX OX 0
«* OX OX 0
** OX OX 0
« OX OX 0
** O/ OX 0
* OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
** 9X10X80
** 9X10X80
* 9X10X80
** 9X10X60
** 9X10X80
** 9X10X80
** 9X10X80
** 9/10X80
** 9X10X80
* 9X10X80
** 9/10X80
«* 9X10/80
** 9X10X80
** 9X10X80
** 9/10/80
*» 9X10X80
** 9X10X80
»» 9/10X80
* 9X10X80
** 9/10/80
* 9/10X80
** 9X10X80
»* 9X10X80
» 9X10X80
«* 9X10X80
** 9X10X80
** 9X10X80
*« 9/10/80
** 9/10X80
IS MIN, DATA
DRV STACK GAS CONCENTRATION
02 COS CO NO CO
TIME
*** it it;
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
500
SIS
530
545
600
615
630
645
700
715
730
745
800
. 815
8JO
84S
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
*****************
LOAD
MWTH
******]
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
o
.0
.0
.0
.0
.0
.0
.0
.0
.0
*o
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
tO
.0
*******
VOL*
ME AS
'******!
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
13.0
10.0
10.3
9.4
7.0
7.3
7.8
6.9
6.7
6.9
7.2
6.9
6.7
6.8
7.0
8.0
7.4
8.0
8.7
8.4
8.0
-1.0
-1.0
-1.0
-1.0
-1.0
9.8
9.0
10.0
*******
VOLX
MEAS
* * * * * * t
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
2.8
5.7
5.2
6.1
7.8
7.7
7.2
7.8
8.0
7.8
7.4
7.7
7.9
7.8
7.0
6.9
7.4
7.1
6.9
6.8
7.2
-1.0
-1.0
-1.0
-1..0
-1.0
5.0
5.7
5.»
PPMV
MEAS
****** 4
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
2
11
11
337
873
885
697
880
842
1003
539
887
927
914
713
78
677
637
38
64
420
-1
-1
-1
!
-1
29
37
«7
PPMV
MEAS
****** 4
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
23
39
38
41
47
46
45
48
48
49
49
48
49
49
46
46
46
45
44
04
45
-1
-1
-1
-1
-1
41
40
39
PPMV
3X02
****** 1
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
4
18
IB
524
1124
1164
952
1125
1061
1282
704
1134
1168
1160
918
108
897
883
55
91
582
0
0
0
0
0
46
Sb
77
NO
PPMV
3X02
*******'
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
52
64
64
63
60
60
61
61
60
62
64
61
61
62
61
63
60
62
64
63
62
0
0
0
0
0
66
60
64
CO
NG/J
********
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
1
5
6
173
371
384
314
371
350
423
232
374
385
383
303
35
296
291
18
30
192
0
0
0
0
0
15
18
25
**
**
**
NO ACUOE **
NG/J **
*»
***************
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
**
**
**
**
**
*«
**
**
**
**
**
**
*
**
**
**
**
**
**
28 **
34 **
34 ..- _ **
34 **
32 **
32 **
33 **
33 «*
32 **
33 **
34 **
33 **
33 **
33 **
33 _ *»
34 **
33 »*
33 **
35 **
34 **
33 **
0 C **
o c **
0 C **
0 C **
0 C **
35 **
32 **
34 **
***********************************************************
153
KVBll-6017-1266
-------
15 "IN, DATA
** DRY STACK GAS CONCENTRATION
**
»*
«* DATE
»****»*»»**«
** 9/10/80
* 9/10/80
** 9/10/80
«* 9/10/80
»* 9/10/80
»« 9/10/80
** 9/10/80
*« 9/10/80
«* 9/10/80
** 9/10/80
** 9/10/80
»* 9/10/80
** 9/10/80
** 9/10/80
»» 9/10/80
** 9/10/80
** 9/10/80
** 9/10/80
** 9/10/80
** 9/10/80
** 9/10/80
** 9/10/80
** 9/10/80
«* 9/10/80
*» 9/10/80
** 9/10/80
** 9/10/80
**. 9/10/80
** 9/10/80
** 9/10/80
** 9/10/80
*» 9/10/80
** 9/10/80
** 9/10/80
** 9/10/80
** 9/10/80
** 9/10/80
* 9/10/80
** 9/10/80
** 9/10/80
* 9/10/80
»* 9/10/80
** 9/10/80
*« 9/10/80
** 9/10/BO
* O/ O/ 0
** O/ O/ 0
*« O/ O/ 0
ft**********]
-
TIME
*******
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
0
0
0
*******
LOAD
MWTH
* £ ****
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
tO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
go
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
******
02
VOLX
MEAS
******* J
9.7
10.0
9.9
10.0
10.0
10.0
10.2
10.1
10.3
10.1
10.4
10.2
10.3
10.2
10.2
9.9
10B6
10e7
10.7
11.2
It. 2
11.1
11.0
11.0
10.9
10.5
1007
11.1
11.1
10.9
11.0
10.8
10.8
10.9
10.7
10.7
10.5
10.3
10.4
10.4
10.4
10.6
10.4
10.6
10..B
.0
.0
C02
VOLX
MEAS
t******l
6.0
5.7
5.9
5.6
5.7
5.6
5.7
5.6
5.6
5.5
5.4
5.5
5,5
5.5
5.7
5.8
5.4
5.2
5.2
4.8
4.8
5.0
5.0
5.0
5.3
5.6
5.5
5.2
5.3
5.4
5.3
5.4
5.5
5.3
5.5
5.3
5.7
5.7
5.6
5.7
5.7
5.7
5.9
5.S
5.4
.0
.0
CO
PPMV
MEAS
fr******4
17
14
14
23
1
0
54
0
39
32
39
16
33
3
58
5
35
21
19
15
15
14
14
14
42
41
34
31
16
31
22
35
37
34
11
12
23
21
0
51
24
0
40
33
10
0
0
.0 .0 0
NO
PPMV
MEAS
^ * * ft * *
41
40
39
39
39
37
38
37
37
37
36
37
36
36
37
38
35
35
36
32
33
34
34
33
33
35
35
33
34
35
33
35
35
34
35
34
37
37
36
37
37
36
37
37
35
0
0
0
CO
PPMV
3*02
*********
27
22
22
37
i
0
90
0
65
53
66
26
55
97
8
60
36
33
27
27
25
25
25
75
70
59
56
29
55
39
62
65
60
19
21
39
35
0
86
40
0
75
57
17
0
0
0
*********
NO
PPMV
3X02
*******
65
65
63
64
64
60
63
61
62
61
61
61
60
60
61
61
60
61
63
59
60
62
61
59
59
60
61
60
62
62
59
62
62
60
6]
59
63
62
61
63
63
62
63
64
62
0
0
0
******<
CO
NG/J
******
8
7
7
12
0
0
29
0
21
17
21
8
18
1
32
2
20
12
11
9
9
8
8
8
24
23
19
18
18
13
20
21
20
6
6
13
11
0
28
(3
0
24
18
5
0
0
0
k* ** * *
NO
NG/J
*******
35
35
34
34
34
32
34
33
33
33
33
33
32
32
33
33
32
33
34
32
33
33
33
32
32
32
33
32
33
33
32
33
33
33
33
32
34
33
33
34
34
33
3«
3«
3i
0
U
0
*******
ft*
Aft
ft*
ACUUE *»»
**
ft ft
***********
«*
ft*
a*
a*
**
*a
*»
cc
Sift
ft*
**
*«
**
*
ft
ft
ft
*»
*«
ft*
ft*
»»
ft*
ft*
ft*
fi«
ft*
ft*
**
**
ft*
e*
a -a
ft*
**
**
**
**
**
*o
**
*«
« Oft
9 ft*
t «*
***********
154
KVB11-6017-1266
-------
*«
**
**
ft*
**
* DATE
AftAAAAAA A A A A4
** ox ox o
** ox ox o
** O/ O/ 0
** OX O/ 0
** OX O/ 0
** OX O/ 0
** o/ ox o
«* O/ OX 0
«* OX OX 0
** OX OX 0
«* OX OX 0
*» OX OX 0
** OX OX 0
** OX OX 0
** OX OX 0
*« OX OX 0
** OX OX 0
ft* OX OX 0
** OX OX 0
* 9X11X80
** 9X11X60
** 9/U/80
** 9/nxeo
ft* 9/11/80
** 9/11/80
** 9/ti/SO
** 9/H/80
* 9/H/80
** 9/11/80
** 9/11/80
** 9/11/60
** 9/11/80
** 9/11/80
** 9/ii/eo
** 9/11/80
** 9/H/60
** 9/11X80
** 9/11/80
** 9/11/80
** 9/U/80
** 9/11/80
** 9/U/80
** 9/11/80
** 9/11/80
** 9/11/80
** 9/11/80
»* 9/11/80
** 9/11X60
*************
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
A A A A 4
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
soo
515
530
S«5
600
615
630
6«5
700
715
730
745
800
815
830
645
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MWTH
A A A A A A '
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
«o
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
02
VOL*
MEAS
tAAAAAAfl
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
II. 3
9.4
9.8
7.0
6.«
6.2
5.6
5.0
5.9
5.9
6.2
5.9
6. I
5.9
6.«
-1.0
S.9
6.2
6.1
6.5
7.0
6.9
-1.0
8.0
8.4
8.7
-1.0
9.0
9.0
C02
vocx
MEAS
A A A A A A '
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
5.1
6.6
6.2
8.0
6.2
8.4
8.6
8.9
8.5
8,5
8.4
6.5
8.5
8.5
6.3
-1.0
8.5
8.4
6.5
8.2
7.9
8.0
-1.0
7.4
7.1
7.0
-1.0
6.6
6.5
CO
PPMV
MEAS
[ A A A A A A '
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
48
21
0
952
267
1208
1215
1314
1093
1110
955
1042
1128
987
748
-1
717
559
296
803
592
632
-1
50
13
0
-1
95
3
NO
PPMV
MEAS
r A A A A A A
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
33
39
38
44
46
46
47
47
46
46
46
46
46
46
62
-1
49
49
48
47
46
46
-I
43
4?
36
-1
42
42
***************************************
CO
PPMV
3X02
A A A A A A A
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
89
32
0
1225
329
1470
1421
1479
1304
1324
1162
1243
1364
1177
923
0
855
680
360
998
762
80S
0
69
16
0
0
It?.
4
*******
NO
PPMV
3*02
A A A A A A A'
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
61
60
61
56
56
56
54
52
54
54
56
54
55
54
76
0
58
59
58
58
59
56
0
59
60
55
0
63
63
CU
NG/J
rAAAAAAAA
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
29
10
0
40«
108
485
469
466
430
437
363
410
450
388
30«
0
282
224
119
329
251
266
0
22
6
0
0
47
1
****************
**
**
**
NO ACUDt **
NG/J **
**
*******?"
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
IWWKKWKIi
**
**
**
ft*
**
»*
ft*
**
**
»*
**
**
**
**
»*
ft*
**
**
**
33 **
32 «*
33 »*
30 **
30 **
30 »*
29 **
28 «*
29 **
29 **
30 **
29 **
30 **
29 **
41 **
0 C **
31 **
32 »*
31 **
31 **
32 «
31 **
0 C **
32 **
32 **
30 **
0 C **
3« ' **
34 **
***************
155
KVB11-6017-1266
-------
ft*
ft*
**
ft*
ft* DATE
***********
** 9/11/80
** 9/11/80
** 9/11/80
* 9/11/80
** 9/11/80
ft* 9/U/80
** 9/11/80
*» 9/11/80
9/11/80
ft* 9/11/80
** 9/11/80
** 9/11/80
* 9/11/80
** 9/11/80
** 9/11/80
** 9/11/80
*« 9/H/80
** 9/11/80
** 9/11/80
9/11/80
ft* 9/11/80
** 9/11/80
** 9/11/80
** 9/11/80
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
* O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
* O/ O/ 0
* O/ O/ 0
* O/ O/ 0
* O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
** O/ O/ 0
« O/ O/ 0
* O/ O/ 0
** O/ O/ 0
* O/ O/ 0
** O/ O/ 0
ft* O/ O/ 0
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
*******
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
LOAD
MWTH
******
.0
.0
.0
.0
.0
.0
.0
.0
«0
.0
0
.0
.0
.0
.0
.0
0
.0
.0
.0
eO
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
eo
.0
02
VOLX
MEAS
*******
9.3
"1.0
9.4
9.6
10.2
-1.0
10.3
10.5
10.2
-1.0
9.9
9.9
9.9
-1,0
10.2
10.5
10. 6
i.o
9.9
10.2
10.0
10.2
11.0
10.9
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
C02
voix
MEAS
»******<
6.3
-1.0
6.0
6.3
6.0
-1.0
5.8
5.5
5.9
i.O
6.2
6.0
-1.0
5.8
5.7
5.5
-S.O
6.0
5.7
5.4
5.4
5^3
,0
.0
.0
.0
.0
.0
,0
Io
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
CO
PPMV
MEAS
»******<
2
-1
0
0
27
-1
36
30
5
"I
0
0
8
-1
5
95
18
-I
0
1
0
5
0
1
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
NO
PPMV
MEAS
>*******
39
"I
50
4i
39
-1
40
39
41
-1
41
40
40
-1
39
40
38
-1
«6
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KVBll-6017-1266
-------
DESCRIPTIVE STATISTICS
STANDARD MEAN HOURLY MAX. MIN. RANGE
DEVIATION DEVIATION HtAN
NO 25.92 -10.10 04.65 69. 22. 16.7
02 «.28 "2.25 7.27 12.3 2.5 9.8
C02 «.32 -2.33 7.53 10.4 3.2 7.2
CO 169,70 "24.68 73.33 **** 6. *****
FIN
157 KVBll-6017-1266
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RUNlDs KVB *CCT| 6I30AA32 PROJECT! JRH
RESOURCE UNITSI TOTALS 7
SYSTEM! ?2.72«
APPLICATION! 0.000
TIME! CPU! 30,882 I/O? ieS9fe
CC/ERf I30fe68 HAITi OeOOO
CORE 8LK SECSg 7887^888 AVERAGE SIZE! 94K
IMAGES READS 19 PAGESS 59
START! 69150166 SEP 23fI9dO FIN! iOl30!S« SEP 23,1980
SYSTEM! 32R2B«eS3 A 09/10X79
158 KVB11-6017-1266
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CUSTOMER RECEIPT PAGE******
RUNlDt KVB ACCTj 01304*32 PROJECT? JRH
RESOURCE UNITS: TOTAL: 72.734
SYSTEM: 72.724
APPLICATION: 0.000
TINE: CPUl 30.4*2 I/O: 1.596
CC/ER: 13.668 WAIT: 0.000
CORE BLK SECSi 7887.818 AVERAGE SIZE: 94K
IMAGES READ: 19 PAGES: 59
START: O9:3o:«6 SEP 23,1980 FIN: iot3o:5« SEP 23,1980
SYSTEM* 32R2B-053 A 09/10/79
159 KVBll-6017-1266
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* * * INFORMATION SYSTEMS DESIGN, lNCe * S205 CORONADU OR, * SANTA CLARAo CA 95051 * C<*0&> 727*6100 « * * 1108 UO * * *
PRINTED BVt KVB
USER NAMES KVB
ACCOUNTS OUOAA32
ON SVSTEHa A
E»EC LEVELS 32R2B-OSS
DATES 99/10
CREATED BV8 KVB
FINISHED PRINTINGS 9/23/SO 108«5t22
OUEUEDs 9/25/60 JO»SO»56
CREATED! 9/23/80 09«30l«6
PART NAME! PR»OOOKVB
PART NO.8 00
FILE NAMEg 3YSSftPR«OOOKVBU>
ACTUAL PAGESI 62
INPUT DEVICE! URN
QUEUED 108 OKU
POINTED ON! OHM
W
cn
-------
TECHNICAL REPORT DATA
(Please read fnttmctions on the reverse before completing)
1. REPORT NO.
EPA-600/7-81-095b,
2.
3. RECIPIENT'S ACCESSION-NO.
4. TITLE AND SUBTITLE
Thirty-day Field Tests of Industrial Boilers: Site 6
Gas-fired Fire-tube Boiler
6. REPORT DATE
May 1981
6. PERFORMING ORGANIZATION CODE
7. AUTHORIS)
W.A. Carter and H. J. Buening
8. PERFORMING ORGANIZATION REPORT NO.
KVB11-6017-1266
9. PERFORMING ORGANIZATION NAME AND ADDRESS
KVB, Inc.
P.O. Box 19518
Irvine, California 92714
10. PROGRAM ELEMENT NO.
C9BN1B
11. CONTRACT/GRANT NO.
68-02-2645, Task 4
12. SPONSORING AGENCY NAME AND ADDRESS
EPA, Office of Research and Development
Industrial Environmental Research Laboratory
Research Triangle Park, NC 27711
13. TYPE OF REPORT AND PERIOD COVERED
Task Final: 3/79 - 3/80
14. SPONSORING AGENCY CODE
EPA/600/13
15.SUPPLEMENTARY NOTES jjERL-RTP project officer is Robert E. Hall, Mail Drop 65, 919/
541-2477. EPA-600/7-80-0852 through -085d are similar reports for Sites 1-4;
Site 5 is covered bv report "a" of this series.
16. ABSTRACT
This is a final report on a test program to evaluate the long-term effect-
iveness of combustion modifications on industrial boilers. During previous pro-
grams, short-term tests were performed on industrial boilers to determine the
effect of combustion modifications on air pollutant emissions such as NOx, SOx,
CO, HC, and particulates. The objective of this program was to determine if com-
bustion modification techniques which were effective for short-duration tests are
feasible for a longer period. The report gives results of a long-duration field test
of a 200-hp fire-tube boiler using low excess air as the NOx control technology. The
field test was conducted with the unit firing natural gas and with the normal duty
cycle. The mean NO level for the 24-day test was 29. 5 ng/J with a geometric dis-
persion of 1.05.
17.
KEY WORDS AND DOCUMENT ANALYSIS
DESCRIPTORS
b.lOENTIFIERS/OPEN ENDED TERMS
c. COSATI Field/Croup
Air Pollution
Combustion
Boilers
Nitrogen Oxides
Fossil Fuels
Natural Gas
Carbon Monoxide
Hydrocarbons
Air Pollution Control
Stationary Sources
Combustion Modification
Industrial Boilers
Low Excess Air
13 B
21B
13A
07A
21D
07B
07C
13. DISTRIBUTION STATEMENT
Release to Public
19. SECURITY C.LASS (ThisReport)
Unclassified
21. NO. OF PAGES
161
20. SECURITY CLASS (nitpage)
Unclassified
22. PRICE
EPA Form 2220-1 (»-7J)
161
-------
U.S. ENVIRONMENTAL PROTECTION AGENCY
Office of Research and Development
Center for Environmental Research Information
Cincinnati, Ohio 45268
OFFICIAL BUSINESS
PENALTY FOR PRIVATE USE. S3OO
AN EQUAL OPPORTUNITY EMPLOYER
POSTAGE AND FEES PAID
US ENVIRONMENTAL PROTECTION AGENCY
EPA-335
Publication No. EPA-600/7-81-095b
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tear off; and return to the above address.
If you do not desire to continue receiving these technical
reports, CHECK HERE O, tear off label, and return it to the
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