vvEPA
United States
Environmental Protection
Agency
Industrial Environmental Research
Laboratory
Research Triangle Park NC 27711
EPA-600/7-81-095a
May 1981
Thirty-day Field Tests
of Industrial boilers:
Site 5—Gas-fired
Low-NOx Burner
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.
-------
EPA-600/7-81-095a
May 1981
Thirty-day Field Tests
of Industrial Boilers:
Site 5—Gas-fired Low-NOx Burner
by
W.A. Carter and H.J. Buening
KVB, Inc.
P.O. Box19518
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
IT.'", ^nvironmental Protection Agon?.y
p-r::. .•:, 5, Llteary (5FL-16)
£'_,"> :]„ Dearborn Streets Boos 1670
&o,. -1L 60604
-------
ABSTRACT
This is a final report on a test program to evaluate the long-term
effectiveness of combustion, modifications on industrial boilers. During pre-
vious 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 particulates. The objective of this program was
X X
to determine whether the combustion modification techniques which were effec-
tive for short duration tests are feasible for a longer period. This report
presents results of a 30-day field test of a 24.9 MW (85,000 Ib steam/hr)
water tube boiler outfitted with low-NO burners. The 30-day test was con-
x •"
ducted with the unit firing natural gas. The mean NO emission level was
33 ng/J with a geometric dispersion of 1.12 at the high load condition.
i;L KVB11-6015-1233
-------
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 Site 5, 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 Low NO Burner/Water Tube Boiler Test Results 19
X
4.0 REFERENCES 36
APPENDIX A 37
APPENDIX B 44
APPENDIX C 62
APPENDIX D 81
APPENDIX E
97
iii KVB11-6015-1233
-------
FIGURES
Section Page
1-1 NO Emissions from Site 5 - Low NO Burner/Water Tube 4
T, -T X
Boiler
2-1 Photograph of KVB Continuous Monitor for Measuring 7
Gaseous Emissions
2-2 Schematic of Continuous Monitor Sampling and Conditioning 9
System
2-3 Typical Industrial Two-drum Steam Generator 13
2-4 New Low NO Burners Register 13
X
3-1 Excess Oxygen as a Function of Boiler Load. Low NO 21
Burner/Water Tube Boiler Natural Gas Fuel x
3-2 Format of Hourly Average Emissions Data 22
3-3 Summary of 24-Hour Average Gaseous Emissions 23
3-4 CO Emissions as a Function of Excess Oxygen - Low NO 24
Burner
3-5 CO Emissions as a Function of Excess Oxygen - Original 25
Burner
3-6 Normal Probability Plot of NO Emission Rate. Site 5 - 27
Low NO Burner/Water Tube Boiler-Natural Gas Fuel
X
3-7 Log-Probability Plot of NO Emissions for a Water Tube 28
Boiler with Low NO Burners
x
3-8 Log-Probability Plot of NO Emissions for a Water Tube 29
Boiler with Low NO Burners
X
3-9 Log-Probability Plot of NO Emissions for a Water Tube 31
Boiler with Original Burner
3-10 Log-Probability Plot of NO Emissions for a Water Tube 32
Boiler with Original Burner
iv KVBll-6015-1233
-------
TABLES
Section Page
1-1 Summary of Daily Gaseous Emissions for Natural 3
Gas-Fired-Low-NO -Burner/Watertube Boiler
X
2-1 Analytical Instrumentation 8
2-2 Schedule of Daily Events - Site 5 15
3-1 Schedule of Certification Test Events - Site 5 17
3-2 Instrument Specifications and Performance 18
3-3 Summary of Spot Comprarisons Between Boilers 1 & 3 30
3-4 Summary of Boiler Efficiency Calculations for 34
Site 5, Natural-Gas-Fired Boiler
3-5 Summary of Natural Gas Analysis of Site 5 35
v KVB11-6015-1233
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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 emis-
sions during short-duration tests are feasible for longer periods. In addit-
tion, boiler performance and reliability were monitored.
The program scope provides for 30-day field tests of a total of seven
industrial boilers with design capacities ranging from 14.65 to 73.25 MW out-
put (50,000 to 250,000 Ib steam/hr). Fuels to be burned include natural gas,
distillate oil, residual oil, and coal. This final report is for a 24.9 MW
(85,000 Ib/hr) water tube boiler outfitted with low-NO burners.
X
During the test period, continuous monitor certification tests were
performed concurrent with low NO testing. Emissions measured were NO , CO,
X X
CO- and O_. Boiler efficiency was measured several times during the program.
This is a final report on the 30-day test, documenting the test
equipment, summarizing the test data, and discussing the data measured during
the test period.
1.2 RESULTS
A water tube boiler outfitted with new low-NO burners was selected
x
for this test. This boiler was selected because the burners, which had
recently been installed, represent the latest technology in low-NO burners.
X
After selection and approval of the test site, the continuous monitor
was shipped to the test site and installed. The next task was to perform the
certification tests as outlined in Performance Specifications 2 and 3,
40 CPR 60, Appendix B. (See Appendix D.)
KVBll-6015-1233
-------
Following the monitor certification, the 30-day field test was con-
ducted. The test was performed according to "Plan for Performing Source
Evaluation Tests in Support of NSPS for Industrial Boilers." Emissions of
NO, CO, CO?, and 0? were monitored continuously. The fuel for these tests
was natural gas; therefore, particulate measurements were not made.
The results of the 30-day test are discussed in detail in Section 3.0.
A daily summary of the gaseous emissions data is presented in Table 1-1 for
the entire test period. A statistical analysis was made of the test data.
A log-probability plot of 24-hour averages is presented in Figure 1-1. This
figure presents NO emissions for boiler load greater than 11 MW (37,000 Ib
steam/hr) output. The mean value for 11 MW and greater is 33 ng/J (65 ppm)
with a geometric dispersion of 1.12.
1.3 CONCLUSIONS
Based on the results of this 30-day test, several important conclusions
can be drawn.
• Retrofitting a water- tube boiler with low-NO burners is an
X
effective NO control technology. The low-NO mode was main-
X X
tained for 30 days with a mean NO emission level of 33 ng/J
(65 ppm @ 3 percent O_, dry) with a boiler load ranging from
£
11 MW (35,000 Ib/hr) to 23 MW (79,000 Ib/hr). At loads less
than 11 MW, the mean NO emission rate was 44 ng/J (87 ppm,
§ 3% 0„, dry) with 99% of the values less than 60 ng/J.
When compared with a standard burner in an identical
boiler, reduction of 71% in the high load range and 54% in
the low load range were achieved.
• Boiler operation with the new burners presented no reliability
or functional problems during the 30-day test. The burner and
boiler controls were serviced prior to the test period.
• The continuous monitor system using an extractive sample sys-
tem provided accurate, reliable data for the entire 30-day
test period. Calibration of the instruments on a daily basis
is necessary as is maintenance on the sample system.
2 KVB11-6015-1233
-------
TABLE 1-1. SUMMARY OF DAILY GASEOUS EMISSIONS
FOR NATURAL GAS-FIRED-LOW-NOx-BURNER/WATERTUBE BOILER
*»
*•
**
**
**
*•
*»1
*«
**
ft*
**
**
**
*•
*•
*»
ft*
**
**
**
**
**
**
**
**
**
*•
• *
**
ft*
*•
**
«»
ft*
ft*
ft*
ft*
ft*
**
**
ft*
ft*
• ft
ft*
ft*
ft*
ft*
ft*
ft*
DATE
!*********
2/ 5/80
2/ 6/80
2/ 7/80
2/ 8/80
2/ 9/eo
2/10/80
2/11/79
2/12/80
2/13/80
2/14/60
2/15/80
2/16/80
2/17/80
2/18/80
2/14/80
2/20/80
2/21/80
2/22/80
2/23/80
2/24/80
2/25/80
2/26/80
2/27/80
2/28/80
2/29/80
3/ 1/80
3/ 2/80
3/ 3/80
3/ a/80
3/ 5/80
3/ 6/80
3/ 7/80
3X 8/80
3/ 9/80
3/10/60
3/11/80
3/12/80
3/13/60
3/14/60
3/15/80
3/16/60
3/17/dO
LOAD
TIME M*TH
>************<
12.0
11.2
H.3
".7
5.3
7.2
10.7
H. «
12.2
12.4
10.2
7.0
6.1
12.3
12.1
11.5
11.0
11.0
6.6
9.5
12.2
13.9
13.4
12.9
11.9
7.6
10.2
12.1
12.5
12.3
12.5
12.1
10.1
».9
12.3
13.0
11.6
13.0
U.5
».7
".0
11.6
DRY
02
VOLX
MEAS
(*»•***<
a. 3
5.4
5.3
7.2
11.7
9.3
5.6
5.0
4.4
3.9
5.3
8.8
8.0
3.8
«.3
4.5
5.0
5.3
10.9
8.2 .
4.6
4.3
«.5
4.4
5.5
8.9
7.0
4.S
4.1
4.0
4.0
4.0
6.7
7.8
«.5
4.2
4.8
4.0
5.0
8.4
7.9
4.7
24 HOUR DATA
3TACK GAS CONCENTRATION
C02
votx
MEAS
»******<
9.5
8.6
8.7
7.«
3.3
5.4
8.6
9.0
9.4
9.6
8.7
5.6
6.7
9.8
9.3
9.2
8.6
8.6
3.5
6.7
9.2
9.3
9.2
9.4
8.4
5.3
7.4
9.3
9.7
9.7
9.6
9.7
7.4
6.7
9.2
9.5
9.1
9.7
8.8
5.8
6.7
9.«
CO
PPMV
MEAS
k******<
139.
18.
19.
18.
15.
22.
30.
24.
1«5.
131.
«1.
20.
22.
216.
90.
52.
36.
33.
16.
75.
165.
129.
190.
133.
133.
16.
20.
57.
74,
107.
51.
51,
33.
22.
148.
178.
51.
166.
61.
2«.
21.
57.
NO
PPMV
MEAS
>******<
66.
63.
64.
65.
90.
0.
59.
72.
57.
50.
56.
59.
0.
0.
57.
56.
55.
55.
63.
56.
53.
59.
60.
56.
55.
59.
75.
59.
66.
59.
60.
66.
61.
66.
50.
51.
50.
58.
48.
60.
71.
"2.
CO
PPMV
3X02
!******)
150.
21.
22.
23.
30.
3«.
35.
28.
157.
138.
46.
30.
31.
226.
97.
57.
«1.
38.
29.
105.
181.
139.
208.
144.
155.
24.
25.
62.
79.
11".
54.
54.
«2.
30.
162.
191.
57.
178,
92.
35.
29.
63.
NO
PPMV
3XP2
>***»**!
72.
72.
73.
8?.
176.
0.
69.
80.
61.
52.
64.
88.
0.
0.
6?.
61.
62.
63.
113.
79.
58.
64.
66.
61.
64.
88.
97.
64.
72.
62.
63.
70.
76.
90.
55.
S5.
55.
61.
54.
86.
97.
47.
CO
N6/J
»****»»!
50.
7.
7.
8.
10.
11.
12.
9.
52.
45.
16.
10.
10.
75.
32.
19.
13.
12.
9.
35.
60.
46.
69.
47.
51.
8.
8.
21.
26.
37.
18.
18.
14.
10.
54,
63.
19.
59.
30.
11.
9.
21.
NO
NG/J
k* ** * *
39.
39.
*»o.
46.
95.
0.
37.
44.
33.
28.
35.
4».
0.
0.
33.
33.
33.
34j
61..
43.
32.
34.
36.
33.
35.
48.
53.
35.
39.
34.
3«.
38.
«1.
49.
30.
30.
30.
33.
29.
47.
53.
*•».
**
ft*
*•
«*
**
**
*****
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
• *
**
**
**
**
**
**
**
*•
*•
**
**
* *
**
**
**
**
**
**
**
**
*•
**
**
**
**
KVBll-6015-1233
-------
W
I
CT.
O
H
Ui
10
U)
U)
200
I-D 100
~oi 90
5 80
o 70
S 60
50
40
30
20
10
I I
I I
Natural Gas Firing
Load Range >11 MW
I I 1 I I t I
_L
I I t I I 1
X = 33 ng/J
g = 1.12
I I I 8
I
0.01
0.2
10 20 30 50 70 80
PERCENT LESS THAN
90
95 98 99 99.8 99.00
Figure 1-1. NO emissions from site 5 - Low NO burner/water tube boiler.
-------
Operation at steady load conditions is not usual for indus-
trial boilers. An effective NO control technology must be
X
capable of operation over fairly large and rapid load changes.
The effectiveness of the low NO burner at low load conditions
X
was less than at high load but still represents a large reduc-
tion from the standard burner design.
KVBll-6015-1233
-------
SECTION 2.0
INSTRUMENTATION AMD PROCEDURES
This section presents a description of the instrumentation used to
measure 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
183 m high (48"W x 30"D x 72"H). A photograph of the continuous monitor is
reproduced 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, CO , and O . 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 used was a Thermo Elec-
tron 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 NO molecules revert to
KVB11-6015-1233
-------
CO
NOx —
Two-pen
Chart
Recorders
Figure 2-1. Photograph of KVB continuous monitor for measuring gaseous emissions.
-------
TABLE 2-1. ANALYTICAL INSTRUMENTATION
Measurement
Emission Species Manufacturer Method Model No.
Nitrogen Oxides Thermo Electron Chemiluminescent 10A
Oxygen Sectarian Instrument Polarographic 742
Carbon Dioxide Horiba Instrument NDIR PIR-2000
Carbon Monoxide Horiba Instrument NDIR PIR-2000
KVB11-6015-1233
-------
w
I
en
o
M
Ln
I
I-1
NJ
Probe
Drop-Out
Flask
^
CJ O
7)Jm Sample
Pump
(Refri
-*—
Drier
ge rat ion
Condenser)
Operating Calibration
Instrument
Range Gases
0 0-10% 5%/0.27%
CO 0-1000 ppm 500 ppm/900 ppra
CO 0-20% 10%/17.3%
HO 0-250 ppm 12O.5 ppm/234 ppm
SeroNfcJ5pan Zero
|H 0-6 SCFH
I
°2
1
~~V^~~ Valve
Q Press
^^^ Gauge
^j. Relief
^ Valve
*&]Span Zero A] Span Zerofij Span
3 0-6 SCFH IE] 0-6 SCFHJ30-6 SCFM
Til Inlet
CO
o-
C02 NO
•^N
1 1 1 ^*
V W | Vacuum
* " Pump
Vent
Vent
Vent
Vent
Figure 2-2. Schematic of continuous monitor sampling and conditioning system.
-------
their ground state. The resulting chemiluminescence is monitored through an
optical filter by a high sensitivity photomultiplier tube, the output of
which 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 down-
stream 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 NO 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, NO molecules in the sample gas are
reduced to NO molecules, and the analyzer then reads NO . NO is obtained by
X £
the difference in readings obtained with and without the converter in
operation.
Specifications
Accuracy: 1 percent of full scale
Span drift: ± 1 percent of full scale in 24 hours
Zero drift: ± 1 ppm in 24 hours
Power requirements: 115 ± 10V, 60 Hz, 1000 watts
Response: 90 percent of full scale in 1 second (NO mode); 0.7 second
3C
(NO mode)
Output: 4 to 20 ma
Sensitivity: 0.5 ppm
Linearity: ± 1 percent of full scale
Vacuum detector operation
Range: 2.5, 10,25, 100, 250, 1000, 2500, 20,000 ppm full scale
10 K7B11-6015-1233
-------
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 NO in the flue gas, based on pre-
4* £*
vious tests (Refs. 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 dropout flask and a refriger-
ated condenser.
B. Carbon Monoxide and Carbon Dioxide—
Carbon monoxide (CO) and carbon dioxide (CO ) concentrations were
measured by Horiba Instruments PTI-2000 short-path-length nondispersive infra-
red 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 concen-
tration 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 CO» analyzer are zero to 5, zero to 10, and zero to 20 percent.
Specifications
Accuracy: 1 percent of full scale
Repeatability: ± 0.5 percent of full scale
Zero drift: ± 1 percent of full scale in 24 hours
Span drift: ± 1 percent of full scale in 24 hours
Response time: Selectable, 90 percent of full scale in 0.5, 1.2, 3,
or 5 seconds
Power requirements: 115 VAC ± 10 percent, 60 Hz
Warm up time: 30 minutes
Output: 0 to 10 MV
11 KVB11-6015-1233
-------
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 con-
tains 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 gasses, oxygen will diffuse from the sample to the cathode in the follow-
ing oxidation-reduction reaction:
Cathode reaction: O + 2H O + 4e -»• 40H
£ £*
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 percent of full scale or ± 0.05 percent O , whichever
is greater
Sensor stability: ± 1 percent of full scale per 24 hours
Response time: 90 percent in 20 seconds
Output: 0 to 10 MV
Power requirement: 120 to 110 VAC, 60 Hz
2.2 SITE 5, BOILER DESCRIPTION AND CHARACTERISTICS
The boiler at site 5 was manufactured by Babcock and Wilcox in 1950
(Figure 2-3). It is an integral water tube boiler with a rated capacity of
24.9 MW (85,000 Ib steam/hr). The air system consists of interconnected
forced-draft and induced-draft fans. Both fans operate with constant speed,
and air flow is controlled by variable dampers. The operating pressure of
the unit is 300 psig. The boiler is equipped with tubular air heater to
preheat the combustion air.
KVB11-6015-1233
-------
Partly shielded
radiant
superheater
\.Hctoir\forcetf
duct draft fan
Figure 2-3. Typical industrial two-drum steam generator.
Originally the unit was outfitted with four B&W steam-atomized oil
burners and natural gas ring burners. All four burners are in line horizon-
tally at the boiler front. The spacing is 31.5 inches (80 cm).
Recently the four original B&W burners were replaced by four newly
designed low-NO burners capable of firing natural gas. (Figure 2-4).
X
2-4.)
Air
I
t
Figure 2-4. New low NOx burners air register.
Gas Inlet
KVBll-6015-1233
13
-------
Figure 2-4 shows the low-NO burner air register adjusted for gas
X
firing. In this case all the air flow is directed down the small 9.6-inch-
diameter duct surrounding the gas tube. The gas is injected radially outward
into the annular air stream, forming a conically shaped flame.
The boiler is installed in the power plant of a large industrial firm.
Three boilers supply process steam to the plant. The steam demand varies
over a large range, and changes in steam demand can be quite rapid.
2.3 DAILY TEST ACTIVITY
This section describes the daily test activity at Site 5 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 contin-
uously recorded on strip chart recorders and an automatic data logger. Gas-
eous data were recorded hourly by a technician. Boiler control room data
(steam flow, air flow, pressures, temperatures) were also recorded hourly
during the eight-hour shift. The automatic data logger provided hourly
averages of the gaseous emissions synthesized from approximately 900 measure-
ments. Each day, the previous day's gaseous emission and load data were
summarized in hourly averages in a form designed for keypunching the data on
computer cards.
Daily tasks consisted of (1) calibration and recording data, (2) con-
sultation with operating personnel to maintain low-NO operation, (3) periodic
X
maintenance of instruments and sampling system, (4) tabulation of previous
data, and (5) visual inspection and trouble shooting of the sampling system
and instrumentation console.
14 KVB11-6015-1233
-------
TABLE 2-2. SCHEDULE OF DAILY EVENTS - SITE 5
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. Summarize previous day's
emissions and operating data.
0900 Perform daily systems checkout and maintenance. Calibrate
and record gaseous emissions data. Record control room
data.
1000 Calibrate and record gaseous emissions data. Record
control room data.
1100 Calibrate and record gaseous emissions data. Record
control room data.
1200 Calibrate and record gaseous emissions data. Record
control room data.
1300 Calibrate and record gaseous emissions data. Record
control room data.
1400 Calibrate and record gaseous emissions data. Record
control room data.
1500 Calibrate and record gaseous emissions data. Record
control room 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-6015-1233
-------
SECTION 3.0
TEST RESULTS
This section summarizes the emission and efficiency data collected on
the water tube boiler equipped with new low-NO burners. The boiler was
X
tested for 42 days firing natural gas. The results presented herein summarize
the gaseous emissions data, efficiency and conclusions for the boiler operat-
ing with low-NO burners for an extended duration.
' x
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 Specifications 2 (PS2) and 3 (PS3), 40 CFR 60.
Appendix B (see Appendix D) establishes minimum performance specifications for
the NO monitoring system 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 December 11, 1979. 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.
Shown in the table are the monitor specifications extracted from PS2 and PS3.
Also included is the performance of the CO analyzer, which is not covered by
the performance specification. The CO analyzer is used to monitor combustion
conditions in the boiler since it is a very sensitive indicator of combustion
performance. Tables C-l through C-18, Appendix C, show the performance of
each of the analyzers for the certification tests.
KVB11-6015-1233
16
-------
TABLE 3-1.
SCHEDULE OF CERTIFICATION TEST EVENTS - SITE 5
Date
Time
Event
12-11-79 0900 Initial 24-hour zero and span reading.
Initial 2-hour zero and span reading.
12-11-79 1100 1st 2-hour zero and span drift point.
12-11-79 1300 2nd 2-hour zero and span drift point.
12-11-79 1500 3rd 2-hour zero and span drift point.
12-11-79 1700 4th 2-hour zero and span drift point.
12-11-79 1900 5th 2-hour zero and span drift point.
12-12-79 0900 1st 24-hour zero and calibration drift point.
Initial 2-hour zero and calibration reading.
12-12-79 1100 6th 2-hour zero and span drift point.
12-12-79 1300 7th 2-hour zero and span drift point.
12-12-79 1500 8th 2-hour zero and span drift point.
12-12-79 1700 9th 2-hour zero and span drift point.
12-13-79 0900 2nd 24-hour zero and calibration drift point.
Initial 2-hour zero and calibration reading.
12-13-79 1100 10th 2-hour zero and span drift point.
12-13-79 1300 llth 2-hour zero and span drift point.
12-13-79 1500 12th 2-hour zero and span drift point.
12-14-79 0900 3rd 24-hour zero and calibration drift point.
Initial 2-hour zero and calibration reading.
12-14-79 1100 13th 2-hour zero and span drift point.
12-14-79 1300 14th 2-hour zero and span drift point.
12-14-79 1500 15th and final 2-hour zero and span drift point.
12-15-79 0900 4th 24-hour zero and calibration drift point.
12-16-79 0900 5th 24-hour zero and calibration drift point.
12-17-79 0900 6th 24-hour zero and calibration drift point.
12-18-79 0900 7th and final 24-hour zero and calibration drift point.
2- 7-80 0945 1st set of relative accuracy samples taken.
2- 7-80 1045 2nd set of relative accuracy samples taken.
2- 7-80 1145 3rd set of relative accuracy samples taken.
2- 7-80 1245 4th set of relative accuracy samples taken.
2- 7-80 1345 5th set of relative accuracy samples taken.
2- 7-80 1445 6th set of relative accuracy samples taken.
2- 7-80 1545 7th set of relative accuracy samples taken.
2- 7-80 1645 8th set of relative accuracy samples taken.
2- 7-80 1745 9th set of relative accuracy samples taken.
3-12-80 1015 1st set of relative accuracy samples taken.
3-12-80 1115 2nd set of relative accuracy samples taken.
3-12-80 1215 3rd set of relative accuracy samples taken.
3-12-80 1315 4th set of relative accuracy samples taken.
3-12-80 1415 5th set of relative accuracy samples taken.
3-12-80 1515 6th set of relative accuracy samples taken.
3-12-80 1615 7th set of relative accuracy samples taken.
3-12-80 1715 8th set of relative accuracy samples taken.
3-12-80 1815 9th set of relative accuracy samples taken.
17
KVB11-6015-1233
-------
TABLE 3-2. INSTRUMENT SPECIFICATIONS AND PERFORMANCE
Parameter
Specifications
Performance
Thermo Electron Series 10 NO Analyzer
A
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% 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
9.02%
4.6%
1,9%
0.96%
1.57%
0.68%
1,83%
18 seconds
720 hours
Horiba Instruments Pir 2000 CO2 Analyzer
Zero drift (2-hour)
Zero drift (24-hour)
Calibration drift (2-hour)
Calibration drift (24-hour)
Response time
Operational period
£0.4% CO
<0.5% OX
<0.4% CO^
SO.5% C02
10 minutes
168-hour minimum
0.08%
0.0%
0.11%
0.18%
24 seconds
720 hours
Beckman Instruments Model 742 0 Analyzer
Zero drift (2-hour)
Zero drift (24-hour)
Calibration drift (2-hour)
Calibration drift (24-hour)
Response time
Operational period
<0.4% O
<0.5% O^
<0.4% 0
<0.5% O
10 minutes
168-hour minimum
DNA*
DNA*
0.06%
0.15%
41 seconds
720 hours
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
1.8%
0.0%
0.08%
0.0%
0.95%
1.96%
23 seconds
720 hours
*Instrument has no zero adjustment.
18
-------
The data presented in Table 3-2 show that analyzers in the continuous
monitor bettered the performance specification values for each parameter for
each instrument.
Certified calibration gases, obtained from Scott Environmental
Technology, Inc., included 50 percent and 90 percent span gases for the NO,
C0_, CO, and 0 analyzers, and a zero gas. In addition to the certified
analysis supplied by the vendor, sample flasks were taken for each calibra-
tion 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 [PDS] colorimetric)
as the standard. Nine sets of three PDS flasks were collected at one-hour
intervals at the beginning and end of the 30-day test period. At the fifteenth
day, an abbreviated series of six flasks was taken. All sample flasks were
returned to an independent laboratory for analysis. The results of the rela-
tive accuracy determination are shown in Tables C-17 and C-18 for the start
and end of the 30-day tests. Both tests showed that the NO instrument greatly
exceeded the accuracy requirements of PS2. The relative accuracy of the
Thermo Electron NO analyzer was about 10.3 percent based on the first test
series and about 7.8 percent based on the final test series. The relative
accuracy requirement published in PS2 is £ 20 percent of mean reference value.
3.2 LOW-NO BURNER/WATER TUBE BOILER TEST RESULTS
The continuous monitor system was installed by KVB personnel on
December 6, 1979 in a trailer near the boiler control room at Site 5, a water
tube boiler equpped with low-NO burners. A single unheated 9.5 MM (3/8-inch)
Ji
nylon sample line was strung from the duct downstream of the induced-draft
fan to the continuous monitor. Nine stainless steel probes were manifolded
together to provide a composite sample. No particulate measurements were
made during the natural gas firing test.
Following the monitor certification tests the boiler was taken off-
line to allow the burner manufacturer to rework the burners. Burner rework
and installation delayed the start of test until February 5, 1980. The
burner and boiler controls were serviced in this period.
19
KVB11-6015-123T
-------
The test boiler was set up for the burners to operate at 3.5 to 4 per-
cent O . The boiler load fluctuates over a wide range, and no attempt was
made to maintain a steady load. Normal operation is in the 11 to 12.5 MW
(37,500 to 43,000 Ib steam/hr) ranges. The steam load varied from 5.3 to
23.1 MW (18,000 to 79,0001b/hr) during the field test period.
The burner maintained the low O condition while operating in the mid
to high load range. At low load conditions, the excess O level would be
quite high with correspondingly high NO readings. A plot of excess oxygen as
a function of load is shown in Figure 3-1.
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
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. Figure 3-2 shows the format
for the daily hour-average gaseous emissions. Also included in the output is
the hourly-average steam load for the boiler. Twenty-four-hour averages
were then calculated from the hourly data. Figure 3-3 presents a list of
24-hour averages compiled for the entire test period.
The effect of excess oxygen on CO emission is shown in Figure 3-4.
The air register controls had been adjusted at the start of the test. The
data presented in Figure 3-4 show that the burner produces good combustion
performance above about 4 1/2% excess O_ but below that value CO emissions
show a rapid increase. Gaseous emissions data were also made on an identical
boiler adjacent to the test boiler. This unit was equipped with the original
burner. The CO emissions as a function of excess oxygen are shown in Figure
3-5 for the original burner. These data indicate that good combustion is main-
tained down to an excess O level of about 3% at which point the CO concentration
shows a sharp rise.
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 KVB11-6015-1233
-------
PERCENT O,
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A*AA**AAA«,^.J
HOURLY
DATA
DRV STACK GAS CONCENTRATION
TIME
bUftft***
too
200
300
400
500
600
700
800
900
tooo
1100
1200
1300
1400
1500
1600
1700
1800
1900
2000
2100
2200
2300
2400
LOAD
MhTH
A A * * A A i
W W ™ WW Wl
10.0
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'.7
8.2
10.0
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12.3
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13.2
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11.7
13.5
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10.5
11.1
02 C02 CO
VOLX VULX PPMV
MEAS MEAS MEAS
'*"™«**^HlA*fcfc*$<|fclKfci
3.6 9.9 16.
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7.0 7.
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Figiore 3-2. Format of hourly average emissions data.
22
KVB11-6015-1233
-------
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DATE
** I/ 5/80
** 2/ 6/80
** 2/ 7/80
** 2/ 8/80
** 2/ 9/80
•* 2/10/80
** 2/11/79
** 2/12/80
** 2/13/80
** 2/14/80
** 2/15/80
** 2/16/80
** 2/17/80
ft* 2/18/80
** 2/19/80
** 2/20/80
** 2/21/80
** 2/22/80
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** 2/26/80
** 2/27/80
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ft* 3/ 1/80
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** 3/12/80
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LOAD
TIME MWTH
**ft*ft*ft*ftftfttf
12.0
11.2
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3.9
4.3
4.5
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4.6
4.3
4.5
4.4
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4.0
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6.7
7.8
4.5
4.2
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4.7
24 HOUR DATA
STACK GAS CONCENTRATION
C02
VOLX
MEAS
ft Aft ft It • i
9.5
8.6
8.7
7.4
3.3
5.4
8.6
9.0
9.4
9.8
8.7
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6.7
9.8
9.3
9.2
8.8
8.6
3.5
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9.2
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Figure 3-3. Summary of 24-hour average gaseous emissions.
23
KVBll-6015-1233
-------
260
240
200
(N
160
80
40
Natural Gas Fuel
Boiler No. 3
Low NO Burner
I
2.0
4.0
6.0
8.0
10.0
EXCESS O (%)
12.0
Figure 3-4. CO Emissions as a function of excess oxygen -
low NO burner.
x
24
KVBll-6015-1233
-------
700
600
500
M
T3
.400
o
<#>
300
O
u
200
100
o
o
o
o
Natural Gas Fuel
Boiler No. 1
I
Original Burner
>O Q
2.0
4.0 6.0 8.0 10.0
EXCESS O (%)
Figure 3-5. CO Emissions as a function of excess oxygen
original burner.
25
KVBll-6015-1233
-------
C, F 20'9
'd d 20.9 - % 0
d
Where E = Pollutant emission rate*-ng/J~41b/million Btu)
C = NO concentration, ng/scm (Ib/scf)
F, = Stoichipmetric conversion factor, 2.43 x 10~
dscm/J (8.710 dscf/million Btu), for natural gas
O = Oxygen concentration, percent by volume, dry
d
The conversion of ppm (NO2) to ng/scm is made by multiplying by 1.912xl06.
To convert from ppm/N02 to Ib/scf, multiply by 1.19xlO~7. NO emissions are
measured as NO dry and reported as NO .
Statistical analysis of the data was performed to determine the
distribution which best characterized the data. The data were divided into
two load ranges since operation at low load resulted in high excess O and a
high NO emission rate. Figure 3-4 presents the NO emission rate plotted vs.
probability. The data do not result in a straight line, indicating that the
data are not normally distributed. The data were then plotted on log-proba-
bility coordinates to determine whether a better data fit could be obtained.
Figure 3-5 shows NO emission rate as a function of probability for the low-
NOx burner firing natural gas with the boiler load greater than 11 MW (37,500
Ib/hr). The mean emission value for this condition is 33 ng/J with a disper-
sion of 1.12. For this operation, 99 percent of the data are less than
42 ng/J. Figure 3-6 shows operation of the unit at load conditions less than
11 MW. The mean NO emission rate is 44 ng/J with a dispersion of 1.14.
Because the test boiler had already been outfitted with low NO
x
burners prior to the 30-day test, no baseline data were available for the
boiler with original burners. The test boiler is, however, one of three
identical boilers immediately adjacent to one another. A separate sample
line was run to one of the other boilers and hourly measurements of the
gaseous emissions were made. These data are tabulated in Table 3-3 along
with spot readings of the low NO burner gaseous emissions.
X
The NO emissions data were then plotted on log-probability paper for
two load ranges to compare with the low NO burner. Figure 3-9 shows a
X
26 KVBll-6015-1233
-------
50
5 40
%••»
o
a
to
30
20
10
§
S 0
en
o
M
_l 1 1 1 I 1 1 1 1 1 1 I 1 1 1 I | 1 || 1 I |_
n^~
^f<^^^
^
Q /^
/o
-
1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 II II 1
10 20 30 40 50 60 70 80 90 95 98 99
% PROBABILITY
i_i
to Figure 3-6. Normal probability plot of NO emission rate.
oj Site 5 - Low NO burner/water tube boiler- natural gas fuel.
-------
to
oo
H
H
1
O
H
Ul
I
LI I I I I I I S—I T
\100
£ 90
~ 80
§ 70
60
50
40
30
20
10
i s i—i—i—rr
TT
Natural Gas Firing
Load Range >11 MW
I I I I I I I I ' l»»l
J L
X = 33 ng/J
g = 112
-J I L_L
5 10 20 30 40 50 60 70
PERCENT LESS THAN
80 90 95 98 99
Figure 3-7. Log-probability plot of NO emissions for a water tube boiler with
low NO burners.
-------
to
I
x emissions for a water tube
boiler with low NO burners.
-------
TABLE 3-3. SUMMARY OF SPOT COMPARISONS BETWEEN BOILERS 1 & 3 - SITE 5
OJ
o
Boiler HI - Regular Burner
1980
Date
2/6
2/7
2/8
2/8
2/11
2/12
2/12
2/12
2/14
2/15
2/20
2/20
2/21
2/21
2/22
2/22
2/22
2/25
2/25
2/25
2/26
2/26
2/26
2/27
2/27
2/27
2/28
3/3
3/4
3/4
3/4
3/4
3/4
3/11
3/11
3/11
3/11
3/11
3/11
3/11
3/11
Tine
-1300
1320
—
—
1116
0719
1224
1225
1110
1046
0732
0950
0720
0914
0807
1009
1203
0814
0951
1210
0746
0907
1209
0749
1005
1206
0806
1008
0906
0936
0940
0945
0950
0907
0914
0918
0923
0929
0937
0944
0958
Sta.Flqw
x 10
33
34
—
—
23
30
26
26
35
24
30
50
40
41
48
36
32
23
48
16
12
32
20
12
26
21
22
30
47
62
70
76
55
43
52
63
74
80
40
35
30
Gas Ft.3
x 103
45
32
—
—
23
36
26
26
33
26
47
54
51
45
56
36
31
21
81
14
14
28
13
14
28
22
22
32
45
60
72
76
50
45
50
60
70
80
40
35
30
ppo
NO
126
214
—
—
134
175
164
158
149
113
161
213
157
189
208
198
175
207
225
116
100
151
103
100
181
94
148
151
222
222
213
212
216
202
205
221
207
209
1%
174
157
Percent
°2
8.1
5.6
—
—
8.2
6.0
3.2
2.8
6.0
7.3
5.2
2.3
5.4
3.9
3.7
5.1
5.3
5.1
3.7
8.1
8.1
6.6
8.4
8.3
5.5
5.0
6.8
5.3
3.4
3.1
2.6
2.4
3.2
4.3
4.2
3.8
2.7
2.3
4.6
5.2
5.8
Percent
C02
6.3
8.4
—
—
6.7
8.5
10.3
10.4
8.4
7.3
8.7
10.9
8.7
9.7
10.2
9.1
8.8
8.9
9.9
6.4
6.2
7.6
6.1
6.2
8.6
10.0
7.7
8.7
10.3
10.5
10.7
10.8
10.3
9.6
9.6
10.0
10.7
10.6
9.3
8.9
8.3
HO ppm
PPM Corrected
CO to 3% 02
10
20
—
—
9
12
526
650
20
21
23
388
"25
30
62
25
24
21
30
24
19
34
21
26
41
57
13
28
27
28
512
1000+
59
25
29
29
198
1000+
28
28
25
176
250
—
—
188
210
166
156
178
148
236
205
181
199
216
224
201
234
234
162
139
189
147
142
210
106
188
173
227*
223*
208*
205*
218*
218*
220*
231*
204*
201*
215*
255
186
00 pjw
Corrected NO
to 3% 02 ng/J
14
23
—
—
13
14
532
643
24
28
34
373
29
32
65
28
28
24
31
33
27
42
30
37
48
64
16
32
28
28
501
968+
60
27
31
30
195
963+
31
41
30
._
—
—
—
102
114
90
85
97
81
128
112
98
108
118
122
109
127
127
88
76
103
80
77
114
58
102
94
123
121
113
112
119
119
120
126
111
109
117
139
101
1980
Date
•2/6
•2/7
•2/8
2/8
2/11
2/14
2/15
2/20
2/20
2/21
2/21
2/22
2/22
2/22
2/25
2/25
2/26
2/26
2/26
2/27
2/27
2/27
2/28
3/3
3/4
Time
1300
1320
1045
1115
1110
1107
1041
0730
0946
0716
0911
0804
1006
1200
0810
1200
0743
0900
1200
0746
1000
1200
0800
1000
0900
Boiler 03 - Low NOx Burner
Load
Stm.Flow
xlO
43
46
38
38
32
42
34
45
59
40
44
52
38
30
36
48
57
82
76
54
65
45
36
47
74
Load
Gas Ft. PPM
xlO NO
46
49
38
38
35
52
34
45
65
40
48
54
37
30
34
50
62
84
80
52
62
47
34
44
72
56-58
58-61
61-69
77-91
62
48
49
50
58
48
45
59
55
59
53
56
54
59
49
54
64
67
58
64
80
Percent
°2
3.5
4.0
5.1
5.7
6.1
2.7
4.7
3.2
2.3
5.6
2.7
2.8
3.7
5.5
3.0
2.7
4.8
1.9
2.2
2.7
2.2
3.3
6.3
3.0
2.3
Percent
C02 CO
9.8
9.4
9.1
8.6
8.5
10.6
9.3
10.2
10.8
8.7
10.6
10.6
10.1
8.6
10.3
10.6
9.1
10.9
10.7
10.4
10.7
10.0
8.2
10.4
10.7
27
34
24
22
16
124
29
47
373
27
206
106
46
22
72
291
25
1000+
195
317
1000+
41
14
75
409
'Burner with steam injection. All other figures - burner w/o steam injection.
-------
(O
Co
CO
900
800
700
600
500
400
300
200
g1 100
"" 90
§ 80
70
60
50
40
30
20
10
m i i i
Natural Gas Firing
Load Range >11 MW (37,500 Ib/hr)
i i
TT
TT
x = 113 ng/J
g = 1.08
III! I I I I I I I I 1 I I ill!
.01.05.1.2 .5 1
5 10 20 30 40 50 60 70 80
PERCENT LESS THAN
90 95 98 99
I I I
99.899.9 99.99
Figure 3-9. Log-Probability plot of NO emissions for a water tube boiler with original
burner.
-------
Utt
10
Ui
I
H
K)
OJ
900
800
700
600
500
400
300
200
100
90
80
70
60
50
40
30
20
10
Z TTT
1IIII I ! I IIIITT
TT
Natural Gas Firing
Load Range <11 MW,
x = 95"ng7J
g = 1.29
T
i i I I i 5 1 I 1 a I I i t I 18 8 i
II I
.01.05.1.2 .512
10 20 30 40 50 60 70 80
PERCENT LESS THAN
90 95 98 99 99.8 99.9 99.99
Figure 3-10. Log-probability plot of NO emissions for a water tube boiler with original
burner.
-------
log-probability plot of the NO emissions for boiler steam load greater than
11 MW (37,500 Ib/hr). The mean value is 113 ng/J (209 ppm @ 3% 0 , dry)
with a geometric dispersion of 1.08. At this load range, 99% of the values
are less than 135 ng/J (250 ppm). At loads less than 11 MW, the mean value
was 95 ng/J (176 ppm) with a dispersion of 1.29. (figure 3-10).
A comparison with the low NO burner shows that at the high load
range a 71% reduction was achieved. In the low load range, a NO reduction
of 54% was achieved.
3.2.1 Boiler Efficiency
Boiler efficiency calculations were made at load levels from 8.8 MW
(30,000 Ib/hr) steam flow to 23.4 MW (80,000 Ib/hr) steam flow in 2.9 MW
(10,000 Ib/hr) increments. The ASME abbreviated efficiency test method was
used to determine the boiler efficiency. The test method is described in
Appendix A. Table 3-4 summarizes the calculated boiler efficiencies. The
data in this table show that boiler efficiency increases with load, with the
primary contribution due to dry gas losses.
The analysis of the natural gas fuel was obtained from the local gas
supplier. The results are tabulated in Table 3-5.
33 KVB11-6015-1233
-------
TABLE 3-4. SUMMARY OF BOILER EFFICIENCY CALCULATIONS FOR SITE 5, NATURAL-GAS-FIRED BOILER
§
H
H
1
O
U1
H
(0
US
W
Date
Test Load
103 Ib/hr
MOTH
Percent of capacity
Stack O2, percent
Stack CO, ppm
Stack temperature (K/°F)
Ambient temperature (K/ F)
Boiler Heat Losses
Dry gas
Moisture in fuel
Moisture from H
Combustibles in refuse
Radiation
Total losses
Boiler efficiency, percent
2-12-80
30
8.8
35
4.9
13
398/257
288/59
4.36
0
10.47
0
1.40
16.23
83.77
2-12-80
40
11.7
47
5.6
56
408/274
296/74
4.85
0
10.42
0
1.10
16.37
83.63
2-21-80
50
14.7
59
2.4
676
401/262
286/55
3.98
0
10.55
0
.9
15.43
84.57
2-8-80
60
17.6
71
3.0
53
408/274
289/61
4.24
0
10.53
0
.8
15.57
84.43
2-29-80
70
20.5
82
2.1
1000
416/290
286/56
4.42
0
10.64
0
.6
15.66
84.34
2-26-80
80
23.4
94
1.9
100
391/245
294/70
3.3
0
10.33
0
.55
14.18
85.82
-------
TABLE 3-5. SUMMARY OF NATURAL GAS ANALYSIS OF SITE 5
Gas Analysis
Constituents
Oxygen
Nitrogen
Carbon Dioxide
Methane
Ethane
Propane
Iso-Butane
N-Butane
Iso-Pentane
N-Pentane
C, + Residuals
o
BTU
Specific Gravity
Results in
Mole %
0.00
1.47
0.66
93.18
3.55
0.84
0.08
0.13
0.03
0.03
0.03
1041
0.600
35
KVB11-6015-1233
-------
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.
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.
36 KVB11-6015-1233
-------
APPENDIX A
EFFICIENCY MEASUREMENTS
37 KVBll-6015-1233
-------
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 O 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
38 KVB11-6015-1233
-------
HEAT IN FUEL (H,) (CHEMICAL)
LIT
ENVELOPE, '
^A MEAT IN ENTERING AIR
Z HEAT IN ATOMIZING STEAM
^ B| SENSIBLE HEAT IN FUEL
BX PULVERIZER OR CRUSHER POWER
BX BOILER CIRCULATING PUMP POWER
BX PRIMARY AIR FAN POWER
BX RECIRCULATING GAS FAN POWER
B«A MEAT SUPPLIED BY MOISTURE
IN ENTERING AIR
— B, HEAT IN COOLING WATER
LOSSES (L)
CREDITS (B;
BOUNDARY * —
c ^
L
c
I s
••••••••••-T
HEAT IN PRIMARY STEAM
HEAT IN DESUPERHEATER 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
•* HEAT IN REHEAT STEAM IN
Luc
UNBURNED CARBON IN REFUSE
LC HE AT IN DRY GAS
Li»l MOISTURE IN FUEL
LH
, I-.*
MOISTURE FROM BURNING HYDROGEN
MOISTURE IN AIR
L Z HEAT IN ATOMIZING STEAM
Lco
UH
* UHC
CARBON MONOXIDE
UNBURNED HYDROGEN
UNBURNED HYDROCARBONS
3 RADIATION AND CONVECTION
L- RADIATION TO ASH PIT, SENSIBLE HEAT IN
^ SLAG & LATENT HEAT OF FUSION OF SLAG
^ i SENSIBLE HEAT IN FLUE DUST
L,
HEAT IN PULVERIZER REJECTS
r I-. MEAT IN COOLING WATER
L« SOOT BLOWING
OUTPUT a INPUT - LOSSES
DEFINITION: EFFICIENCY (PERCENT) = r, (ft) = fiUIZUI « 100
S IN" u I H
x 100
* 100
HEAT BALANCE: Hf + B = OUTPUT + L OR ^ (%} = I | _ fj-^
Figure A-l. Heat balance of steam generator
39
KVB11-6015-1233
-------
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.
40 KVB11-6015-1233
-------
SUMMARY SHEET
TABLE A-l
A.SME TEST FORM
FOR ABBREVIATED EFFICIENCY TEST
PTC 4. l-o (1964'
OWNER OF PLANT
TEST CONDUCTED BY
BOILER MAKE i TYPE
TEST NO.
LOCATION
OBJECTIVE OF TEST
BOILER NO.
RATED CAPACITY
DATE
DURATION
STOKER TYPE I SIZE
PULVERIZER. TYPE » SIZE
FUEL (BED MINE
COUNTY
BURNER, TYPE &
SIZE
STATE SIZE AS FIRED
PRESSURES t TEMPERATURES
FUEL DATA
1
2
3
4
5
6
7
t
9
10
11
12
13
U
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 KBOILER)
STEAM OUALITY'.MOISTURE OR P. P.M.
AIR TEMP AROUND BOILER (AMBIENT)
TEMP AIR FOR COMBUSTION
TEMPERATURE OF FUEL
CAS TEMP. LEAVING (Boiler) (Eeon.l (Air Hti.)
GAS TEMP. ENTERING AH (II condition! 19 be
PIIO
pne
P«IO
psia
F
F '
F
F
F
F
F
F
F
UNIT QUANTITIES
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
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 LBOF STEAM (ITEM 16-ITEM I?)
HEAT A8S/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
HOURLY QUANTITIES
ACTUAL WATER EVAPORATED
REHEAT STEAM FLOW
RATE OF FUEL FIRING (AS FIRED .1)
TOTiL HPAT IklPMT (Item 28 X lt,m 41)
1000
HEAT OUTPUT IN BLOW.00WN WATER
M?I*L d«» J6.lt.mJO)«(lt.»27.ll.m2n»lt«m 30
OUTPUT 1000
3iu/lb
Biu/lb
Btu/lb
Btu/lb
Btu'lb
Blu 'Ib
3lu/lb
Ib/lb
Blu/lb
Ib/lb
Ib/lb
Ib/hi
Ib/hr
Ib/hr
kBAr
kB/hr
kB/nr
FLUE CAS ANAL. (BOILER) (ECON) (AIR HTR) OUTLET
CO,
o,
CO
N, (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 FIREO
ULTIMATE ANALYSIS
43
44
45
46
47
40
37
CARBON
HYDROGEN
OXYGEN
NITROGEN
SULPHUR
ASH
MOISTURE
TOTAC
COAL PULVERIZATION
48
49
50
64
GRINDABILITY
INDEX-
FINENESS HTHRU
SOU-
FINENESS S THRU
200 M-
INPUT.OUTPUT
EFFICIENCY OF UNIT%
51
52
53
44
41
OIL
FLASH
Sp. Gre
POINT f
-iiy Deg.API*
VISCOSITY AT SSU'
BURNER SSF
TOTAL HYDROGEN
% .1
Btu pe.
Ib
CAS
54
55
56
57
58
59
60
61
CO
CH4 METHANE
C,H, ACETYLENE
C,H« ETHYLENE
C,H,
ETHANE
H,S
CO,
H,
HYDROGEN
TOTAL
62
63
41
TOTAL HYDROGEN
7. wt
r.voL
DENSITY 68 F
ATM. PRESS.
Btu PER CU FT
Biu PER LB
ITEM 31
• 100
ITEM 29
HEAT LOSS EFFICIENCY
65
66
67
61
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 OFH,
HEAT LOSS DUE TO COMBUST. IN REFUSE
HEAT LOSS DUE TO RADIATION
UNMEASURED LOSSES
TOTAL
Blu/lb
A.F. FUEL
EFFICIENCY > (100 - l»". 71)
Kef A.
FUEL
'Net Requited lot Efficiency Telling
t Fer Peini ef M.eeu.emenl See P.r. 7.M.1.PTC 4.1-1964
41
KVB11-6015-1233
-------
CALCULATION SHEET
FOR
TABLE A-2
ASME TEST FORM
ABBREVIATED EFFICIENCY
TEST
PTC 4.1-b (1964)
Revised September, 7965
OWNER OF PLANT TEST NO.
30
54
35
36
65
66
67
M
69
70
71
72
HEAT OUTPUT IN BOILER BLOW.DOWN WATER *LB OF WATER BLOW.DOWN PER HR
If impractical to weigh re/use, ihii
item con be estimated as follows
FRY REFU-E PEH LB Or A" CIUCD fUCL * **" '" ** """ C°*L
100 -ft COMB. IN REFUSE SAMPLE
ITEM 43 pTEM22 ITEM 23 ~j
CARBON BURNED 1 I
FUEL '°° L U>50° J
DRY CAS PER LB 11CO, « 10, « 7(N, « CO)
BURNED 3(C°> 4 C0) / \
ITEM 32 ITEM 33 ( ITEM 35 ITEM 34 1
11 X « i x *7\ * /
/ITEM 32 ITEM 34 \
3 n 1. * I
V /
EXCESS °J - — ITEM 33 - "I" *
.26B2N, - (0. . CO ,
2 •**** - rat •»«uii*4, KM ABMA ~
^ Uiwt llswd ifi PTC 4.1
i« V.2 - PTC 4.1-19*4
i» O»rt, Fif *. PTC 4.1-1964
mutually
42
KVB11-6015-1233
-------
FIGURE A-2
HP-67 KEYED CALCULATIOH SHEW
ASME ABBREVIATED EFFICIENCY CALCULATION - HEAT LOSS METHOD
Test No.
Date
Location
Unit No.
Fuel
(Turn Calculator Off and Then On. Load Program Card.)
A. FKOM FUEL ANALYSIS:
Wt. % in as-fired fuels C
%. Moisture
Al:(STO 0)
High heating value of fuel as-fired
\. H
%. S
B. FROM FLUE GAS ANALYSIS:
Volume % in flue gas of: O,
AS:(STO 4)
%. CO,
A2:(ST01) A3:(STO 2) A4:(STO3)
Btu/lb
\, CO
Bl:(STO 5)
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 8)
C2. Heating value of dry refuse (weighted average) Btu/lb dry refuse
C3. Wt. % of combustibles in refuse
(STO 9)
(f P ^ S) (STO 4) (f P $ S)
D. MEASURED TEMPERATURES
Dl. Gas temp, leaving boiler, econ. or air heater
D2. Comb, air temp.
E. FROM STEAM TABLES:
El. Enthalpy: H20(g) at temp. Dl t 1 psia
E2. Enthalpy: H 0(1) at conb. air temp.
(STO A)
(STO B)
(STO C)
Btu/lb
(STO D)
Btu/lb
F. FROM AK'IA STANDARD RADIATION LOSS CHART (UNLESS MEASURED):
Fl. Heat loss due to radiation % of gross heat input
(STO E)
G. FROM tr.:iT SPECIFICATIONS (if available, otherwise enter 0):
Gl. Unmeasured losses
(f P ^ S) (STO 0) (f P $ S)
% of gross heat input
1. Excess Air
100 (2E1 - S3)
0.5364(100 - Bl - B2) - (2B1 - B3)
2. (Optional) Pounds dry gas per pound of fuel »
(A)
Bl + 4B2 * 700 I Al Cl x C2
3(B2 + B3) 1100 " 14500
100
3A4
800 I
Heat Losses
24 x Eg.2 x (Dl - D2)
3. Due to dry gas « jg
4. Due to moisture in fuel -
A2 x (El - E2)
AS
5. Due to H^O from combustion of H2
6. Due to combustibles in refuse «
-
-
(R/S)
Ibs dry gas/lb as-fired fuel
% of Cross (Optional)
Heat Input Btu/lb as-fired fuel*
(E)
7. Total Losses - Sum of calculated losses + Fl + Cl (f a)_
8. Efficiency - 100 - Total Losses (f b)_
(R/S)
(R/S).
(R/S)
•Calculated as percent of gross heat input x AS * 100
43
KVBll-6015-1233
KVB 6015-21 (Rev 1)
11/7/78
-------
APPENDIX B
DATA RECORDING FORMATS
44 KVBll-6015-1233
-------
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 (0 ) 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. Opacity, particulate loading, and POM concen-
tration are measured at the sampling port and the measurements recorded on
data sheets.
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
45
KVB11-6015-1233
-------
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
46
KVBll-6015-1233
-------
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.,0
Over fire air, in. H.,0
Boiler exit, in. H^O
Economizer exit, in. HJD
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
47
(continued)
Data Sheet 6017-26
12/12/78
KVBll-6015-1233
-------
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:
48
Data Sheet 6017-26
12/12/78
KVBll-6015-1233
-------
Figure B-2.
KVB, INC.
GASEOUS EMISSIONS DATA
Date_
Engr.
Low NO Control Method
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% O., (ppm)
10. N02 (hot)
read/3% Om (ppm)
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 (%)
49
Data Sheet
6015-23
9/29/78
KVBll-6015-1233
-------
Figure B-3.
HP-67 Keyed Calculation Sheet
NOZZ1£ SIZE, O and AH CALCULATIONS
Test No.
Unit Ho.
Crew: Enor.
Date
Fuel
Location
Sampling Method
Techs .
DATA
Constants
Pi tot Factor, Fs
Orifice Factor, J
Orifice Dian. . D (in.)
Ideal Meter Flow? Q (ACFM)
n
NOTE: TO RECALCULATE IDEAL
RESTORE DATA IN REGISTERS 4
STACK AND RE-ENTER % HO, %
IDEAL HOZZLE CALCULATION
(A) Ideal Nozzle Size, D .
n i
METER FLOW RATE AND ORIFICE
Key
(STO
(STO
(STO
(STO
NOZZLE SIZE,
THRU 8, CLEAR
02, and % C02
Ideal)
Actual Conditions
1) Meter Temperature, Tm(*F)
2) Barom. Press., PBar (in. Hg)
3) Static Press. Diff.. APg (iwg)
4) Nozzle Temp. , Tn (*F)
Stack Vel. Press., Ap (iwg)
Caseous Stack Composition
% HjO (%)
% 0? dry (%)
% CO, dry (%)
inches
Key
(STO 5)
(STO 6)
(STO 7)
(STO 8)
(STO 9)
ENTER
ENTER
PRESS. DIFF. CALCULATIONS
Actual Nozzle Size. Dn(Actual)
(C) Actual Meter Flow Rate, ^|Actuml)
(RCL 7) Orifice Press. Diff., AH to obtain
inches
ACFM (on meter)
0 iwa
*•> f»^.»-i-i»i i ______ '
NOTE: To Determine On and AH for Other Actual Nozzle Size, Key in Dn(Actuajj, Press C for Q_» then RCL 7
_ for AH. __ __________________
For one Dn(Actual) witn Changing Stack Velocity Pressure (Ap) and Nozzle Temperature (Tn)
(It is not necessary to restore data in registers 4-8 for these calculations)
Ap (ENTER)
(iwg)
Tn
I'D
(E)
(ACFM)
(R/S) AH'
(iwg)
EQUATIONS
(l) «a - i/as c« % co2 * % o2»
/ \
15)
V '
, .1.) (2) ii. - «d (* "fioo * «» V" cu>/lb
• ».* P^, * ». <1«. of mt«r) («|) VB . 1M92 f§ f (Ap " '
(f_ » 460) (11.6 »I-r * AHj.j)
1 • 1,11 nhir* n - nwtar of tt«r»ttoM to obuin ,
o.ooi
(9) _, . '-"-' "«"
* ' * MM7S «Vo_4 (T_ »
11.6
460) - 76*
(in. of vitar)
50
KVBll-6015-1233
KVB 6015-2S (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
Analyzer Span Setting
1
Upscale 2
3
Average
1
Downscale 2
3
Average
System average response time
PPm
ppm
seconds
seconds
seconds
upscale response seconds
seconds
seconds
seconds
downscale response seconds.
(slower time) = seconds.
% deviation from slower _ [average upscale minus average downscale] „„„„
system average response 1
slower time 1 —
51 7/1/77
Data Sheet 6017-35
40CFR60/App. B
KVBll-6015-1233
-------
Figure B-5.
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (24-HOUR)
Date Zero Span Calibration
and Zero Drift Reading Drift
Time Reading (AZero) (After Zero Adjustment) (ASpan)
Zero Drift * [Mean Zero Drift* + C.I. (Zero)
•5- I Instrument Span] x 100 » .
Calibration Drift - [Mean Span Drift* + C.I. (Span)
T [Instrument Span] x 100 = .
*Absolute Value
Data Sheet 6017-34
40CFR60/App. B
7/1/77
52 KVBll-6015-1233
-------
Ln
o
M
Ul
M
K)
u>
W
Data
Set
No.
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)
J * [Span] x 100 =
+ CI (Span)
J T [Span] x 100
^
H-
iQ
C
CD
W
cn
CD
Data Sheet 6017
40CFR60/App. B
7/1/77
-33
-------
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)
N0x
Sample 3
(ppm)
-
NO Sample
Average
(ppm)
Mean reference method
test value fNO )
95* Confidence intervals = + ppm
Accurac
* Exple
.j Mean of the differences + 95%
X
-------
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 Difference + C.I. „__
Calibration error = Average calibration Gas Concentration x 10° %
Calibration gas concentration - measurement system reading
«s
Absolute value
Data Sheet 6017-31
40CFR60/App. B
7/1/77
55 KVBll-6015-1233
-------
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
56 40CFR60/App. B
7/1/77
KVBll-6015-1233
-------
Figure B-10.
Test No._
Box No.
Test Description
PARTICU1ATE CALCULATION SHEET
Test Crew
Date
Location
Sample Probe Position
Dry Gas Meter Vol. (
Final
Initial
Total
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 Wt
Final 650-Tare
ft")
Probe
(Acetone)
Final
Initial
A Vol
Probe
(Water)
Impinger
1 2
Cyclone
(Acetone)
Water V<
3
Flask
(Dry)
3l .(ml)
S. Gel
Filter
No.
Potal
Blank
No.
'
Comments:
Data Sheet 6002-3
57
KVB11-6015-1233
-------
Figure B-ll.
Location
K VB. INC.
STACK DATA
Unit No.
Test No.
Engr. '
Fuel
Load
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
%
OF
in.
in.Hg
J
diam.
Ps
iwg
Stack Gas Pressure,
Abs. Stack Press., AP=P +407= iwga
Stack Gas Sp. Gravity, 5s n.d.
Stack Area, As ft2
Remarks
Final Meters
Initial Meter:
Time
Total
Avg.
Vm
Meter
Volume
Heading
(CF)
Vacuum
Gage
Reading
(iwg)
fcP
Pitot
Tube
Pressun
(iwg)
H
Orfice
Pressurt
; Diff
(°F)
Stack
Temp.
(°F)
°F
°F
+ 460
Impinger
Temperature
Out
(°F)
In
(°F)
Filter
Box
Temp.
(°F)
Meter
Temp.
(°F)
58
KVBll-6015-1233
11/20/75
-------
Figure B-12.
Test No. Date_
•nit No. Fuel_
.83
HP-67 KEYED CALCULATION SHEET*
PARTICULATE EMISSION CALCULATIONS
Location
Engr.
Sampling Train and Method
Pitot Factor, Fs
Barometric Pressure, P
bar-
Tot. Liquid Collected, V
Velocity Head, AP_
(STO 0)
ml Total Particulate, M
n (STO 2)
(STO 1.)
iwg Stack Temp., Ts
. Hg
m gm
TSTO
(STO 4}
°F stack Area, As
ft
(STO 5)
Sample Volume, Vm_
(STO 6)
Orifice Press. Diff., H
Stack Press., Psg
JLwg Excess 0 , XO %_
Sample Time, 6_
(STO
min Nozzle Dia., Dn
(STO 7) * * (STO 8)
_iwg,(Flue Gas Density/Air Density)© Ts, Gs n.d.
(STO A)
(STO B)
(STO C)
in. Meter Temp., T
m-
(STOD)
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 . . » 0.0334 Vm(P, + H/13.6)
sta bar
2. Water Vapor
Vw
0.0474 V,
std lc
3. Moisture Content Bwo « Eq. 2/(Eq. 1 + Eq. 2)
std
std
3
4. Concentration a. C = 0.0154 Mn/Vm
b. C = 2.205 x 10"6 Mn/Vm
c. C = Eq. 4b x 16.018 x 10
5. Abs. Stack Press. Ps
6. Stack Gas Speed Vs = 174 Fs /APTs
P. x 13.6 + Psg
oar
7. Stack Gas Flow a. Qsw = Eq. 6 x As x
Rate @ 70°F
530
1.00
Gs
Ps
Ts 407
b. Qsd - Eq. 7a x (1. - Eq. 3)
8. Material Flow
9. XO2 factor
10. Emission
11. % Isokinetic
Ms
Eq. 7b x Eq. 4b x 60
XO f - 2090/(20.9 - XO %)
a. E - Eq. 4b x Fe x Eq. 9
b. E - Eq. 4c x Fm x Eq. 9 X 1000
14077 x Ts(Vm
^,
std
Vw
.,
std
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(°R) if meter not temperature compensated.
3) F = 2.684 x 10"5 x Fe
SCF
SCF
N.D.
grains/DSCF
Ib/DSCF
grams/DSCM
in. w abs.
ft/min
WSCF/min
DSCF/min
Ib/hr
N.D.
Ib/MMBtu
ng/joule
Data sheet 6002-4
Revised 9/27/78
KVBll-6015-1233
-------
Figure B-13.
- ojeets
bate:
KVB, Inc.
VELOCITY TRAVERSE
Test Description:_
Location:_
Unit:
Test:
Fuel:
Stack Cross Section
Personnel:
Barometric Press, (in. Hg):
Absolute Static Press, in Stack (in. Hg):.
Pitot Tube Coefficient:
<*•>
(Cp)
85.48
1/2
Time
Traverse Point
Port Depth
Velocity
Head
(in. H20)
AP
Gas Temp.
CF)
Gas Temp.
(°R)
TS
Molecular
Wt.
MS
Velocity
(ft/sec)
vs
02
Cone.
(% Dry)
60
Data Sheet KVB 6002-13 KVBll-6015-1233
-------
Figure B-14.
Test No
Fuel
(f ) (CL
(C)
(R/S)
(R/S)
(R/S)
(R/S)
(R/S)
(R/S)
(f) (A)
(R/S)
(R/S)
(R/S)
(R/S)
(R/S)
(R/S)
(R/S)
lecimal
.) (2) (E)
.
REG)
1
2
3
4
5
6
7
8
9
(
(
10
11
12
13
14
IS
16
pt.
17
KVB
Date Location Unit No.
Fuel Sample Ho. Fuel Sample Point
LIQUID OR SOLID FUEL CALCULATIONS
, (f) (Pjs) , IS ) (CL REG), Load data card, then PGRM card (both tides)
•Input HHV (Btu/lb) (A)
•Input wt C (R/S)
•Input wt H (R/S)
•Input wt S (R/S)
•Input wt O (R/S)
•Input wt N • (R/S) - decimal point blinks after
pressing; item tl displayed
Dry stoichiometric moles flue gas/lb fuel •
(One may proceed to items 9, 17, or 18 by pressing (f ) (A) , (E) , or
entering MW and pressing (B) , respectively.)
•Input wt t HjO in fuel (0 if none)
. Moles H,O in flue gas/lb fuel
. Total moles of flue gas (stoichiometric )/lb fuel
Dry volume/wet volume
Volume % H,O in flue gas
Volume % CO,, dry in flue gas
SO, (ppm by vol.), dry at stoichiometric
NO (ppm by vol.), dry at stoichiometric
Stoichiometric air/fuel ratio (Ib air/lb fuel)
Before items 10-16 may be determined, items 1-9 must be completed.)
D) - 20.95 displayed
•Input measured vol. % 0; for O., correction
Gas moles at % 02 _ 20.95
Gas moles, stoic. 20.95 - % Oj
Dry moles flue gas/lb fuel at % Oj
. Vol. % C02, dry at % 02
SO- (ppm by vol . ) dry at % O,
NO (ppm by vol . ) dry at % 0.
. Vol. % HjO at % 02
Percent Excess Air
blinks)
Converts item 1 to SCF dry flue gas at stoich/10 Btu «
Item 18.
•Input MW, (B), program calculates K (lb/10 Btu
(MW « 46 for NOx, CO - 28, HC « 16, SOx - 64)
ppm/K)
1.
2.
3.
•Input measured ppm at 3% O,, dry, (R/S), program calculates lb/10
* £
(Optional) No input, (R/S), program converts lb/10 Btu •> ng/J
Repeat steps (1) and (2) as necessary.
Btu.
b.
•Enter next value of MW, complete step
(3). Repeat for all species desired.
NOx
CO
HC
SOx
MW
46
28
16
64
(a) followed by steps (1), (2), and
K for lb/10° Btu
•Indicates input is required
61
Data Sheet 6015-19
Revised 7/6/78
KVBll-6015-1233
-------
APPENDIX C
CONTINUOUS MONITOR CERTIFICATION DATA SHEETS
62 KVBll-6015-1233
-------
MONITOR PERFORMANCE TEST DATA SHEET
ACCURACY DETERMINATION (NO )
X
EngineerdS&'tst
Test
No.
1
2
3
4
5
6
7
8
9
i
Date
and
Time
<2-7-&0
9>*JT
<3 ' 7'&&
/0t*j-
f" 7~g0
//:4f
£~7-&0
&f*jT
<* - 7'-
I-- "•• • — — • 1
Reference Method Samples
NO
X
Sample 1
»W8T?^
49
^
?/
££
44
63~
60
£7
££
NO
X
Sample 2
9 jiPiP^
//
74
73
£
6?
73
7/
N0x
Sample 3
&J&& *,*
£6
77
Z2
69
4S"
67
60
?e
S£
NO Sample
Average
G>jJn%\j*>~
6/-f
Mean of
the dif
& J%, 0* sJ'2-
-4
-I/
-42
-7
+ *t
->3
^v5""
•f 4
i
-------
MONITOR PERFORMANCE TEST DATA SHEET
ACCURACY DETERMINATION (NO )
Engineer
(Ti
J^
3
w
H
H
cn
o
H
Ln
1
M
NJ
W
OJ
Test
No.
1
2
3
4
5
6
7
8
9
Date
and
Time
3~'2-&0
/?-£<=>
/3f/S-
3 -;<=>-&&
/4n/S~
3-J2- £0
tfttf
3-'2-&jJ?S£**+
JZ
^
^x7
6 • 3(0 ppm
Accura<
* Expl
Mean of the differences + 95%
NO
X
Sample 3
&jiffis$. eSsf
<£/
£jT
-r«fWk
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
RESPONSE TIME FOR CONTINUOUS INSTRUMENTS
/•
r
Date of Test
-? ' ">/
Span Gas Concentration
Analyzer Span Setting /£>. & pjpar
seconds
Upscale 2 seconds
3 7£ seconds
Average upscale response fy/. 3 seconds
seconds
Dovmscale 2 4V seconds
3 * seconds
Average downscale response 3&& seconds
System average response time (slower time) = fy/.3 _ seconds.
% deviation from slower _ faverage upscale minus average downscale j
= I _ ; . I X J-OvJ*
system average response 1 slower time
j
I
I
Data Sheet 6017-35
65 40CFR60/App. B
7/1/77
KVBll-6015-1233
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
<
RESPONSE TIME FOR CONTINUOUS INSTRUMENTS
,t .-,/,»
Date of Test — / ? ~
Span Gas Concentration
Analyzer Span Setting
1
3
Average
Downscale 2
3
Average
System average response time
/?>£ ppttf ^
seconds
/«? seconds
// seconds
upscale response // 7 seconds
^ y seconds
i?,^ seconds
^^ seconds
downscale response c?^. "7 seconds.
(slower time) = c?S. 7 seconds.
% deviation from slower _ [average upscale minus average downscale | , „„„ _ ,-^ x
system average response 1
slower time 1 —
66
Data Sheet 6017-35
40CFR60/App. B
7/1/77
KVBll-6015-1233
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
V
RESPONSE TIME FOR CONTINUOUS INSTRUMENTS
Date of Test
£ O
Span Gas Concentration c?3 fy ppm
Analyzer Span Setting
seconds
Upscale
2 /~?
3 ^7
seconds
seconds
Average upscale response /£ seconds
seconds
Downs cale
2
3
seconds
seconds
Average downscale response
seconds.
System average response time (slower time)
seconds.
% deviation from slower _ average upscale minus average downscale
system average response
slower time
cale [
J
\r\e\* -
~
67
Data Sheet 6017-35
40CFR60/App. B
7/1/77
KVBll-6015-1233
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
-------
KVB
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (24-HOUR)
Engineer
Date Zero Span Calibration
and Zero Drift Reading Drift
Time Reading (AZero) (After Zero Adjustment) (Aspan)
""'
-------
KVB
Engineer //,
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (24-HOUR)
Date Zero Span
and Zero Drift Reading
Time Reading (AZero) (After Zero Adjustment)
Calibration
Drift
(ASpan)
*>££* & —
/«?-/«?•*? & ^ /7.7 -.4
'./.''• 7f & & J7,<3
y./
te'/g'W & o /?.9 1,1
Zero Drift = [Mean Zero Drift* & + C.I. (Zero)
-------
KVB
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (24-HOUR)
Engineer
Date
and
Time
Zero Span
Zero Drift Reading
Reading (AZero) (After Zero Adjustment)
Calibration
Drift
(ASpan)
/„-?•//• 7'f __ _
&-/?'?i>, x-;
's7 13 C.^ 7 &
te-WF i2 13 £3I
Zero Drift
Calibration
- [Mean Zero Drift* &.S7 + C.I. (Zero) *-?-&£~ ]
•»• [Instrument Span] x 100 * /<£*7 ~/.
Drift « [Mean Span Drift* /<^ * C.I. (Span) £
T [Instrument Span] x 100 = /'££•? . •
'Absolute Value
71
Data Sheet 6017-34
40CFR60/App. B
7//1/77 KVBll-6015-1233
-------
KVB
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (24-HOUR)
Engineer
Date Zero
and Zero Drift
Time Reading (AZero)
Span Calibration
Reading Drift
(After Zero Adjustment) (ASpan)
/i?-//. 7<^
G.-&CJ o ~~ 9 c
-------
MONITOR PERFORMANCE TEST DATA.SHEET
ZERO AND CALIBRATION DRIFT (2 HOUR)
Data
Set
No.
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
Begin
?:ao
//:0*>
/£*!&£?
/7 ' ' ' &'*0
~
9. S3
9,A~0
9,4"?
// .07
'.c-3
* .0t
' .&<
—
"' .,2
",&?
-*.&•*
* •&?
—
-./*
4 .03
4 .01
.
~ .C?
•> . ^ ,-
&
. S
'fyj'f\ •«• [Span] x 100 » £,.£4/£. S
Ul
I
10
U)
Data Sheet 6017-33
40CFR60/App. B
3/26/79 (Rev. 1)
-------
MONITOR PERFORMANCE TEST DATA.SHEET
ZERO AND CALIBRATION DRIFT (2 HOUR)
Data
Set
No.
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
Begin
^y * &£}
//*&£?
/f:*e
/J-.&?
/ f *&£?
/?
a
&
&
0
o
-------
MONITOR PERFORMANCE TEST DATA.SHEET
ZERO AND CALIBRATION DRIFT (2 HOUR)
Ul
w
H
H
'£&
/?:&?
/f;#0
/7:#
/r:c&
^/ '&&
//:#7*?
&-/3-7 /g . S
Data Sheet 6017-33
40CFR60/App. B
3/26/79 (Rev. 1)
-------
MONITOR PERFORMANCE TEST DATA.SHEET?
ZERO AMD CALIBRATION DRIFT (2 HOUR)
Data
Set
No.
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
Begin
00
&
//:00
/S&0
te~:00
End
Date
tf'//'7 %f
Calibration
Drift
(Span-Zero)
— .
-//
-^
O
. tftr '
.&j"
./
-a
-./
o
—
./
o
~— /
—
'.3
o
o
./ &rJcfr»wfC' <•
teXf ] * [Span] x 100 • &Sg%.S
**/•/»».«/?«• ^//
en
Data Sheet 6017-33
40CFR60/App. B
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
CALIBRATION ERROR DETERMINATION
Calibration Gas Mixture Data
Mid (50%) .j^^BpT High (90%)
Calibration Gas Measurement: System .
Run f Concentration, ppnf^ Reading, ppiti^? Differences,
2 //
±A &3L
H
8
/r
10
//
12 //
13
9,2
0
Mid High
Mean difference •$ — , /
Confidence interval + O + Q
Calibration error Mean Difference2 + C.I. o
Average Calibration Gas Concentration —: • •
Calibration gas concentration - measurement system reading
Absolute value
Data Sheet 6017-31
77 40CFR60/App. B
7/1/77
KVB11-6015-1233
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
CALIBRATION ERROR DETERMINATION
Calibration Gas Mixture Data
Mid (50%) /0.0 BPTO High (90%) /Zg
Run If
Calibration Gas
Concentration,
Measurement System
Reading,
Differences,
//
J7£_
5 //
S0.0
/?.&
7 //
t*.0
0.0
10
11
12
n.s
/7.8
14
15
//?£.
Mean difference
Confidence interval
Calibration error =
Mean Difference
Mid High
0 C
Average Calibration Gas Concentration
x 100
0 % 0 %
Calibration gas concentration - measurement system reading
Absolute value
78
Data Sheet 6017-31
40CFR60/App. B
7/1/77
KVB11-6015-1233
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
CALIBRATION ERROR DETERMINATION
Calibration Gas Mixture Data
Mid (50%) /
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
CALIBRATION ERROR DETERMINATION
Calibration Gas Mixture Data
Mid (50%) ^~ 49 900 O
12
-3
13 //
14 & &
Mid High
Mean difference flNir Q
Confidence interval + » "7 + ^
Mean Difference + C.I. ,_0 / » - />
Calibration error = Average calibration Gas Concentration X 10° -^-% -2—
Calibration gas concentration - measurement system reading
Absolute value
~~Data Sheet 6017-31
80 40CFR60/App. B
-------
APPENDIX D
CONTINUOUS MONITOR PERFORMANCE SPECIFICATIONS
KVBll-6015-1233
-------
App.B
Title 40—Protection of Environment
PntrosMANCi ErecrncATTOH 3 —
^SyEtl^ClfloJTTT^D BPXCiriCATIOK TZST WO-
coumzs rot MONTroma or SOi un NO«
STATIONAXT SOUBCXB ~— "*
1. Principle and Applicability.
1.1 Principle. The concentration of sulfur
dioxide or oxides of nitrogen pollutant* In
•tack emissions U measured 07 a continu-
ously operating emission measurement sys-
tem Concurrent with operation of the eon*
tlauous monitoring system, the pollutant
concentrations are also measured with refer-
ence methods (Appendix A). An average of
the continuous monitoring system data to
computed for each reference method testing
period and compared to determine the rela-
tive accuracy of the continuous monitoring
system. Other tests of the continuous mon-
itoring system are also performed to deter-
mine calibration error, drift, and response
characteristics of the system.
IS Applicability. This performance spec-
ification 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.
3. Apparatus.
3.1 Calibration Gas Mixtures. Mixtures of
knows concentrations of pollutant gas In a
diluent gas shall be prepared. The pollutant
gas shall be sulfur dioxide or the appropriate
oxide(s) of nitrogen specified by paragraph
fl and within subparti. For sulfur dioxide gas
mixtures, the diluent gat may be air or nitro-
gen. For nitric oxide (NO) gas mixtures, the
diluent gas shall be oxygen-free «10 ppm)
nitrogen, and lor nitrogen dioxide (NO,) gas
mixtures the diluent gas shall be air. Concen-
trations of approximately BO percent and 90
percent of span are required. The 90 percent
gas mixture Is used to set and to cheek the
span and Is referred to as the spaa gas.
2.2 Zero Oat. A gas certified by the manu-
facturer to contain less than 1 ppm of the
pollutant gas or ambient air may be used.
3.3 Equipment for measurement of the pol-
lutant gas concentration using the reference
method specified in the applicable standard.
3.4 Data Recorder. Analog chart recorder
or other suitable device with input Toltage
range compatible with analyzer system out-
put. The resolution of the recorder's data
output shall be sufficient to allow completion
of the test procedures within this specifi-
cation.
3.5 Continuous monitoring system for BO,
or NO> pollutants as applicable.
S. Definitions.
' 3.1 Continuous Monitoring System. The
total equipment required for the determina-
tion of a pollutant gas concentration la a
source effluent. Continuous monitoring sys-
tems consist of major subsystems as follow*:
1 1.1 Sampling Interface. That portion of
an extractive continuous monitoring system
that performs one or more of the following
operations: Acquisition, transportation, and
. conditioning of a sample of the source efflu-
ent or that portion of an in-situ continuous
• monitoring system that protects the analyzer
from the effluent.
3.12 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.
3.3 Span. The value of pollutant concen-
tration at wblcb 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.
3.3 Accuracy (Relative). The degree of
correctness with which the continuous
monitoring system yields the value of gas
concentration of a sample relative 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.
3.4 Calibration Error. The difference be-
tween the pollutant concentration indi-
cated by the continuous monitoring system
and the known concentration of the test
gas mixture.
3.6 Zero Drift. The change In 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 eero.
.3.8 Calibration Drift. The change In the
continuous monitoring system output over
« stated time period of norms] continuous
operations when the pollutant concentra-
tion at the time of the measurement* is the
same known upscale value.
S.T Response Time. Trie time Interval
-from a step change in pollutant concentra-
tion at the input to the continuous moni-
toring system to the time it which 96 per-
cent of the corresponding final value Is
reached as displayed on the continuous
monitoring system data recorder.
3.8 Operational Period. A minimum period
of time over which a measurement system
U expected to operate within certain per-
formance specifications without unsched-
uled maintenance, repair, or adjustment.
3.0 Stratification. A condition identified
J>y a difference in excess of 10 percent be-
tween the average concentration in the duct
or stack and the concentration at any point
more than 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
of the total emissions from the affected
82
KVB11-6015-1233
-------
Chapter I—Environmental Protection Agency
App.B
facility. Conformance with this requirement
•hail be accomplished as follows:
4.1 Effluent gases ma; be assumed to ba
nonstratlned II a sampling location elgbt or
more stack diameters (equivalent diameters)
downstream of any air in-leakage Is se-
lected. This assumption and data correction
procedures under paragraph 4.2.1 may sot
be applied to sampling locations upstream
of an air preheater In a steam generating
facility under Subpart D of this part. For
sampling locations where effluent gases are
either demonstrated (4.3) or may be as-
sumed to be nonstratlfled (eight diameters),
a point (extractive systems) or path (tn-sltu
systems) of average concentration may be
monitored.
4.2 For sampling locations where effluent
gases cannot be assumed to be nonstratl-
fled (less than eight diameters) or have been
shown under paragraph 4.3 to be stratified.
results obtained must be consistently repre-
sentative (e.g. a point of average concentra-
tion may shift with load changes) or the
data generated by sampling at a point (ex-
tractive systems) or across a path (In-sltu
systems) must be corrected (42.1 and 433)
so as to be representative of the total emis-
sions from the affected facility. Conform-
ance with this requirement may be accom-
plished In either of the following ways:
4.3.1 Installation of a diluent continuous
monitoring system (O, or CO, as applicable)
in accordance with the procedures under
paragraph 4.3 of Performance Specification
3 of this appendix. If the pollutant and
diluent monitoring systems are not of the
same type (both extractive or both In-situ).
the extractive system must use a multipoint
probe.
4.2.3 Installation of extractive pollutant
monitoring systems using multipoint sam-
pling probes or in-situ pollutant monitoring
systems that sample or view 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 emissions
sampled or viewed are consistently repre-
sentative for several typical facility process
operating conditions.
43 The owner or operator may perform a
traverse to characterize any stratification of
effluent gases that might exist in a stack or
duet. If no stratification is present, sampling
procedures under paragraph 4.1 may be ap-
plied even though the elgbt diameter criteria
ls not met.
4.4 When single point sampling probes tar
extractive systems are installed within the
stack or duet under paragraphs 4.1 and 42.1.
the sample may not be extracted at any point
less than 1.0 meter from the stack or duct
wall. Multipoint sampling probes Installed
under paragraph 433 may be located at any
points necessary to obtain consistently rep-
resentative samples.
6. Continuous Monitoring System Per-
formance Bptemeatlona.
The continuous monitoring system shall
meet the performance specifications In Table
3-1 to be considered acceptable under this
method.
- TABLE 2-1.—Performance tpedflcatlon»
Psrasuter
Spedftallm
I. AouancT' . ....„..„•.-—„ <3B pet of the mean value of the reference metbad ust
dau.
2. Calibration error' -< 6 pet of each (SO pet, 90 pet) calibration tat miitnre
value.
S. Zero drift O h) > 8 pet of span
4. Zero drift (24 h)' . . Do.
(. Calibration drift (2 h)' Do.
ft. Calibration drtft (24 h) • 23 pet. of tpaa
7. Response tine .. IS mln «MTitnmn.
L Operational period...... IB h minimum.
> Expressed at nun of absolute mean value plus U pet ooiBdenoel nurral of a series of tests.
A. Performance Specification Test Proce-
dures. The following test procedures shall be
wed to determine conformance with the
requirements of paragraph 6. For NO. An-
alyzers that oxidize nitric oxide (NO) to
nitrogen dioxide (NO,), the response time
test under paragraph 8.3 of this method shall
be performed using nitric oxide (NO) span
gas. Other tests for NO. continuous monitor-
log systems under paragraphs 8.1 and 93 and
all tests for sulfur dioxide systems shall.be
•'performed using the pollutant span .fas spe-
cified by each subpart. ''
•6.1 Calibration Error Test Procedure. Set
up and calibrate the complete continuous
monitoring system according to the manu-
facturer's written Instructions. This may be
accomplished either In the laboratory or in
• the field.
•8.1.1 Calibration Oas Analyses. Triplicate
analyses of the gas mixtures shall be per-
formed within two weeks prior to use using
Reference Methods 8 for SO, and 7 for NOm.
Analyze each calibration gas mixture (50%.
•0%) and record the results on the example
sheet shown in Figure 3-1. Bach sample test
result must be within 30 percent of the aver-
aged result or the tests shall be repeated.
This step may be omitted for non-extractive
monitors where dynamic calibration gas mix-
tures are not used (6.1.3).
8JJ Calibration Error Test Procedure.
Make a total of IB nonconsecutlve measure-
ments by alternately using zero gas and each
calibration gas mjrtureyconceptratlon (e.g.
0%. 80%. «%. 90%. 80%. 80%, 80%. 0%.
etc.) . T ........... I ..... in* Mlllllimmiii iiiimllqi
ITFttr" ftif* **** r"— TJiirt mir t»i r»r
*"rm*il r-y ruing, fsm ar more -?"»— -*t~»«
83
KVB11-6015-1233
-------
APP.B
Title 40—Protection of Environment
cells whose concentrations are certified by
the manufacturer to be functionally equiva-
lent to these gu concentrations Convert the
continuous monitoring system output read-
ings to ppm and record the results on the
example sheet shown in Figure 2-2.
83 Field Test for Accuracy (Relative).
Zero Drift, and Calibration Drift. Install and
operate tbe continuous monitoring system In
accordance with the manufacturer's written
instructions and drawings as follows:
6.3.1 Conditioning Period. Offset the eero
setting at least 10 percent of the spaa so
that negative zero drift can be quantified.
Operate the system for an initial 168-hour
conditioning period In normal operating
manner.
922 Operational Test Period, Operate tbe
continuous monitoring system for an addi-
tional 168-hour period retaining the eero
offset. Tbe system shall monitor tbe source
effluent at all times except when being
zeroed, calibrated, or backpurged.
6.3.3.1 PI»M T»«!t far f^fnr^f rp.1.»l».^
For continuous monitoring systems employ-
Ing extractive sampling, the probe tip for tbe
continuous monitoring system and the probe
tip for tbe Reference Method sampling train
should be placed at adjacent locations In the
duct. For KOX continuous monitoring sys-
tems, make 37 NOX concentration measure-
ments, divided into nine sets, using tbe ap-
plicable reference method. No more than one
set of tests, consisting of three individual
measurements, shall be performed la any
one hour. All individual measurement* of
each set shall be performed concurrently,
or within a three-minute interval and the
results averaged. For BO, continuous moni-
toring systems, make nine SO, concentration
measurements using the applicable reference
method. No more than one measurement
shall be performed in any one hour. Becord
the reference method test data and the con-
tinuous monitoring system concentrations
on the example data sheet shown in Figure
.3-8.
4222 Field Test for Zero Drift and Cali-
bration Drift. For extractive systems, deter-
mine tbe values given by eero and span gas
pollutant concentrations at two-hour inter-
val* until 16 sets of data are obtained, for
reycfalr*^ tha
— hSSKEJcaBy
en-* r't- electronic clrculLry~incl.udlng-.tbe
p^t>*lQIl_iiTiTiT* snrt tlittrttir isenrntilj nr
by-tn»ertlng-tlme ui "Uiorercallbratton -«a»
and. computing the zero point from "the
uriinis rneeeuremeat*. H-tMi-fcrttsr-taen-
nique If ntfl a
by-ibe -owner or-operatorf or each -measure"
"rnent system that shows the relationship- be
CWMB— tbe -trpsnsle -meaaurement*~tad the
t»ro point. _Tne span -of -the system shall be
checked
ments (or the computed zero drift) on Uu
example data sheet shown in Figure 3-4.
The two-hour periods over which measure-
menu are conducted need not be consecutive
but may not overlap. All measurement* re-
quired under thi* paragraph may be eon-
ducted concurrent with tests under para-
graph 622.1.
9223 Adjustment*. Zero and calibration
corrections and adJv^p^nU *>» allowed o5JT
at J4-hour 'intervals or at such shorter In-
iervals a* tee manufacturer's written In-
structions specify. Automatic corrections
made by the measurement system without
operator intervention or initiation are allow-
able at any time. During the entire 188-hour
operational test period, record on the ex-
ample sheet shown in Figure 3-5 the values
given by cero and span gas pollutant con-
centrations before and after adjustment at
24-hour intervals,
6 A Field Test for Response Time.
6.S.] Scope of Test. Use the entire continu-
ous monitoring system as installed. Including
sample 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
sample line), etc.. shall be at the nominal
values for normal operation as specified in
the manufacturer's written Instructions. If
the analyzer is used to sample more than one
pollutant source (stack), repeat this test for
each sampling point.
6.32 Response Time Test'Procedure. In-
troduce eero gas into the continuous moni-
toring system sampling Interface or as close
to the sampling interface a* possible. When
the system output reading has stabilized.
•witch quickly to a known concentration of
pollutant gas. Record the time from concen-
tration switching to 95 percent of final stable
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 seouence three m times
Record the results of each test on the
example sheet shown in Figure 2-8.
7. Calculations. Data Analysis and Report-
tog.
7.1 Procedure for determination of mean
values and confidence intervals.
• 7.1.1 Tbe mean value at a data set I*
calculated according to equation 3-1.
.
*tft«d »}y th»_ manufacturer-to-be •functkm-
ally-equivaleni4o-60 percent of span coaeen—
Jratloo. Becord the zero and span measure-
Equation 2-1
where:
a.=absolute value of the measurement*.
. Z=sum of the Individual values.
zsxaesn value, and
as number of data points.
7.12 The .95 percent confidence interval
(two-sided) I* calculated according to equa-
tion 3-2:
Equation 2-2
84
KVB11-6015-1233
-------
Chapter 1—Environmental Protection Agency
App.B
4
i
B
7
t
9 .....
10
11
12
U
It
IB
16
where:
£xt=sum of all data points,
t.tri^ti — o/2, and
C.I.w=95 percent confidence interval
estimate of the average mean
value.
Values for '.975
• «.«7S
• » 12.7C6
4.103
(182
2.77S —
ZJ71
2.447
2.165
2.S08 —
1262 -
1228
2.201
2.17B
£160
2.145 .
ZU1
The values in this table are already cor-
rected for n-1 degrees of freedom. Use n
equal to the number of samples as data
points.
72 Data Analysis and Reporting.
72.1 Accuracy (Relative). For each of the
nine reference method test points, determine
the average pollutant concentration reported
by the continuous monitoring system. These
average concentrations shall be determined
from the continuous monitoring system data ,
recorded under 722 by integrating or aver-
aging the pollutant concentrations over each
of the time intervals concurrent with each
reference method testing period. Before pro-
ceeding to the next step, determine the basis
(wet or dry) of the continuous monitoring
system data and reference method test data
concentration*. If the bases are not con-
sistent, apply a moisture correction to either
reference method concentrations or the con-
tinuous monitoring system concentrations
as appropriate. Determine the correction
factor by moisture tests concurrent with the
reference method testing periods. Report the
moisture test method and the correction pro-
cedure employed. For each of the nine test
runs determine the difference for each test
run by subtracting the respective reference
method test concentrations (use average of
each act of three measurements for NOi)
from the continuous monitoring system Inte-
grated or averaged concentrations. Using
these data, compute the mean difference and
the 05 percent confidence Interval of the dif-
ferences (equations 9-1 and 9-9). Accuracy
Is reported as the sum of the absolute value
of the mean difference and the 85 percent
confidence interval of the differences ex-
pressed as a percentage of the mean refer-
ence method value. Use the example sheet
'town In Figure 9-3.
722 Calibration Error. Dong the data
from paragraph 0.1. subtract the measured
pollutant concentration determined under
paragraph 6.1.1 (Figure 2-1) from the value
abown by tbe continuous monitoring system
tar each of tbe five readings at each con-
•bo
/I
centration measured under 6.12 (Figure 2-2).
Calculate the mean of these difference-values
and the 95 percent confidence Intervals ac-
cording to equations 2-1 and 2-2. Report the
calibration error (the sum of the 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.
722 Zero Drift (3-hour). Using tbe zero
concentration values measured each two
hours during the field test, calculate the 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 cum of tbe absolute mean value and
the confidence interval as a percentage of
span. Use example sheet shown In Figure
3-4.
72.4 Zero Drift (24-hour). Using tbe zero
concentration values measured every 34
hours during tbe field test, calculate the dif-
ferences between tbe zero point after zero
adjustment and tbe zero value 24 hours later
Just prior to zero adjustment. Calculate the
mean value of these points and tbe confi-
dence interval using equations 2-1 and 2-3.
Report the zero drift (tbe sum of the abso-
lute mean and confidence interval) as a per-
centage of span. Use example theet abown in
Figure 3-6.
• 72.6 Calibration Drift (3-aour). Using
tbe calibration values obtained at two-hour
Intervals during tbe field test, calculate the
differences between consecutive two-hour
readings expressed as ppm. These values
should be corrected for tbe 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 the sum of the abso-
lute mean and confidence Interval as a per-
centage of span. Use example sheet shown In
In Figure 2-4.
72.6 Calibration Drift (34-hour). Using
the calibration values measured every 34 •
hours during tbe field test, calculate the dif-
ferences between tbe calibration concentra-
tion reading after zero and calibration ad-
justment, and the calibration concentration
reading 34 hours later after zero adjustment
but before calibration adjustment. Calculate
the mean value of these differences and tbe
confidence interval using equations 3-1 and
3-3. Report the calibration drift (tbe sum of
the absolute mean and confidence Interval)
aa a percentage of span. Uae tbe example
sheet shown la Figure 2-5.
72.7 Response Time. Using the charts
from paragraph 62, calculate tbe time Inter-
val from concentration switching to 05 per-
cent to the final stable value for all upscale
and dowaseale tests. Report the mean of the
three upscale test times and the mean of the
three downseale test times. The two aver-
age times should not differ by more than 16
percent of tbe slower time. Report the slower
85
KVB11-6015-1233
-------
App.B
Title 40—Protection of Environment
time as the system response time. Use tbe ex-
ample sheet shown In Figure 2-6.
7.2.8 Operational Test Period. During the
168-hour performance and operational test
period, the continuous monitoring system
•hall not require any corrective maintenance,
repair, replacement, or adjustment other than
that clearly specified as required la tbe op-
eration and maintenance manuals as routine
and expected during a one-week period. If
tbe continuous monitoring system operates
•within the specified performance parameter!
and does not require corrective maintenance.
repair, replacement or adjustment other than
as specified above during the 168-hour test
period, the operational period will be success-
Sully concluded. Failure of the continuous
monitoring system to meet this requirement
abal] call for a repetition of tbe 168-hour test
period. Portions of the test which were satis-
factorily completed need not be repeated,.
Pallure to meet any performance specifica-
tions shall call for a repetition of the one-
week performance test period and that por-
tion of tbe testing which is related to the
fa'Jed specification. All maintenance and ad-
justments required shall be recorded. Out-
put readings shall be recorded before, and
' after all adjustments.
8. References.
8.1 "Monitoring Instrumentation for the
Measurement of Sulfur Dioxide In Stationary
Source Emissions," Environmental Protection
Agency. Research Triangle Park, N.C.. Feb-
ruary
8.2 "Instrumentation for the Determtna*
tlon of Nitrogen Oxides Content of Station-
ary Source Emissions," Environmental Pro-
tection Agency, Research Triangle Park, N.C.
Volume X. APTD-0847, October 1971: Vol-
ume 2. APTD-0042. January 1872.
8.3 "Experimental Statistics." Department
of Commerce, Handbook 01. 1963, pp. 3-31,
paragraphs 3-3.1.4.
8.4 "Performance Specifications for Sta-
tionary-Source Monitoring Systems for Oases
and Visible Emissions," Environmental Pro-
tection Agency, Research Triangle Park, N.C,
EPA-650/2-74-013. January 1974.
(ffcmict iktM MM
Him M.
-------
Chapter I — EnvIr«nm«niafTrol*cKon Agency
App.B
Calibration Gas Mixture Data (From Figure 2-1)
(SOS) ppe\ High (90t)
' Calibration Oas" Measurement System
un I Concentratlon.ppttt Reading, ppa
Differences, ppa
10
12
13
14
15
Hid High
Mean difference
Confidence interval
Calibration error *
Hean Difference* * C.I.
Average Calibration Gas Concentration
•X100
Calibration gas concentration - measurement system reading
•Absolute value
figure 2-2. Ctlfbratfon Error Petemtnatfen
87
KVBll-fi.015-1233
-------
Title 40—Protection of Environment
«*t
NO.
1
I
J
,
S
j
7
8
1
Otte
TIM
•Si1
!
tein refcrtnet'i
est Mlut (S02;
Reference He t hod &«mplei
Sttipfc 1
lit Confidence inumtt • *
m. t M.
bxpft I Swft 3
1
,
Nun rtfcrti
.test vilvc
eoi
<(enoe
(PP-i
•
KtWttod
(so.) •«
Antlytir 1-Heur
Avfrtgl (ppn)*
SO, «,
_
-'
_
Difference
so,""1*,
"
Mun ef
the dlfftrcneu
pp.
" ««n reference ncthod nluc * >™2
liln ind report wthed uud to detimlni Iflttgnud mrtgu
"
.**' .-
• I OK,)
Flgurt Z-3. Accurtcy ficunnliutlen (S02 *nd NOX)
Tl«
End
0«t«
1m
lertlng
•Zero
Drift
• • -Spin ••
Spin Drift
«M«1ng («Sptn)
•- OHbr»t1on
Drift
-• •( fptn- Zerg)
Zere Drift • l«e«n Jere Drift* * CI litre)
Ctllbritlon Drift • [«e«n Spin Drift* '. « CI (Sunl
«*tiolut« Vtlut. ' -
ISptn] ilOO •
« [Spui] i 10'
f\t»n 1-4. im
-------
Chapter I—Environmental Protection Agency
App.B
Date Zero Span Calibration
and Zero Drift Reading ' Drift
Tine Reading (aZero) (After zero adjustment) (ASpan) ••-.
Zero Drift « [Mean Zero Drift*
.-* C.I. (Zero)
« [Instrument Span] x 100
Calibration Drift • [Mean Span Drift*
.<*• C.I. (Span)
[Instrument Span] x 100 «
* Absolute value
Figure 2-5. Zero and Calibration Drift (24-hour)
89
KVB11-6015-1233
-------
App.8
Till* 40—Protection of Environment
Date of Test,
Span Cas Concentration
Analyzer Span Setting _
DDK
_ppm
'Upscale
seconds
seconds
seconds
Average upscale response ,
seconds
Downscalt
1 .
2.
3
seconds
seconds
seconds
; Average downscale response
System average response time (slower time) • _
{deviation from slower
system average response
jeconds
seconds.
[average upscale minus average dewnscale
slower time
laverj
U x 100X • .
Figure 2-6. Response Time
•pecincation* and specification teat proce-
dure* for monitor* of CO, and O, from sta-
tionary sources.
1. Principle mnd Applicability.
U Principle. Effluent gases are continu-
ously sampled and »re analyzed for carbon
dioxide or oxygen by a continuous monitor-
ing system. Testa ol the system are performed
during a minimum operating period to deter-
mine eero drift, calibration drift, and re-
sponse time characteristics,
1.2 Applicability. This performance ipeet-
fleatlon la applicable to evaluation of con-
tinuous monitoring systems for measurement
of carbon dioxide or oxygen. Tbeae speciflca-
ttona contain test procedure*. Installation re-
quirement*, and data computation proce-
dures for evaluating the acceptability of the
eontlnuoua monitoring system* subject to
approval by the Administrator. Sampling
may include either extractive or non-extrac-
tive (in-aitu) procedures.
3. Apparatus.
3.1 Continuous Monitoring System (or
Carbon Dioxide or Orygen.
3.3 Calibration Oas Mixtures. Mixture of
known concentration* of carbon dioxide or
oxygen in nitrogen or air. Mldrange and BO
percent of span carbon dioxide or oxygen
concentrations are required. The BO percent
Of span gas mixture la to be used to set and
Check the analyzer span and is referred to
a* spaa gas. For oxygen analyzers. If tb«
•pan is higher than 31 percent Or ambient
air may be -used la place of the BO percent of
•pan calibration gas mixture. Triplicate
analyses of the gas mixture (except ambient
air) shall be performed within two week*
prior to use using Reference Method 8 of
• thl* part.
. 2.S Zero Oas. A gas containing leas than 100
ppm of carbon dioxide or oxygen.
3.4 Data Recorder. Analog chart recorder
or other suitable device with Input voltage
range compatible with analyzer system out-
put. The resolution of the recorder'* data
output shall be sufficient to allow completion
of the test procedure* within thl* specifica-
tion,
8. Definitions.
3.1 Continuous Monitoring System. The
total equipment required for the determina-
tion of carbon dioxide or oxygen in a given
source effluent. The system consist* of three
major subsystem*:
8.1.1 Sampling Interface. That portion of
the continuous monitoring system that per-
form* one or more of the following opera-
tions: Delineation, acquisition, transporta-
tion, and conditioning of a cample of the
source effluent or protection of the analyzer
from the hostile aspects of the sample or
source environment.
90
KVB11-6015-1233
-------
Chapter I—Environmental Protection Agency
App. B
8.1.2 Analyzer. That portion of the oan-
Unuoui monitoring system which senses the
pollutant gu 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. Tbe value of oxygen or carbon di-
oxide concentration at which the continuous
monitoring system Is set that produces the
maximum data display output. For the pur-
poses of this method, the span shall be set
no less than 1.5 to 3A times the normal car-
bon dioxide or normal oxygen concentration
in the stack gas of the affected facility.
8.3 Mldrange. The value of oxygen or car-
bon dioxide concentration that is representa-
tive of the normal conditions in the stack
gas of the affected facility at typical operat-
ing rates.
3.4 Zero Drift. The change in the contin-
uous monitoring system output over a stated
period of time of normal continuous opera-
tion when the carbon dioxide or oxygen con-
centration at the tune for the measurement*
is zero.
34 Calibration Drift. The change In the
continuous monitoring system output over a
stated time period of normal continuous op-
eration when the carbon dioxide or oxygen
continuous monitoring system is measuring
the concentration of spaa gas.
8.6 Operational Test Period. A minimum
period of time over which the continuous
monitoring system 1* expected to operate
within certain performance specifications
without unscheduled maintenance, repair, or
adjustment.
3.7 Response time. The time Interval from
a step change in concentration at the input
to the continuous monitoring system to the
time at which 06 percent of the correspond-
ing final value is displayed on the continuous
monitoring system data recorder.
4. Installation Specification.
Oxygen or carbon dioxide continuous mon-
itoring systems aball be installed at • loca-
tion where measurement* are directly repre-
sentative of the total effluent from the
affected facility or representative of the earn*
effluent sampled by a BO, or NQ, continuous
monitoring system. This requirement (hall
be complied with by use of applicable re-
quirements in Performance Specification 2 of
this appendix a* follow*: .. .•
e.l installation of Oxygen at Carbon Di-
oxide Continuous Monitoring Systems Not
TJsed to Convert Pollutant Data. A sampling
location ehall be selected In accordance with
the procedures under paragraphs 4.2.1 or
4.2.3, or Performance Specification 3 of t&ia
appendix. . ... -
4.3 installation of Oxygen or Carbon Di-
oxide Continuous Monitoring System* Used
to Convert Pollutant Continuous Monitoring
System Data to Units of Applicable Stand-
ards. The diluent continuous monitoring sys-
tem (oxygen or carbon dioxide) (hall be In-
stalled at a sampling location where measure-
ments that <•»" be made are representative of
the effluent gases sampled by the pollutant
continuous monitoring system (s). Conform-
ance with this requirement may be accom-
plished in any of the following ways:
4.3.1 Tbe sampling location for the diluent
system shall be near the sampling location for
the pollutant continuous monitoring system
such that the same approximate point (s)
(extractive systems) or path (ln-*ltu •ye-
tems) In the croes section 1* sampled or
viewed.
4.3.2 The diluent and pollutant continuous
monitoring systems may be Installed at dif-
ferent locations If the effluent gases at both
sampling locations are nonstratlfled a* deter-
mined under paragraphs 4.1 or 44, Perform-
ance Specification 3 of this appendix and
there Is no in-leakage occurring between the
two sampling locations. If the effluent gate*
are stratified at either location, the proce-
dures under paragraph 422, Performance
Specification 3 of this appendix shall be used
tor installing continuous monitoring system*
at that location.
S. Continuous Monitoring System Perform-
ance Specification*. •
The continuous monitoring -system ahall
meet the performance specifications In Table
8-1 to be considered acceptable under this
method.
8. Performance Specification Teat Proce-
dures. .- - . •
The following test procedures (ball be used
to determine conformance with the require-
ments of paragraph 4. Due to the wide varia-
tion existing in analyzer designs and princi-
ple* of operation, these procedure* are not
applicable to all analyzers. Where this occurs,
alternative procedures, subject to the ap-
proval of the Administrator, may be emi
ployed. Any such alternative procedure* must
fulfill the same purpose* {verify response,
drift, and accuracy) a* the following proce-
dure*, and must clearly demonstrate con-
formance with specifications in Table 8-1.
«.l Calibration Check. Establish a calibra-
tion curve for the continuous monitoring
system using zero, mldrange, and *pan con-
centration ga* mixture*. Verify that the re-
eultant curve of analyzer reading compared
with the calibration gas value is consistent
witb the expected response curve a* described
by the analyzer manufacturer. If the ex-
pected response curve is not produced, addi-
tional calibration gas measurements «*«"
be made, or additional step* undertaken to
verify the accuracy of the response curve of
the analyzer.
•.3 Field Test for Zero Drift and Cali-
bration Drift. Install and operate the con-
tinuous monitoring system la accordance
91
KVB11-6015-1233
-------
App. B
Title 40—Protection of Environment
wltb tbe maoufacturer'l written Instruction*
and drawings as follow*:
TABLE 3-1.—Performance tpecifleatlona
Pannuter
Bptcifieatlon
1. Zero drift (2 b)'
2. Zero drift (24 b)'
I. Ckllbnuoo drill (2 b) >..
4. CtUbratloD drift (24 b)'.
t. Operational period ...
1. Response time...........
<0.4 pet Oi or COi.
-------
Chapter I—Environmental Protection Agency
APP.B
The values tn this table are already corrected
lor n-1 degrees of freedom. CM n equal to
the number of samples as data points.
7.2 Data Analyst* and Reporting.
7.2.1 Zero Drift (2-hour). Using the cero
concentration values measured each two.
hours during the field test, calculate the dif-
ference* between the consecutive two-hour
readings expressed In ppm. Calculate the
mean difference and the confidence Interval
using equations 3-1 and 3-2. Record the sum
of the absolute mean value and the confi-
dence interval on the data (beet shown la
Figure 3-1.
7.2.3 Zero Drift (24-hour). Using the eero
concentration values measured every 34
hours during the field test, calculate the dif-
ferences between the cero point after cero
adjustment and the eero value 24 hours
later just prior to cero adjustment. Calculate
the mean value .of these points and the con-
fidence Interval using equations 8-1 and 3-2.
Record the zero drift (the sum of the ab-
solute mean and confidence Interval) on the
data sheet shown In Figure 3-2.
7.2.3 Calibration Drift (2-hour). Using the
calibration values obtained at two-hour In-
tervals during the field test, calculate the
differences between consecutive two-hour
readings expressed as ppm. These values
should be corrected tot the corresponding
cero drift during that two-hour period. Cal-
culate the mean and confidence interval of
these corrected difference values using equa-
tions 3-1 and 3-2. Do not use the differences
between non-consecutive readings. Record
the sum of the absolute mean and confl-
dence Interval upon the data sheet shown
to Figure 3-1.
72.4 Calibration Drift (24-hour). Using the
calibration values measured every 34 boun
during the field test, calculate the differ-
ences between the calibration concentration
reading after zero and calibration adjust-
ment and the calibration concentration read-
ing 24 boun later after cero adjustment but
before calibration adjustment. Calculate the
mean value of these differences and the con-
fidence Interval using equations 3-1 and $-3.
Record the sum of the absolute mean and
confldence Interval on the data sheet shown
In Figure 3-2.
T-2.fi Operational Test Period. During the
168-hour performance and operational test
period, the continuous monitoring system
shall not receive any corrective maintenance,
repair, replacement, or adjustment other
than that clearly specified as required In the
manufacturer's written operation and main-
tenance manuals as routine and expected
during a one-week period. If the continuous
monitoring system operates within the speci-
fied performance parameters and does not re-
quire corrective maintenance, repair, replace-
ment or adjustment other than as specified
above during the 168-hour test period, the
operational period will be successfully con-
cluded. Failure of the continuous monitoring
system to meet this requirement shall call
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 aball
call for a repetition of the one-week perform-
ance test period and that portion of the test-
Ing which Is related to the failed specifica-
tion. All maintenance aad adjustments re-
quired shall be recorded. Output readings
shall be recorded before «nd after all ad-
justments.
7.2.8 Response Time. Using the date, devel-
oped under paragraph 6.3. calculate the time
Interval from concentration switching to 86
percent to the final stable value for all up-
scale and dowascale tests. Report the mean of
the three upscale test times and the mean of
the three downscale test times. The two av-
erage times should not differ by more than
16 percent of the slower time. Report the
slower time as the system response time. Re-
cord the results on Figure 8-3.
8. References.
8.1 "Performance Specifications for Sta-
tionary Source Monitoring Systems for Oases
and Visible Emissions," Environmental Pro-
tection Agency, Research Triangle Park, H.C,
EFA-660/3-74-013. January 1974.
8.3 "Experimental Statistics." Department
of Commerce. National Bureau of Standards
Handbook 01. 1983. pp. 8-ai. paragraphs
93
KVB11-6015-1233
-------
App. B
Title 40—Protection -of Environment
ItU
let Tin
(a. Icgln tntf Dm
1
I
1
4
$
«
1
»
9
10
n •
12
13
14
IS
C«Mbr«t1en Drift • (Htin Spin IT
•Abwlutt Vtlut.
Ztro SH« UUbntlcn
bra Drift Soin Drift Drift
bidln« (»Z«rc) btdlng (*Spm) Uip.n-iZ.ro)
» CI (^«ro) J •
F««ura 3-1, bra Md Ctlttntlan Drift U Hour).
94
KVBll-6015-1233
-------
Chapter t—Environmental Protection Agency
App.B
)ate Zero Span Calibration
ind Zero Drift Reading • Drift
rime Reading (aZero) (After zero adjustment) (ASpan)
Zero Drift « [Mean Zero Drift*
+ C.I. (Zero)
:a!1brat1on Drift - [Mean Span Drift*
+ C.I. (Span)
Absolute value
Figure 3-2. Zero and Calibration Drift (24-hour)
95
KVB11-6015-1233
-------
App.C
Title 40—Protection of Environment
Datt of Test
4 Span Gas Concentration
Analyzer Span Setting
1.
' Upscale 2.
3.
ppn
.PP"
.seconds
. seconds
seconds
Average upscale response
seconds
Downscale
1.
2.
3.
, seconds
_seconds
seconds
Average downscale response
seconds
System average response time {slower'tfrne}
seconds
t<£ev.*W from slower
system average response
average upscale minus average dcwnscale
slower time
x 1002
Figure 3-3. Response
(40 FR 46258, Oct. 6, 1975; 40 FR 59204. 59205, Dec. 22, 1675, as amended at 43 FR 6937,
Jan. 31.19771 . . _ _
AiraroB O—DSTmtDunoN or Etusaaoit RATS
C&iMOB
L Jtarrorfiutton.
LI Tb» following method shall be usrd to determine
wbetber a physical or operational change to an existing
facility resulted In an increase ID tbe emission rat* to tbe
atmosphere. Tbe method used is tbe Student's ( lest,
commonly used to make inferences from small (ample*.
I Data.
2.1 Each emission test shall consist of « runs (usually
three) whlcb prodace * emission rates. Tbns two acts of
emission rates are generated, one before and one after tbe
change, the two aeu being of equal rite.
2.2 when using ro»nniJ emission tests, eieept as pro-
Tided in { W,8(b) of tola part, tbe reference methods of
Appendix A totals pert shall be used In accordance with
tbe procedures specified In tb* applicable sobpart both
before and after tbe change to obtain the data.
2J When iranj continuous monitors, the facility shall b*
operated as U a menui.l emission test were being per-
formed. Valid data using tbe averaging time which would
be required If r. iranual emission test wen being con-
ducted shall be osea.
S. Procedure.
(.1 Subscripts a and b denote preehang* and post-
change respectively.
t.2 Calculate tbe arithmetic mean eml^on rate, E, for
each an of data using Equation L
... -t-g.
(1)
when:
E,-EmMon rate for tb* f th ran.
•-number of runs
U Calculate the sample Tarlance, S>, for each act of
data nslni Equation 2.
«,
» ••
_ .
n — i
.
n — i
1.4 Calcolate the pooled estimate, &V, nslnj Equa-
tton ft.
(3)
n.+n.-2
Calculate th*tattsututle,f,nsli«»qttafloot
96
KVB11-6015-1233
-------
APPENDIX E
TABULATION OF 15-MINUTE EMISSIONS DATA
97 KVB11-6015-1233
-------
SITE A
KVB CODES A THRU T
Code Explanation
A - Testing begins-
B - Testing ends
C - Data not taken
D - NO instrument out of service
E Op instrument out of service
F CO and CO instruments out of service
G NO and 0 instruments out of service
H - Typical high 02 (Top 20%)
I - Typical low 0 (Bottom 40$)
J - Very high 02 (Top 10%)
K - Very low 02 (Bottom 5%)
L - Typical high load (Top 20%)
M - Typical low load (Bottom 20%)
N - COp instrument out of service
0 - C0_ and NO instruments out of service
P - Boiler load data not taken
Q CO instrument out of service
R CO and NO instruments out of service
S - CO and Op instruments out of service
T - CO, NO and 0_ instruments out of service
98 KVBll-6015-1233
-------
**
**
**
ft*
**
**
DATE
ft* 6/ 3/60
•* 6/ 4/80
ft* 6/ 5/80
** 6/ 6/60
** 6/ 7/80
ft* 6/ 9/60
** 6/10/60
** 6/11/60
** 6/12/80
ft* 6/13/60
** 6/14/80
** 6/16/80
** 6/17/60
** 6/16/80
** 6/19/80
** 6/20/80
** 6/21/60
** 6/23/80
ft* 6/24/80
** 6/25/60
** 6/26/60
** 6/27/60
** 7/ 9/80
** 7/10/60
** 7/11/80
** 7/12/80
** 7/13/80
LOAD
TIME MWTH
ftftftftftftftftftftftj
12,0
11.2
10.8
11.4
7.6
12.2
12.6
11.9
11.6
10,4
8.0
11.3
11.5
11.2
11.3
10.9
8.5
10,4
10. e
10.1
8,4
7.0
12.5
11.0
H.l
9,8
7.8
DRV
02
VOLX
MEAS
tftftftftftftl
7.0
7.3
7.1
7.3
10.0
5.8
5.8
6.1
6.1
6.8
9.6
6.2
6.2
6.1
6.1
6.0
8.6
7.6
6.5
7.2
7.8
9.1
5.9
6.5
6.5
7.3
9.0
24 HOUR DATA
STACK GAS CONCENTRATION
C02
VOLX
MEAS
kftftftftftft^
10.7
10.4
10.1
10.0
7.6
11.2
11.4
11.2
11.2
10,5
7.9
11.1
11.1
11.2
11.0
11.2
8.4
9.8
10.7
10.0
9,4
7.9
11.0
10.8
10.6
10.0
8,3
CO
PPMV
MEAS
LAAAAAAd
IVCHKKWW)
17
28
26
24
28
26
29
27
27
26
34
35
28
28
31
27
54
65
21
23
58
205
26
27
27
23
21
NO
PPMV
MEAS
kftftftftftftl
195
208
216
237
195
235
244
246
248
240
204
223
212
215
219
230
202
234
242
237
223
199
206
218
217
221
208
CO
PPMV
3X02
bAAA*A*4
VwWWHwW*
21
36
33
31
45
30
34
32
32
33
53
42
34
33
37
32
78
87
26
29
79
311
31
33
33
30
31
NO
PPMV
3X02
tftftftftftfti
250
272
280
312
319
278
289
296
300
304
323
270
257
260
265
275
292
314
301
306
304
302
246
271
269
290
313
CO
N6/J
b******4
•WWHw""'
7
12
11
10
15
10
11
10
10
11
18
14
11
11
12
10
26
29
8
10
26
104
10
11
11
10
10
NO
NG/J
k Aft ft ft ft ft 4
138
ISO
154
172
176
153
159
163
165
168
178
149
142
143
146
152
161
173
166
170
168
166
135
149
148
160
173
**
**
**
**
**
**
k ** *
ft*
ft*
ft*
ft*
**
ft*
ft*
**
ft*
ft*
**
ft*
ft*
ft*
ft*
**
**
**
ft*
ft*
**
**
**
**
**
**
**
99
KVBll-6015-1233
-------
ft*
ft*
ft*
ft*
ft*
** DATE
************
** 6/
** 6/
** 6/
ft* 6/
** 6/
** 6/
** 6/
«* 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
»* 6/
** 6/
** 6/
ft* 6/
** 6/
** 6/
** 6/
ft* 6/
** 6/
ft* 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
ft* 6/
ft* 6/
ft* 6/
•* 6/
ft* 6/
** 6/
** 6/
** 6/
** 6/
** 6/
3/80
3/80
3/80
3/60
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/60
3/80
3/80
3/80
3/60
3/80
3/80
3/80
3/80
3/80
3/80
3/60
3/80
3/60
3/80
3/60
3/80
3/80
3/80
3/80
3/60
3/60
3/80
3/60
3/80
3/80
3/80
3/80
3/60
3/60
3/60
3/60
3/60
3/60
3/60
3/80
3/80
TIME
******
15
30
45
100
115
130
t«5
200
215
230
2«5
300
315
330
345
400
415
430
445
500
515
530
545
600
615
630
645
700
715
730
745
800
815
830
845
900
-------
**
**
ft*
»«
ft*
ft*
ft ft ft ft ft
** 6/
ft* 6/
** 6/
** (,/
** <»/
** ft/
ft* 6/
** 6/
** 6/
** 6/
** &/
** 6/
ft* 6/
** 6/
ft* 6/
ft* 6/
ft* 6/
** 6/
ft* 6/
** 6/
** 6/
** 6/
** 6/
ft* 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
ft* 6/
** 6/
** 6/
** 6/
** 6/
ft* 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6X
** 6/
** 6/
IS HIN. DATA
DRY STACK GAS CONCENTRATION
DATE
ft ft ft ft ft ft
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/60
3/BO
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
3/80
TIME
t ft ft £ ft ft ft
1215
1230
1245
1300
1315
1330
1345
1UOO
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
2330
2345
2400
LOAD
MKTH
ft A A A A A'
16.4
16,7
ia,s
16.4
13.5
10.5
10.5
10.0
10.5
11.7
10.3
10.3
10,0
10.5
12.'
12.9
11.4
10,5
10.8
10.3
10,3
10,8
10,5
10.8
10,8
10.0
10.8
14,9
13.8
13.2
13,2
12,0
11.7
10,3
9.7
9.7
9.7
10.5
10.3
10.3
9.7
10,3
9.4
9.4
9.4
9.1
9.1
9.1
02
VOLX
MEAS
t ft ft ft ft ft ft '
4.7
4.8
5.4
5.B
6.4
6.8
6.8
7.6
7.2
7.2
7.
7.
7.
7.
7.
7.
7.8
7.7
7.1
7.5
7.5
7.4
7.5
7.7
7.3
7.4
7.5
6.4
6.4
6.4
7.2
7.3
7.6
8.0
8.4
8.6
8.8
8.2
7.7
7.7
8.0
7.8
8.3
8.4
7.8
7.4
8.1
7.4
C02
VOLX
MEAS
F ft ft ft ft, ft ft '
12.6
13.0
13.0
13.2
12.4
12.0
11.6
11.4
11.0
11.2
11.2
10.0
10.2
10.0
10.0
10.6
10.4
10.2
10.6
10.6
10.6
10.0
10.0
10.0
10.1
10.1
10.0
9.8
11.0
H.I
11.2
10,2
10.4
10.0
10.0
9.7
9.8
9.8
10.1
10.0
10.0
9.8
9.8
9.8
9,8
10.0
10.0
10.0
CO
PPMV
MEAS
r * * 4 * * 4 i
•WUwKWWl
25
25
28
28
25
20
18
18
20
18
IB
20
15
15
15
15
15
15
15
15
10
10
10
15
10
10
15
20
15
15
15
IS
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
NO
PPMV
MEAS
f ft ft ft ft ft ft 1
205
205
200
205
200
205
190
195
200
190
185
183
188
160
188
185
185
190
185
180
190
195
185
188
185
188
200
195
195
198
190
188
185
185
184
189
190
190
182
190
195
195
185
186
188
188
190
168
CO
PPMV
3202
• * * + 4 * * '
i W W W W W W
27
27
32
33
30
25
22
24
26
23
24
26
20
19
19
20
20
20
19
20
13
13
13
20
13
13
20
24
18
18
19
19
13
13
14
14
14
14
13
13
13
13
14
14
13
13
13
13
ft*
ft*
**
NO CO NO ACUDE **
PPMV NG/J NG/J
3X02
r**+AAA*A**4ftftftftAftftftft4ft*'
rWWWUWWwWWWwWWWWWWWWWWKW
226 9 124
227 9 125
230 10 127
243 11 134
246 10 136
260 8 143
241 7 133
262 8 144
261 8 144
246 7 136
248 8 137
246 9 135
253 6 139
236 6 130
247 6 136
248 6 137
252 6 139
257 6 142
239 6 132
240 6 132
253 4 139
258 4 142
247 4 136
254 6 140
243 4 134
249 4 137
267
240
240
244
248
247
248
256
263
275
281
267
246
257
270
266
262
266
256
147
132
132
134
136
136
137
141
145
151
154
147
136
142
149
146
144
146
141
249 4 137
265 4 146
249 4 137
**
**
t ft ft ft ft ft ft
ft*
**
• *
**
**
ft*
**
**
**
ft*
**
ft*
ft*
ft*
»*
ft*
**
*«
ft*
**
**
**
• *
**
**
**
**
**
**
**
**
ft*
**
**
**
**
**
**
**
**
ft*
**
ft*
**
**
ft*
**
**
101
KVBll-6015-1233
-------
**
**
**
**
**
»* DATE
AAAAAAAAAAA1
** 6/ 4/80
«* 6/ a/eo
** 6/ 4/60
** 6/ a/80
** 6/ a/80
** 6/ a/80
** 6/ 4/eo
** 6/ a/80
** 6/ a/80
** 6/ 4/80
** 6/ a/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
»* 6/ 4/80
** 6/ 4/80
** 6/ 4/80
•* 6/ 4/80
• * 6/ 4/80
** 6/ 4/80
«» 6/ 4/80
• • 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ a/80
** 6/ a/80
** 6/ a/80
** 6/ 4/80
** 6/ 4/80
** 6/ a/80
** 6/ a/80
*• 6/ a/80
** 6/ 4/80
*» 6/ 4/80
** 6/ 4/80
** 6/ 4/80
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
A A 1t A it It
15
30
45
100
115
130
145
200
215
230
245
300
315
330
345
400
415
430
445
500
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
1145
1200
LOAD
MWTH
ff £ £ rik £ £ d
9.7
9.4
9.7
10.0
9.1
9.7
9.7
10.0
9.4
9.7
15.5
17.0
12.3
11. 4
10.3
10.0
10.0
9.7
9.1
9.4
9. a
8.8
7.6
9.7
14.9
12.0
12.6
12.6
13.8
14.6
16.4
15.8
13.8
13.8
15.2
15.2
12.9
10.0
8.8
8.5
8.5
8.2
8,2
8.2
8.2
B.2
11.4
12.3
02
VOLX
MEAS
£ dk db £ db * «
7.8
7.6
7.8
7.8
8.0
8.0
8.0
8.0
7.6
6.6
6.0
5.4
6.0
6.6
7.2
7.4
7.4
7.6
7.8
7.6
7.8
7.5
7.6
7.6
7,2
7.3
6.6
6.8
6.6
6.3
5.7
5.2
5.4
5.5
5.8
5.8
6.4
7.2
7.8
8.2
8.4
8.4
8.0
8.2
7.8
7.5
6.9
6.4
C02
vocx
MEAS
A ft ft A 4k Al
11.0
11.2
10.2
10.2
10.0
10.2
10.4
10.4
10.4
10.6
10.8
11.0
11.0
11.0
10.6
10.3
10.3
10.2
10.2
10.0
10.0
10.1
10.2
10.0
10.2
10.3
10.4
10.2
10.0
10.6
10,7
11.3
11.0
11.2
11.6
11.7
11.2
11,0
10.0
9.2
9.1
9.0
9.2
9.2
9.7
10.7
10.6
11.2
CO
PPMV
MEAS
i A + A + + * .
fWWwWWW]
20
20
20
19
19
19
20
20
20
20
20
20
20
20
20
20
20
20
20
20
20
20
65
40
43
35
22
25
25
25
28
40
40
36
35
30
32
33
34
32
32
35
30
25
25
26
28
25
NO
PPMV
MEAS
A A A A A A. •
K W W M W W 1
190
18S
185
190
190
195
185
185
185
190
190
195
195
190
200
195
192
192
188
166
190
195
195
205
200
205
205
200
200
195
195
190
190
195
195
195
198
200
210
215
215
215
200
200
200
210
205
200
CO
PPMV
3X02
1 A A A A A A i
27
26
27
25
26
26
27
27
26
25
24
23
24
25
26
26
26
26
27
26
27
26
87
53
56
46
27
31
31
30
32
45
46
at
at
35
39
43
46
as
45
50
41
35
34
34
35
30
NO
PPMV
3X02
1 A AA A A At
259
248
252
259
263
270
256
256
248
237
228
225
234
237
261
258
254
256
256
253
259
260
262
275
261
269
256
253
250
239
229
216
219
226
231
231
244
261
286
303
307
307
277
28}
273
280
262
246
CO NO ACODE
NG/J NG/J
^AAA^AA^^AAAAAAAAAAJ
AW A A r
143
137
139
143
145
149
141
141
137
131
125
124
129
131
144
142
140
142
141
139
143
143
29 144
18 152
16 144
15 148
9 141
10 140
10 138
10 131
11 126
15 119
15 120
14 124
13 127
11 127
13 134
14 144
15 158
15 167
15 169
16 169
13 153
11 155
11 150
11 154
12 144
10 136
• *
**
**
**
**
**
.A A A
r w w w
**
**
**
**
**
**
•*
• *
**
**
**
**
**
**
• *
**
*•
**
•*
**
**
• *
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
•*
**
**
•*
**
**
**
**
102
KVBll-6015-1233
-------
**
ft*
**
**
**
** DATE
ftftftftftftftftftftfti
** 6/ 4/80
• * 6/ 4/80
** 6/ a/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6X 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
• * 6/ 4/80
** t>/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
ft* 6/ 4/80
ft* 6/ 4/80
** 6/ 4/80
• * 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
** 6/ 4/80
15 MIN. DATA
DRY STACK GAS CUNCENTHATIQN
TIME
fc ft ft ft ft ft ft
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
2330
2345
2400
LOAD
MWTH
A A A A A Ad
W W W W W wl
13.8
14.9
14.9
11.4
10.3
9.4
9.1
10.3
10.8
12.9
11.7
11.7
11.7
12.0
12.0
12.3
12.3
11.7
12.0
13.2
13.2
12.3
11.7
13.2
12.9
10.3
10.0
9.4
10.3
10.5
10.5
10.0
9.7
9.7
9.7
9.7
11.7
14.9
13.5
13.5
11. «
9.4
9.1
9.1
9.4
10.0
9.7
9.7
02
VOL It
MEAS
kftftftftftftt
6.5
6.6
6.8
6.9
7.2
7.0
7.0
7.0
6.8
6.9
7.3
7.2
7.4
6.6
6.7
6.7
6.8
6.9
7.2
7.3
7.3
7.4
7.4
7.3
7.3
7.6
7.8
6.3
8.4
6.5
8.5
8.5
7.6
8.4
8.4
7.8
7.8
7.6
7.4
7.0
7.4
7.4
7.2
7.6
7.6
7.4
7.8
7.4
C02
VOLX
MEAS
kftftftftftftl
11.5
11.4
11.0
10.2
10.0
10.0
10.4
10.2
10.6
10,4
10.2
10,4
10.4
10.4
10.7
10.6
10.6
10.4
10.4
10.2
10.2
10.2
10.4
10.4
10*7
11.3
11.4
11.5
10.6
10.0
10.4
9.0
9.2
9.2
9.8
10.0
10.2
10.6
10.6
11.0
11.2
10.6
10.2
9.6
9.5
9.4
9.4
9.4
CO
PPMV
MEAS
kftftftftftfti
30
32
32
32
32
35
35
35
38
35
38
35
35
34
32
30
30
30
30
30
30
30
30
30
32
30
30
28
28
28
29
30
30
30
30
30
30
30
30
32
30
30
30
30
30
30
30
30
NO
PPMV
MEAS
kftftftftftftl
205
205
205
205
200
220
228
240
240
235
235
230
230
230
235
235
235
220
225
225
225
225
230
230
225
220
220
220
220
215
218
215
214
215
212
210
210
220
225
230
220
210
210
210
210
205
205
210
CO
PPMV
3X02
fcftftftftftftl
37
40
40
40
41
45
45
45
48
44
50
45
46
42
40
37
38
36
39
39
39
39
39
39
42
40
40
39
40
40
41
43
40
42
42
40
40
40
39
41
39
39
39
40
40
39
40
39
NO
PPMV
3X02
kft ft ft ft ft ft 1
254
256
260
262
261
283
293
309
304
300
309
300
304
287
296
296
298
261
293
296
296
298
304
302
296
296
300
312
315
310
314
310
268
307
303
286
286
296
298
296
291
278
274
282
262
271
280
278
CO
NG/J
fc ft ftftft ft ft 1
12
13
13
13
1«
15
15
IS
16
15
16
15
15
1«
13
12
12
12
13
13
13
13
13
13
1«
13
13
13
13
13
14
14
13
1«
14
13
13
13
13
13
13
13
13
13
13
13
13
13
NO ACODE
NG/J
k^AAjhAAVk**A4*<
KwHWITIIKicWWXWI
140
141
143
144
144
156
161
170
168
165
170
165
168
156
163
163
164
155
162
163
163
164
160
166
163
163
165
172
173
171
173
171
158
169
167
158
158
163
164
163
160
153
151
155
155
149
154
153
• *
**
**
**
**
**
b * * A
m W W W
**
**
**
»*
**
**
**
**
**
**
**
**
**
**
**
**
• *
**
**
**
**
• ft
**
**
**
**
**
**
**
**
**
**
**
• *
• *
**
**
**
**
**
**
**
**
**
**
• *
*•
**
103
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
ftftftftftftftftftftftl
** b/ 5/80
** b/ 5/80
** b/ 5/80
** b/ 5/60
** b/ 5/80
** b/ 5/80
** b/ 5/60
** b/ 5/80
** 6/ 5/80
** b/ 5/60
** 6/ 5/80
** 6/ 5/80
** b/ 5/80
** 6/ 5/80
** b/ 5/60
** b/ 5/80
** b/ 5/80
** b/ 5/80
** 6/ 5/60
** b/ 5/60
** 6/ 5/80
** b/ 5/80
** b/ 5/60
** 6/ 5/80
** b/ 5/80
** 6/ 5/80
** b/ 5/80
** b/ 5/80
** 6/ 5/80
** b/ 5/80
** 6/ 5/80
** b/ 5/80
** b/ 5/80
** 6/ 5/60
** b/ 5/80
** 6/ 5/80
** b/ 5/60
** b/ 5/80
** 6/ 5/80
** b/ 5/80
** 6/ 5/80
** b/ 5/80
** b/ 5/80
** 6/ 5/80
** b/ 5/80
«* b/ 5/80
** b/ 5/80
** b/ 5/80
15 MIN, DATA
DRY STACK GAS CONCENTRATION
TIME
ft ft ft ft ft ft
15
30
45
100
115
130
145
200
215
230
245
300
315
330
3*5
400
415
430
445
500
515
530
545
bOO
b!5
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
kft ft ft ft ft i
14.1
11.7
9.4
9.4
9.1
9.4
8.8
9.4
.4
.4
.5
.8
.8
.1
.8
.1
.4
.7
.7
10.0
9.4
9.4
IQtO
10.3
8.8
12.9
10.3
9.4
8.5
9.4
8.5
8.5
13.8
11.7
9.4
12.0
12, b
12. b
12, b
10.3
10,0
10.3
8.6
10.3
13.8
14.6
14.6
14. b
02
VOLX
MEAS
ft ft ft ft ft ft 1
b.9
6.4
7.0
7.7
7.b
7.7
7.9
7.8
7.7
7.7
8.0
8.1
8.0
8.0
7.8
7.9
7.4
7.5
7.5
7.b
7.7
7.8
7.8
7.7
7.7
7.b
7.5
7.9
6.5
8.6
8.8
8.7
b.8
5.6
5.4
5.4
5.7
5.5
5.5
7.0
8.1
7.2
7.7
6.9
5.5
5.b
5.4
5.b
C02
VOLX
MEAS
ft ft ft ft ft ft 1
11.2
11,2
10.0
9.b
9,5
9.4
9.8
9,4
9.5
9.3
9,2
9,b
9,2
9.4
9,5
9.5
10.0
9,8
10.0
9.9
9.5
9.5
9.7
9.8
9,7
10.0
10.0
9.1
9.0
9.0
9.0
9.0
9.8
11.0
10.2
10.2
10.3
10.4
10.2
10.3
9.4
10.0
9.7
10.3
11.5
11.4
11.5
11.5
CO
PPMV
MEAS
ft ft ft ft ft ft 1
28
28
28
28
28
28
26
29
29
28
28
28
28
28
28
28
28
29
29
29
29
29
29
29
29
29
30
30
30
38
38
35
35
41
41
40
38
32
22
19
22
7
21
27
26
27
31
24
NO
PPMV
MEAS
' ft ft ft ft ft ft 1
230
230
210
210
210
205
205
210
215
210
220
215
205
210
212
212
210
215
210
212
210
210
215
215
215
215
210
205
199
190
190
192
212
215
210
210
210
210
212
217
214
222
212
218
224
225
222
221
CO
PPMV
3*02
BAAAAAdhl
W K w W W W 1
35
34
36
37
37
37
38
39
39
37
38
39
38
38
38
38
37
38
38
39
39
39
39
39
39
39
40
41
43
55
56
51
44
47
47
4b
44
37
25
24
30
9
26
34
32
31
35
26
NO
PPMV
3X02
' * A A A * * «
W W W W W IV 1
294
263
270
284
282
277
282
266
291
284
305
300
284
291
269
291
278
287
260
285
284
286
293
291
291
289
260
262
287
27b
281
261
2b9
251
242
242
247
244
24b
279
299
290
287
278
260
2b3
25b
258
CO
NG/J
rA*A*ft4i
W W W W W w 1
12
11
12
12
12
12
12
13
13
12
13
13
13
13
12
12
12
13
13
13
13
13
13
13
13
13
13
13
14
18
18
17
14
16
15
15
15
12
8
8
10
3
9
11
10
10
12
9
NQ ACUOE
NG/J
'ftftAftAtkAftftAAA1
162
156
149
157
155
153
155
156
IbO
157
168
165
156
IbO
159
tbO
153
158
154
157
157
156
tbl
IbO
IbO
159
154
155
158
152
154
155
148
138
133
133
136
134
135
154
165
159
158
153
143
145
141
142
**
**
**
**
• *
**
f A 4 A
I W W M
**
**
**
**
**
**
• *
**
**
**
**
**
**
**
**
**
ft*
**
«*
**
**
ft*
**
**
**
**
**
**
• *
**
**
**
**
• *
**
**
**
**
**
**
**
**
**
**
*«
**
**
**
104
KVBll-6015-1233
-------
**
**
**
**
**
IS MIN. DATA
D«Y STACK GAS CONCENTRATION
02 C02 CO NO CO
LOAD VOLX VOLX PPMV PPMV PPMV
** DATE
******
** t,/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
«* 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
*» 6/
** 6/
** 6/
** 6/
«« 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
»* 6/
** 6/
** 6/
** 6/
******
5/80
s/eo
5/80
5/80
5/60
s/eo
5/eo
5/80
5/80
5/80
5/80
5/80
5/80
5/80
5/80
5/80
5/60
5/80
5/80
5/80
5/80
5/80
5/80
5/60
5/80
5/80
5/60
5/80
5/80
5/80
5/80
5/80
5/80
5/60
5/80
5/60
5/80
5/80
5/60
5/80
5/80
5/80
5/60
5/80
5/80
5/80
5/80
5/80
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
1615
1830
1645
1900
1
-------
**
**
**
**
**
** DATE
AAAAAAAAAAA1
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/60
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
*• 6/ 6/80
** 6/ 6/80
** 6/ 6/80
*ft 6/ 6/80
** 6/ 6/80
** 6/ 6/80
ft* 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
15 MIN, DATA
DRY STACK GAS CONCENTRATION
.
TIME
A A A A A A
15
30
45
100
115
130
145
200
215
230
245
300
315
330
345
400
415
430
445
500
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
1145
1200
LOAD
MWTH
jf £ £ £ A £ .
10.3
10.5
13,8
12.0
10.3
9.4
9.7
9.1
9.1
9.4
8.8
8.5
8.5
8.8
8.5
10.0
.4
.7
.4
.4
.1
.4
.1
.4
.7
10.8
15.2
11. 1
18.5
14.6
18,5
14.6
15.5
13.8
9,4
9,7
11.7
17.0
18.2
18.8
18.8
16.1
11.7
11.7
10.8
10.0
A. 8
13.8
02
VOLX
MEAS
, Jk JL Jk Jk JL £ .
7.2
7.2
5.4
6.4
7.8
7.9
7.9
8.3
8.3
7.9
9.0
6.8
9.0
8.7
8.8
8.4
7.4
8.0
8.3
8.1
8.4
8.3
8.1
8.3
7.8
6.7
5.7
7.1
5.6
5.5
5.0
5.2
5,7
6.1
8.6
8.6
7.4
5.0
4.6
4.6
4.4
5.0
6.4
6.1
6.5
6.2
8.4
5.6
C02
VOL*
MEAS
' A It A A It It !
10.2
10.2
11.7
10.8
9.7
.6
.6
.1
.2
.6
8.6
8.7
8.6
8.8
8.7
9.0
10.0
9.5
9.2
9.4
9.1
9.2
9.4
9.2
9.7
10.5
11.5
10.3
11.6
11.7
12.0
11.8
11.5
11.1
9.1
9.1
9.9
11.9
12.2
12.3
12.4
12.0
10.8
11.1
10.7
11.0
9.0
11.4
CO
PPMV
MEAS
r A; Hf A A A A i
17
18
23
19
15
15
15
19
17
16
18
16
16
16
16
17
20
18
17
t7
17
17
18
17
21
18
21
18
27
27
37
37
31
41
22
26
41
44
37
37
39
35
30
33
25
26
29
42
NO
PPMV
MEAS
r A A A A A A i
215
214
216
227
219
220
217
205
210
214
185
189
186
185
185
187
190
192
189
189
189
191
188
191
200
229
228
230
247
243
243
224
224
216
195
189
202
234
262
243
246
234
234
226
229
231
207
214
CO
PPMV
3X02
r A A A A A Ai
22
23
26
23
20
20
20
26
24
22
27
23
24
23
23
24
26
24
24
23
24
24
25
24
28
22
24
23
31
31
41
42
36
49
32
37
54
49
40
40
42
39
37
39
31
31
41
49
NO
PPMV
3X02
A A A A A Ai
280
279
249
280
299
302
298
291
298
294
278
279
279
271
273
267
251
266
268
264
270
271
262
271
273
288
268
298
288
282
273
255
263
261
283
275
267
263
287
266
266
263
288
273
284
281
296
250
CO
NG/J
k AAA A *Ai
7
7
8
7
6
6
6
9
8
7
9
7
8
7
7
8
8
8
8
7
8
8
8
8
9
7
8
7
10
10
13
14
12
16
10
12
16
16
13
13
14
13
12
13
10
10
13
16
NO ACODE
NG/J
rAAAAAAAAAAAAl
154
154
137
154
165
167
164
160
164
162
153
154
154
149
150
147
138
146
148
145
149
149
144
149
150
159
148
164
159
155
150
140
145
144
156
151
147
145
158
147
147
145
159
150
156
155
163
136
ft*
**
• *
**
**
**
r * * *
**
**
**
**
**
**
ft*
ftft
**
**
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
**
**
ft*
ft*
ft*
ft*
ft*
ft*
ft*
**
ft*
*•
ft*
**
**
ft*
ft*
ft*
ft*
*•
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
**
106
KVBll-6015-1233
-------
**
**
**
**
ft*
** DATE
44**44*44**<
WWWWWWWWWWW1
** 6/ 6/BO
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/BO
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
ft* 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
•* 6/ 6/80
ft* 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
ft* 6/ 6/80
«* 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
ft* 6/ 6/80
ft* 6/ 6/60
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/80
** 6/ 6/60
ft* 6/ 6/60
** 6/ 6/BO
15 HIN. DATA
DRY STACK GAS CONCENTRATION
TIME
, A A ^ + A A
w w w w w w
1215
1230
1215
1300
1315
1330
13U5
1400
1*15
1030
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1600
1815
1830
1645
19QO
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
MtoTH
ff £ £ Jb £ Jk .
17.0
17.0
17.6
13.2
10.5
10.8
9.4
9.4
11.7
10.8
10.8
11.1
10.8
15.5
13.8
12.6
12.3
10.8
9.7
10.5
11.7
9.1
13.2
13.5
13.2
12.9
10.5
10.0
10.0
10.0
10.0
10,5
10.3
10.0
10.0
10.0
9.7
9.7
9.7
9.4
10.0
9.1
6.6
9.1
9.4
10.0
10.0
10.0
02
VOLX
MEA3
JL £ Jf £ ^k J. .
4.8
5.0
5.0
5.8
6.2
7.1
7.3
9.1
7.2
6.4
5.2
5.7
6.9
5.4
5.6
6.4
6.5
7.1
8.1
7.3
6.6
7.6
6.3
5.6
5.8
6.1
6.8
7.9
7.6
8.1
8.0
7.2
7.2
7.6
7.8
8.0
8.3
6.1
8.0
6.3
11.8
11.1
13.0
10.7
10.2
9.5
9.3
9.5
C02
VOLX
MEAS
1 1t fc 1t to ft ft 1
12.1
11.9
12.0
11.2
9.3
10.2
10.0
6.3
10.1
10.8
11.8
11.4
10*4
11.6
11.3
10.8
10.8
10.3
9.4
10.0
10.6
9.8
11.0
11.3
11.3
11.1
10.5
9.6
9.8
9.4
9.5
10.2
10.2
9.8
9.7
9.5
9.1
9.3
9.4
9.2
5.3
6.0
5.8
6.6
7.0
8.0
6.1
6.0
CO
PPMV
MEAS
1 ft ft ft ft ft ft i
42
35
39
37
26
34
47
29
37
30
37
29
29
30
27
22
21
20
20
20
21
19
21
22
21
19
19
17
16
15
15
17
17
17
17
16
16
16
16
16
38
26
27
26
39
22
20
19
NO
PPMV
MEAS
» + *4 + 4*4
1 W W W W W W 1
245
243
242
233
216
220
196
192
209
234
251
238
233
237
254
259
255
253
246
243
251
252
264
260
266
263
260
252
254
253
252
253
246
253
243
241
236
240
242
244
164
161
1611
167
177
195
197
198
CO
PPMV
3X02
F* * A* * ^4
W W W W W W1
46
39
43
43
36
44
61
43
46
37
42
34
37
34
32
27
26
25
27
26
26
25
25
26
24
22
24
23
21
20
20
22
22
22
23
22
22
22
22
22
74
47
61
45
65
34
30
29
NO
PPMV
3X02
' A*4 A A Al
W W W W W Wl
272
273
272
276
304
285
257
291
273
286
286
260
297
273
301
319
316
326
344
319
314
339
323
306
317
318
330
346
341
353
349
330
321
340
332
334
335
335
335
346
322
294
3650
293
296
306
303
310
CO
NG/J
**** ftft 1
W W W W " " *
15
13
H
14
12
14
20
1«
16
12
14
11
12
11
10
7
8
7
7
7
6
7
7
7
7
7
7
7
7
7
25
15
20
15
21
11
10
10
NO ACOOE
NG/J
ftftftftftftftftftftftftft
150
150
150
152
167
157
142
160
150
159
157
154
164
150
166
176
174
180
189
176
173
187
178
169
175
175
182
191
188
195
192
162
177
187
163
184
164
105
185
191
177
162
2012
161
163
166
167
171
**
**
• *
**
**
**
***
**
ft*
ft*
**
**
**
**
• *
• *
**
**
*•
**
**
**
**
«*
• •
**
*•
**
**
**
**
**
**
*»
**
**
**
**
**
**
**
*•
*•
**
**
**
**
**
**
**
**
**
**
**
• •
107
KVBll-6015-1233
-------
**
**
**
**
ftft
15 MIN. DATA
DRY STACK GAS CONCENTRATION
ft* DATE
***********<
ft* 6/
*ft 6/
ft* 6/
** 6/
** 6/
ft* 6/
** 6/
** 6/
** 6/
** 6/
ft* 6/
** 6/
*• 6/
** b/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
*« 6/
** 6/
** 6/
** b/
** b/
** 6/
** 6/
** 6/
• ft 6/
ft* 6/
ftft 6/
ftft 6/
ft* 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
7/80
7/80
7/80
7/80
7/80
7/80
7/60
7/80
7/80
7/60
7/80
7/80
7/80
7/80
7/80
7/80
7/80
7/60
7/80
7/80
7/80
7/60
7/80
7/80
7/80
7/80
7/80
7/80
7/80
7/80
7/80
7/80
7/80
7/80
7/80
7/80
7/80
7/60
7/80
7/80
7/80
7/80
7/80
7/60
7/80
7/60
7/80
7/80
TIME
rftft ftftftft
15
30
45
100
115
130
145
200
215
230
245
300
315
330
345
400
415
430
445
500
515
530
545
600
615
630
645
700
715
730
745
600
815
830
845
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
M*TH
******!
7,3
7,0
.4
.4
,7
.7
.2
,7
.4
.2
6.7
6.7
6.7
6.4
6.2
6,2
6.7
6.4
6,2
6,2
6.2
6.2
6.2
6.2
6.4
6.7
6.2
6.2
6.7
12.3
12.9
14.1
13,2
10.3
9,4
8,2
10.0
9.4
7,9
7,6
11,7
15.5
19.9
18.5
18.5
13.5
12.0
12.0
02
VOLX
MEAS
1 ft ft ft ft ft ft 1
9.2
9.6
10.0
10.0
9.
9.
10.
10.
.
1 .
1 .4
.7
.3
.8
10.4
10.0
9.5
9.6
10.2
10.4
10. 5
10.4
10.1
10.5
9.6
9.1
10.2
10.1
9.6
7.4
5.3
5.2
5.8
.8
.8
.7
.4
.8
.8
.7
5.6
4.5
4.5
4.5
4.5
5.B
5.8
5.8
C02
VOLX
MEAS
;ft ft ftft ftft'
8.3
7.8
7.4
7.4
7.6
7.5
6,9
6.6
7.5
7.8
6.9
7,7
8.1
9.5
6.9
7.3
7.9
7.9
7.1
6.9
6.8
7.0
7,3
6.9
7.9
8.4
7.3
7.3
7.9
10.0
11.7
U.9
11.3
10.3
10.3
10.5
10,9
10.3
10.3
10.5
11.6
12.5
12.6
12.6
12.4
H.4
11.3
11.3
CO
PPMV
MEAS
F ft ft ft ft ft ft 1
23
20
20
19
20
20
21
20
21
20
21
21
22
21
21
23
23
22
22
22
23
22
20
19
34
24
20
21
20
22
22
23
21
21
22
23
23
23
22
23
25
25
23
23
22
21
21
21
NO
PPMV
MEAS
. A A A A A A ,
r w »i w w w W .
195
194
189
168
189
166
164
162
183
168
183
187
169
188
185
166
187
169
166
186
185
187
188
188
195
202
195
192
196
253
256
252
252
232
227
216
245
231
223
218
237
263
276
275
266
250
243
246
CO
PPMV
3X02
[ ft ft ft ft ft ft '
35
31
32
31
31
32
35
34
34
31
35
33
33
33
35
37
36
34
36
37
39
37
33
32
53
36
33
34
31
29
25
26
24
26
27
28
30
29
27
28
29
27
25
25
24
24
24
24
NO CO
NO ACODE
PPMV NG/J NG/J
3X02
[ftftftftftftftftftftftfcwHwwvrwwwivwicwwwi
296 H 164
307 10 169
310 H 171
306 10 170
299 10 165
303 10 167
313 12 172
313 11 172
297 11 164
297 10 164
311 12 172
298 1
291 11
1 164
1 160
303 11 167
315 12 173
305 12 168
293 12 161
299 11
1 165
311 12 171
317 12 174
318 13 175
318 12 175
311 H 171
323 10 178
308 18 170
306 12 168
326 1
316 1
313 1
335
293
287
296
294
288
272
324 1
293
283
274
277
287
179
175
172
184
161
158
164
162
158
150
179
161
156
151
152
158
301 8 166
300 6 165
290 8 160
296 6 163
268 6 156
291 8 160
**
**
**
**
**
**
t * * *
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
*ft
**
**
**
**
**
**
**
**
ftft
•*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
108
KVBll-6015-1233
-------
**
»*
**
**
• *
** DATE
AAAAAAAAAA*
WWWWWHKWWWW
** 6/ 7/60
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
«* 6/ 7/60
** 6/ 7/80
** 6/ 7/80
»* 6/ 7/60
•* 6/ 7/80
** 6/ 7/80
** 6/ 7/60
** 6/ 7/80
** 6/ 7/80
»* 6/ 7/80
** 6/ 7/80
** 6/ 7/60
** 6/ 7/80
•* 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
•* 6/ 7/80
** 6/ 7/80
«* 6/ 7/80
** 6/ 7/80
«* 6/ 7/60
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
** 6/ 7/80
»* 6/ 7/80
** 6/ 7/60
IS HIN. DATA
DRV STACK GAS CONCENTHATION
TIME
k ft ft ft ft ft ft
1215
1230
1205
1300
1315
1330
1305
1400
1415
1430
14U5
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
2330
2345
2400
LUAD
MWTH
ft ft ft ft ft ft '
11.1
10.0
6,8
8.2
7.9
8.2
5.9
5.6
5.3
5.3
5,3
5.3
5.3
5.3
5.3
5.6
5.6
5.6
5.3
5.3
5.3
5.6
5.9
5.9
5.9
5.6
5.6
5.6
5.6
5.3
5,6
5.9
5.9
5.9
5.9
5.9
6.2
6.2
5.9
5.9
-.3
-.3
-.3
-.3
-.3
-.3
-.3
".3
02
VOLX
MEAS
r ft ft ft ft ft ft '
6.4
7.3
8.0
8.6
8.8
8.8
10.3
12.3
12.4
12.3
11.9
11.9
14.8
12.8
11.9
11.9
12.3
12.5
12.8
12.8
11.9
11.9
11.4
11.4
11.7
12.8
11.9
13.0
12.8
12.9
13.9
13.9
13.7
13.0
13.7
13.4
12.8
13.2
13.4
13.7
- .0
- .0
- .0
• .0
- .0
• .0
- .0
-1.0
C02
VOLX
MEAS
t ft ft ft ft ft ft '
10.8
10.0
9.4
8.0
8.6
8.7
7.3
5.7
5.4
5.6
5.9
5.9
3.2
5.2
5.6
5.8
5.6
5.5
5.2
5,2
5.8
5.8
6.3
6.3
6,1
5.3
6.0
5.0
5.2
5.1
4.0
4.0
4.1
5.0
4.7
4.6
4.9
«.7
4.6
4.1
.0
.0
.0
.0
.0
.0
.0
.0
CO
PPMV
MEAS
t ft ft ft ft ft ft
20
16
18
15
15
16
16
7
28
23
21
21
123
56
25
23
23
25
28
26
25
23
23
23
33
38
33
37
37
39
59
67
67
51
53
56
49
55
57
110
1
1
1
1
1
1
1
1
NO
PPMV
MEAS
t ft ft ft ft ft ft '
243
235
215
231
224
222
207
160
171
176
181
160
132
157
174
178
176
175
159
166
171
172
175
175
175
167
176
167
170
169
154
157
154
164
163
162
169
165
161
145
CO
PPMV
3X02
[ ft ft ft ft ft ft I
24
21
24
21
22
23
27
14
56
47
41
41
360
123
49
45
47
53
61
57
49
45
43
43
64
83
65
83
81
87
150
171
166
115
131
136
108
127
136
273
0
0
0
0
0
0
0
0
NO
PPMV
3X02
t A Aft ft ft ft '
299
309
298
336
331
326
349
374
360
366
359
357
387
346
346
354
366
372
351
371
340
342
329
329
340
369
350
378
375
378
393
401
382
371
405
386
373
383
384
360
0
0
0
0
0
0
0
0
CO
N6/J
i A * * A A * <
1 11 • W W W w
8
7
8
7
7
7
9
4
19
16
14
14
121
41
16
IS
16
17
20
19
16
IS
14
14
21
26
22
26
27
29
50
57
55
36
44
46
36
42
45
91
0
0
0
0
0
0
0
0
NO
NG/J
t ft ft ft ft ft '
165
170
164
165
162
181
192
206
196
201
198
197
213
191
190
195
201
205
193
204
187
186
161
181
187
203
193
208
207
208
217
221
211
204
223
213
205
211
211
198
0
0
0
0
0
0
0
0
ACODE
F ft ft ft ft ft ft '
C
C
C
C
C
C
C
C
**
**
**
**
**
**
p * 4 A
r K n W
*»
**
**
**
**
**
**
**
**
**
**
**
**
**
**
»*
**
**
**
t*
**
**
**
**
**
**
**
**
*«
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
«*
*«
**
**
109
KVBll-6015-1233
-------
**
**
**
**
**
**
*****
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** ft/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** fc/
** 6/
** 6/
** 6/
** 6/
• * 6/
** 6/
** 6/
** 6/
** 6/
** 6/
*« 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
** 6/
15 MIN, DATA
DATE
A A A A AA4
9/80
9/80
9/80
9/80
9/80
9/80
9/60
9/80
9/80
9/80
9/60
9/80
9/80
9/60
9/60
9/80
9/80
9/80
9/80
9/80
9/80
9/80
9/80
9/60
9/80
9/60
9/80
9/80
9/80
9/80
9/60
9/80
9/80
9/80
9/80
9/80
9/80
9/80
9/60
9/80
9/80
9/80
9/80
9/80
9/80
9/80
9/80
9/80
TIME
r A A A A A A
15
30
45
too
115
130
145
200
215
230
245
300
315
330
345
400
415
430
445
500
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
1145
1200
LOAD
MWTH
A A A A A A'
-.3
-.3
-.3
-.3
-.3
".3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
1.6
1.8
5.0
7.9
5.9
6.7
5.9
5.9
5.9
7.3
7.9
7.9
7.9
10.3
-.3
-.3
14.6
17.6
16.7
16.2
18.8
15.2
13.2
12.3
12.6
12.6
13.5
11.7
14,9
15,8
02
VQLX
MEAS
r A A A A A 1
- .0
• .0
• .0
• .0
• .0
• .0
- .0
- .0
• .0
- .0
• .0
• .0
• .0
• .0
• .0
• .0
- .0
- .0
12.5
10.0
9.8
7.9
9.7
8.6
11.4
11.0
10.1
7.4
7.3
7.3
7.6
5.9
-1.0
"1.0
4.3
4.0
3.9
DRY
STACK GAS CONCENTRATION
C02 CO
NO CO
VOLX PPMV PPMV PPMV
MEAS MEAS MEAS 3X02
.
.
m
•
•
•
.
•
•
.
•
•
•
.
•
.
«
.
« HMKHWWUWWHIfWW
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
,0
.0
.0
.0
5,4 444
7.6 35
7.8 26
9,5 24
8,0 20
8.8 45
6.3 46
6.7 40
7.6 35
9.9 21
10.1 20
10.1 20
9.8 25
11.3 34
-1
-1
.0 -1
.0 -1
12.1 30
12.2 39
12.3 33
4.0 12.8 38
3.8
5.7
5.2
5.1
5.1
5.4
4.8
4.5
4.7
4.4
12.8 36
11.2 36
11
.7 4
11.7 29
11
11
.7 27
.6 28
12.0 31
12.2 34
12.0 28
12.3 31
VWWVWWKVKIVIf!
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
141 946
200 57
211 41
235 33
222 31
211 66
190 86
192 72
204 58
242 27
249 26
251 26
241 33
253 40
-1 0
•1 0
231 32
212 41
223 34
228 40
227 37
210 42
224 4
233 32
239 30
244 32
239 34
239 37
246 30
245 33
NO
PPMV
3X02
k******<
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
300
328
340
323
354
312
357
347
338
320
327
330
324
301
0
0
249
224
234
241
237
247
255
263
270
281
265
260
271
265
CO
NG/J
k******<
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
317
19
14
11
10
22
29
24
19
9
8
8
11
13
0
0
10
13
11
13
12
14
1
It
10
10
11
12
10
11
NO
NG/J
k*****4
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
165
181
187
178
195
172
197
191
166
176
180
182
178
166
0
0
137
123
129
133
131
136
140
145
149
155
146
143
149
146
ACODE
******
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
**
**
**
**
**
**
**«
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
• *
*«
**
**
**
110
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
ftftftftftftftftftftft
** 6/ 9/80
** 6/ 9/80
ft* 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
ft* 6/ 9/80
ft* 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/60
*• 6/ 9/80
** 6/ 9/80
*ft 6/ 9/80
** 6/ 9/60
** 6/ 9/80
** 6/ 9/60
** 6/ 9/80
ft* 6/ 9/80
• * 6/ 9/80
ft* 6/ 9/80
«* 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
»* 6/ 9/80
** 6/ 9/80
** 6/ 9/60
** 6/ 9/80
** 6/ 9/80
** 6/ 9/80
15 MIN, DATA
DRY STACK GAS CONCENTRATION
TIME
t A A 4 1k A 4
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
2345
2300
2315
2330
2345
2400
LOAD
MWTH
444*4*1
K W W W W W l
13.5
12.9
11.7
12.3
15.2
16. 1
13.8
12,0
11*1
11.4
11.1
12.3
11. «
12.3
13.2
15.5
19.0
15.8
15.2
15.2
14.6
14.6
13.8
16.1
15.5
13.5
14.6
l«.l
12.0
12.3
12.9
J7.6
16.4
16.1
14.9
13.2
10.3
10.5
10.3
10.5
10.0
10.3
9.1
8.5
10.0
14.4
12.3
10.8
02
VULX
MEAS
r JL A 4 4 4 4 i
4.8
5.5
5.3
5.6
4.7
4.7
4.9
5.9
5.8
6.5
5.0
5.5
5.2
5.2
4.8
4.3
4.2
«.7
4.6
0.7
«.6
5.0
1.9
a. 3
4.8
5.3
4.8
5.6
5.5
5.3
5.2
4.6
4.6
4.6
4.8
5.4
7.0
6.0
6.5
6.2
6.7
6.5
7.3
7.4
6.6
5.1
5.0
6.7
C02
VOLX
MEAS
r 4 * 4 4 4 4<
12.0
11.6
11.7
11.5
12.2
12.0
11.0
11.0
11.2
10.7
11.9
11.5
11.7
11.6
12.0
12.5
12.5
12.1
12.2
12.1
12.2
11.9
12.0
12.4
12.0
11.7
12.1
ll.«
11.5
11.7
11.7
12.2
12.2
12.2
12.1
11.6
10.4
11.1
10.7
11.0
10.6
10.8
10.1
10.0
10.6
12.0
11.9
10,6
CO
PPMV
MEAS
' A A A A ft 4 '
24
25
25
24
29
27
27
28
22
26
31
29
30
27
27
29
33
27
25
31
26
23
21
22
21
20
22
20
21
22
23
28
27
26
26
23
23
24
23
23
22
23
20
20
21
23
23
21
NO
PPMV
MEAS
r ft *.*.*.*/ ^
257
252
252
258
234
222
223
230
247
235
230
236
235
237
231
226
234
232
230
230
229
238
238
227
238
242
231
245
246
242
242
228
225
228
231
247
241
246
244
247
247
246
239
238
236
238
243
248
CO
PPMV
3X02
ft ft ft ft ft ft ft 1
26
29
28
28
32
29
30
33
26
32
34
33
34
30
30
31
35
29
27
34
26
25
23
23
23
22
24
23
24
' 25
26
30
29
26
28
26
29
28
28
28
27
28
26
26
26
26
25
26
NO
PPMV
3X02
' ft ft ft ft ft ft 1
265
292
289
301
258
245
249
274
292
292
256
276
267
270
256
243
250
256
252
254
251
267
266
244
264
277
256
266
285
277
275
250
247
250
256
285
310
295
303
300
311
305
314
315
295
269
273
312
CO
NG/J
i 4 A 4 4 4 4 1
1 WW ft W W W •
6
9
9
9
10
10
10
11
6
10
11
11
11
10
10
10
11
10
9
11
9
6
7
7
7
7
6
7
1
6
6
8
8
8
6
NO ACODE
NG/J
'ftftftftftftftftftftftft'
157
161
159
166
142
135
137
151
161
161
142
152
147
148
141
134
136
141
139
140
136
147
146
134
145
153
141
156
157
153
152
138
136
138
141
157
171
162
167
165
171
166
173
174
162
146
150
172
**
*»
**
**
**
**
p 4 4 4
i W If W
**
**
**
**
**
**
**
**
**
«*
**
**
**
**
**
**
**
»*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
111
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
************
** 6/10/60
** 6/10/60
** 6/io/eo
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
•* 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/60
** 6/10/80
** 6/10/80
** 6/10/80
»* 6/10/60
•* 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/60
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/60
«* 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
«* 6/10/80
** 6/10/80
** 6/10/60
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/60
** 6/10/80
** 6/10/60
** 6/10/80
** 6/10/80
** 6/10/80
15 MIN. DATA
DRV STACK GAS CONCENTRATION
TIME
*******
IS
30
as
too
115
130
145
200
315
230
245
300
315
330
345
400
415
430
445
500
515
530
545
600
615
630
645
700
715
730
745
800
815
630
845
900
915
930
9a5
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MWTH
*******
12.6
10.3
10.0
10,3
10.0
10.5
10,0
10.3
10.5
10.8
9.7
10.6
10.8
10.8
10.6
12.0
14,9
14,9
12.'
12.6
13.2
12.0
9. a
9.4
6.6
10.3
12.3
10.5
14.6
11.7
12.0
10.8
9.4
9.7
9.7
13.6
15.5
16.2
16. a
15.2
14.1
15.5
17.3
15.5
14,9
15.5
16.1
15.5
02
VOLX
MEAS
********
6.3
6.8
7.3
7.1
6.9
7.1
.9
.5
.5
.7
.3
.7
.7
6.9
6.5
5.6
4.8
5.0
5.3
5.5
5.5
6.8
7.1
7.4
7.5
6.6
6.2
5.9
4.9
7.0
5.6
6.8
7.8
7.5
6.9
5.3
4.8
4.4
4.6
4.9
4.6
4.4
4.6
4.4
4.4
4.4
4.4
4.4
C02
VOLX
MEAS
r** ** * *<
11.0
10.6
10,1
10.3
10.6
10.3
10.5
10.6
10.8
10.7
10.1
10.6
10,6
10, 5
10.8
11.5
12.1
12.0
11.7
11.6
11.6
10.5
10.4
10.1
10.0
10.6
11.1
11.4
12.1
10.5
11.6
10.6
9.9
10.0
10.6
11.8
12.2
12.4
12.3
12.0
12.3
12.4
12.4
12.4
12.5
12.5
12.4
12.4
CO
PPMV
MEAS
r ******'
21
21
20
21
19
21
21
21
21
22
22
22
21
21
23
23
24
23
23
22
22
21
19
21
21
22
22
23
23
22
24
23
22
31
31
33
35
35
34
33
33
35
34
33
36
35
35
35
NO
PPMV
MEAS
r ******
250
246
243
243
243
245
241
243
246
244
237
243
242
242
244
234
236
241
247
253
251
249
238
235
237
246
248
243
243
251
251
254
243
226
226
230
221
219
223
227
227
226
226
226
226
229
229
232
CO
PPMV
3X02
(*****•*!
25
26
26
27
24
27
26
26
26
27
28
27
26
26
28
26
26
25
26
25
25
26
24
27
28
27
26
27
25
28
28
29
30
41
39
37
36
37
37
36
36
37
37
35
39
37
37
37
NO
PPMV
3X02
[******]
306
312
319
315
310
317
308
302
308
307
311
306
305
309
303
273
262
271
263
290
291
316
308
311
316
312
301
269
271
323
293
322
332
304
291
263
245
237
244
253
249
245
248
245
245
248
248
251
CO
NG/J
k*******
6
8
8
9
8
8
8
6
6
8
8
8
9
9
9
10
13
13
12
13
12
12
12
12
12
12
12
13
12
12
12
NO ACOOE
NG/J
*************
169
172
176
173
171
175
169
166
169
169
172
166
168
170
167
150
144
149
156
162
160
174
170
171
174
172
166
159
149
176
161
177
183
167
160
145
135
131
135
140
137
135
136
135
135
136
136
138
**
**
**
**
**
**
****
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
*•
**
**
**
**
**
**
**
**
**
**
**
**
112
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
ftftftftftftftftftftft
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
*• 6/10/80
** 6/10/80
•* 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
•* 6/10/80
** 6/10/60
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
•* 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/8Q
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/60
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
** 6/10/80
IS MJN. DATA
DRY STACK GAS CONCENTRATION
TIME
fc ft ft ft ft ft 41
1215
1230
1245
1300
1315
1330
1345
1UOO
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1615
1630
1645
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
MhTH
ft ft ft ft ft It '
15.2
16.4
15.2
17.3
15.2
13.2
12.9
12.3
11.7
12.0
11.7
12.0
13.2
15.5
15.2
14.6
15.8
20.5
15.5
17.6
12.6
13.2
16.4
16.1
14.9
14.9
13.8
13.8
12.3
12.0
1 .7
1 .7
1 .7
12.6
1 .4
1 .1
1 .4
1 .4
11.7
11.7
10.6
10.5
1 .1
1 .1
10.8
1 .1
1 .4
1 .1
02
VOLt
MEAS
[ £ £ £ £ A £ '
4. a
4.4
4.4
4.3
4.7
5.6
5.7
6.4
5.6
5.8
6.8
5.6
5.2
4.3
4.5
5.0
4.6
4.1
4.9
5.0
7.0
5.3
4.7
4.7
5.0
4.9
5.4
5.4
5.8
6.2
6.2
6.1
6.0
6.2
6.6
6.9
6.3
6.4
6.0
6.4
6.6
6.8
7.1
6.4
6.8
6.4
6.6
7.1
C02
VOL*
MEAS
( ft ft ft ft ft ft i
12.4
12.4
12.5
12.5
12.2
1.5
1.4
0.9
1.5
1.3
0.6
1.6
1.9
12.5
12.3
12.0
12.2
12.6
12.0
12.0
10.4
11.8
12.3
12.2
12.0
12.1
.6
.7
.5
.1
.1
.1
.3
.1
0.8
0.6
.0
.0
.3
tO
10.9
10.7
10.4
11.0
10.7
11.0
10.9
10.5
CO
PPMV
MEAS
i ft ft ft ft ft ft '
36
37
39
42
38
35
35
37
36
34
33
34
36
38
36
35
37
36
34
33
33
33
34
33
33
35
32
33
32
32
31
31
30
29
30
31
31
29
30
30
30
29
29
32
31
32
29
27
NO
PPMV
MEAS
r A ft ft ft A A '
230
232
231
231
237
252
252
242
253
263
252
255
253
240
248
257
246
239
253
256
255
252
248
251
254
249
258
259
257
258
252
257
254
258
249
252
249
253
253
257
253
254
249
253
252
257
256
253
CO
PPMV
3XU2
[ ft ft ft ft ft ft J
39
40
42
45
41
40
41
45
42
40
41
39
41
40
39
39
40
38
38
37
42
37
37
36
37
39
36
38
37
38
37
37
36
35
37
39
38
35
36
37
37
36
37
39
39
39
36
35
NO
PPMV
3X02
f ft ft ft ft ft ft 1
249
251
250
249
261
294
296
298
295
311
319
298
288
258
270
289
270
254
283
286
328
289
274
277
285
278
297
299
304
314
306
310
305
314
311
322
305
312
303
317
316
322
322
312
319
317
320
328
CO
NG/J
t ft ft ft ft ft ft'
13
13
1«
15
14
13
13
15
14
13
1«
13
13
13
13
13
13
12
12
12
1«
12
12
12
12
13
12
12
12
13
12
12
12
11
12
13
12
12
12
12
12
12
12
13
13
13
12
11
NO ACODE
NG/J
rftftftftftftftftftftftft'
137
136
136
137
144
162
163
164
163
171
176
164
159
142
149
159
148
140
156
156
181
159
151
152
157
153
164
164
167
173
169
171
168
173
171
177
166
172
167
174
174
177
178
172
176
174
176
180
*•
**
**
**
**
**
f * * A
r ft W W
**
**
**
**
**
**
**
**
**
**
*«
**
»*
**
*»
**
**
**
**
**
**
**
**
'**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
113
KVBll-6015-1233
-------
**
**
**
**
**
*#
+ A4
W W 1
ft*
**
**
**
**
ft*
**
**
**
**
**
**
**
**
**
ft*
**
ft*
ft*
**
ft*
ft*
**
**
**
ft*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
ft*
15 MIN. DATA
DRY STACK GAS CONCENTRATION
DATE
t444*+*+44
rWWWWWWWWl
6/11/80
6/11/80
6/11/80
6/11/60
6/11/80
6/11/80
6/11/80
6/11/80
6/11/80
6/11/80
6/11/80
6/11/80
6/11/80
6/11/80
6/11/80
6/11/60
6/11/80
6/11/60
6/11/60
6/11/80
6/11/80
6/11/80
6/11/80
6/11/80
6/11/60
6/11/80
6/11/60
6/11/80
6/11/80
6/11/80
6/11/80
6/11/80
6/11/80
6/11/60
6/11/80
6/11/80
6/11/80
6/11/80
6/11/60
6/11/80
6/11/80
6/11/60
6/11/60
6/11/60
6/11/60
6/11/80
6/11/80
6/11/60
TIME
b4 * A 4 * *
I W W W W W W
IS
30
45
100
115
130
145
200
215
230
2«5
300
315
330
345
400
415
430
445
500
515
530
545
600
615
630
645
700
715
730
745
800
615
630
845
«»oo
915
«»30
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MWTH
A + A A 4 A 4
W W W w W W r
11.1
10.5
13.2
13.2
9.7
15.2
!«.!
13.2
12.9
11.1
9.1
".1
8.8
8.5
«.l
9.1
10.3
10.0
10.3
10.5
7.9
8.2
8.8
8.6
9.0
8.6
8.2
10,3
8.5
8.5
8.5
8.5
".1
12.3
14.6
13.5
13,2
14.6
16.1
16,1
13.2
13.2
15.5
14,9
12.3
12.0
15.8
16.1
02
VOLX
MEAS
LAA*A**d
(WWKWWWV
6.2
6.6
5.7
5.3
6.9
5.1
5.5
5.6
6.2
6.5
7.6
7.8
7.7
8.0
7.5
7.6
6.5
6.9
6.9
6.9
7.7
7.4
7.6
7.8
7.3
7.0
7.5
6.6
7.6
7.9
8.1
8.1
7.7
6.1
4.8
4.8
5.1
4,9
4.6
4.9
5.3
5.1
4.6
4.8
5.8
5.6
4.5
4.5
C02
VOLX
MEAS
h*4**4*d
(WWWWWWV
11.2
10.9
11.5
11.9
10,7
12.1
11.8
H.7
11.2
11.0
10,1
10.0
10.0
9.9
10.3
10.2
11.0
10,7
10.8
10.7
10.1
10.4
10.2
10.1
10.5
10,7
10.4
11. 0
10.3
10.0
9.9
9.9
10,3
10.9
12.2
12.1
11.8
12.1
12.2
12.0
11.7
11.9
12.3
12.1
11.4
11.5
12.3
12.3
CO
PPMV
MEAS
F******4
30
29
33
31
30
31
31
31
30
33
28
30
28
28
30
29
29
30
29
29
29
30
29
31
30
30
26
31
30
29
29
29
29
12
27
28
0
26
30
30
28
27
26
27
29
29
30
30
NO
PPMV
MEAS
1 * It ** * * 4
253
257
244
256
252
250
257
257
254
255
246
242
246
239
242
243
250
246
247
250
246
235
241
237
240
246
243
246
247
241
241
241
244
232
237
244
244
243
238
244
251
247
239
245
253
245
235
239
CO
PPMV
3X02
t ****** f
36
36
38
35
38
35
36
36
36
41
37
40
37
36
40
39
36
38
37
37
39
39
39
42
39
38
37
36
40
39
40
40
39
14
30
31
0
31
32
33
32
30
30
30
34
33
32
32
NO
PPMV
3X02
1* *****4
308
321
287
293
322
283
298
300
309
316
331
330
333
331
323
327
310
317
315
319
333
311
324
323
315
316
324
307
332
331
337
337
330
260
263
271
276
271
261
272
288
279
262
272
299
286
256
260
CO
N6/J
********
12
12
13
11
12
11
12
12
12
13
12
13
12
13
13
13
12
12
12
12
13
13
13
14
13
12
12
13
13
13
13
13
13
4
10
10
0
10
11
11
10
10
10
10
11
11
10
10
NO ACODE
NG/J
k************4
169
177
156
161
177
156
164
165
170
174
182
182
183
182
178
180
171
174
174
176
183
171
178
178
174
174
178
169
163
182
165
185
182
154
145
149
152
149
144
150
158
154
144
150
165
158
141
143
• *
**
• *
**
**
• *
& ft * ft
• *
««
**
«*
ft*
**
**
**
**
**
**
• *
**
ft*
«*
**
**
**
«*
ft*
**
**
ft*
**
**
*ft
**
**
**
«*
**
**
**
**
ft*
«*
«*
ft*
ft*
ft*
ft*
**
**
ft*
**
**
**
**
114
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
************
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/60
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
«* 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
«* 6/11/80
** 6/11/80
«* 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
•* 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
** 6/11/80
15 HIM, 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
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
HWTH
*******
15.5
16,4
16.4
15.5
14.1
13.8
14.6
13.2
13.2
13.8
".7
11. 1
11.7
13.2
14.9
15.5
14,6
13.2
11.1
17.0
17.9
18.2
12.3
12.3
12.6
12.0
13.8
11.7
12.3
10.5
11.1
10.8
11.7
10.8
10.3
10.5
10.5
10.8
10.5
10.3
10.0
9.4
10.0
9.4
10.3
10.3
10.5
10.5
02
VOLX
HEAS
*******
4.5
4.5
4.5
4.6
5.0
5.2
4.7
5.3
4.9
5.3
7.1
6.0
5.6
5.0
4.7
4.6
4.7
5.3
5.9
4.6
4.4
4.3
5.7
5.5
5.6
5.7
5.2
5.9
5.7
6.6
6.2
6.4
5.9
6.3
7.0
.8
.7
.3
.6
.6
.8
7.1
7.2
7.4
6.6
7.0
6.3
6.5
C02
VOLX
MEAS
****** i
12.3
12.3
12.3
12.2
11.9
11.8
12.0
11.6
12.0
11.7
10.1
11.1
11.5
11.9
12.1
12.2
12.1
11.6
11.1
12.2
12.4
12.4
11.4
1.6
1.6
1.5
!.*»
1.3
1.5
0.7
1.1
1.0
11.3
11.1
10.6
10.7
10.8
11,0
10.8
10.9
10.7
10.5
10.4
10.3
10,9
10.6
11.1
11,0
CO
PPMV
MEAS
****** t
31
32
31
29
28
28
31
26
24
24
26
26
24
27
26
28
26
26
25
26
27
28
25
25
25
25
26
27
26
24
24
24
25
23
22
23
25
26
26
25
24
21
21
21
24
22
24
24
NO
PPMV
MEAS
****** 1
238
237
236
241
251
246
248
255
247
254
243
247
252
246
244
246
250
257
256
240
239
236
257
251
254
252
248
252
252
253
250
252
248
252
247
245
246
245
246
245
243
249
244
245
248
247
250
253
CO
PPMV
3X02
4 * * * 4 4 4
w K K X W H •
33
34
33
31
31
31
34
29
26
27
33
31
28
30
28
30
28
29
29
28
29
30
29
29
29
29
29
32
30
30
29
29
29
26
28
29
31
31
32
31
30
27
27
27
30
28
29
29
NO .
PPMV
3X02
****** 4
259
258
257
264
262
280
274
292
276
291
315
296
294
276
269
270
276
294
305
263
259
254
302
291
297
296
282
300
296
316
304
311
295
308
316
311
310
300
307
306
306
322
318
324
310
318
306
314
CO
NG/J
****** A
11
11
11
to
10
10
H
10
9
9
11
10
9
10
9
10
9
10
10
9
9
10
9
9
9
9
9
10
10
10
1
10
10
10
10
10
9
9
9
10
9
9
10
NO ACUDE
NG/J
************<
143
142
142
145
155
154
151
161
152
160
173
163
162
152
148
148
152
162
166
145
142
140
166
160
163
163
155
165
163
174
167
171
163
170
175
171
170
165
169
169
170
178
175
179
171
175
169
173
**
**
**
**
**
**
>***
**
**
**
**
**
**
**
**
**
*»
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
115
KVBll-6015-1233
-------
**
ft*
ft*
ft*
ft*
** DATE
A^tftftftftftft***
** 6/12/80
ft* 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
•* 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
ft* 6/12/80
** 6/12/80
ft* 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/60
** 6/12/80
** 6/12/80
** 6/12/80
*• 6/12/80
** 6/12/80
** 6/12/80
•* 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
ft******
IS
30
45
100
IIS
130
145
200
215
230
245
300
315
330
345
400
415
430
445
SOO
515
530
545
600
615
630
645
700
715
730
745
800
815
830
845
900
915
930
9<45
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MWTH
*******
11. 1
10.8
10.0
10.3
14.6
13.8
13.5
13.2
12.6
12.9
10.0
10.0
10.3
10.3
10.8
10.8
11.1
10.8
10.3
10.3
»0.3
7.6
8.2
8.8
10,0
11.7
10.3
9.4
8.2
8.2
8.2
9.7
10.0
8.2
8.2
8.8
12.9
13.5
12.3
14.1
15.2
15.2
16.1
16.4
15.8
16.1
14.9
14.1
02
VOLX
MEAS
********
6.2
6.4
7.0
6.9
5.2
5.2
5.4
5.4
5.5
5.7
7.2
.7
.9
.8
.3
.4
.4
.4
.0
.a
.9
7.8
7.5
7.8
7.2
5.9
6.6
8.0
7.4
8.1
8.0
7.7
6.7
7.8
7.4
7.4
6.2
5.2
5.9
5.5
5.0
4.8
4.8
4.9
4.9
4.8
4.9
5.1
C02
VOLX
MEAS
»******<
11.2
11.1
10.5
10,7
12,0
1 .9
1 .8
1 .8
1 .7
1 .5
10.4
10.9
10.7
10.8
H. I
11.0
H.l
11.1
10.6
10.8
10.8
10.0
10.2
9.9
10.5
11.4
10.9
9.9
10.3
9.7
9.9
10.2
11.0
9.9
10.2
10.1
11.1
11.9
11. «
11.7
12.1
12.2
12.3
12.2
12.2
12.2
12.1
12.0
CO
PPMV
MEAS
k******<
24
24
24
22
24
24
23
22
23
23
21
22
23
24
24
21
21
20
23
24
23
24
24
23
24
25
23
23
23
22
21
21
22
30
31
34
38
33
32
31
32
34
34
33
35
37
37
36
NO
PPMV
MEAS
k******<
250
251
246
246
243
248
252
254
256
255
250
251
247
251
251
254
254
254
248
253
251
241
238
236
249
256
258
244
247
241
241
251
270
230
234
237
239
251
245
243
240
238
234
235
236
240
242
241
CO
PPMV
3X02
»******!
29
29
30
28
27
27
26
25
26
27
27
27
29
30
29
25
25
24
29
30
29
32
32
31
31
29
28
31
30
30
29
29
27
40
41
45
46
37
38
36
36
37
37
36
39
41
41
40
NO
PPMV
3X02
»******<
304
309
316
314
277
282
291
293
297
300
326
316
315
318
307
313
313
313
319
321
320
329
317
322
325
305
322
338
327
337
334
340
340
314
310
314
291
286
292
282
270
264
260
262
264
266
270
273
CO NO ACOOE
NG/J NG/J
********************
1
1
167
170
174
173
152
155
160
161
164
165
180
174
174
175
169
172
172
172
176
10 177
9 176
11 181
10 175
10 177
10 179
10 168
9 178
10 186
10 180
10 185
9 184
9 187
9 187
13 173
13 171
15 173
15 160
12 157
12 161
12 155
12 148
12 145
12 143
12 144
13 145
13 147
13 149
13 150
**
**
**
**
**
**
****
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
•*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
• *
**
**
**
**
**
**
**
116
KVBll-6015-1233
-------
ft*
ft*
**
**
**
** DATE
ftftftftftftftftftftfti
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/60
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
*« 6/12/80
** 6/12/80
*• 6/12/80
** 6/12/80
•* 6/12/80
** 6/12/80
** 6/12/60
*» 6/12/60
** 6/12/80
** 6/12/80
• ft 6/12/80
** 6/12/80
** 6/12/80
** 6/12/80
** 6/12/60
** 6/12/60
** 6/12/80
** 6/12/80
** 6/12/80
• ft 6/12/80
** 6/12/80
IS MIN, DATA
DRY STACK GAS CONCENTRATION
TIME
: ft ft ft ft ft*
1215
1230
1245
1300
1315
1330
1315
1400
1415
1430
144S
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1645
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
MWTH
ft ft ft ft ft ft i
12.6
12.3
11.7
11.7
10,3
9.1
6.8
8.8
11.7
12.6
12.3
12.3
12.3
15.6
14.6
13.5
14.1
12.6
12.3
12.3
12.6
12.9
13.5
13.5
12.3
12.3
11.7
14.9
16.4
14.4
13.2
12.0
M.l
9.7
'.7
10.0
10.0
10.3
10.0
10.0
10.0
9.4
0.7
9.4
9.7
9.7
10.5
10.5
02
VOLX
HEAS
ft ft ft ft ft ft 1
5.5
5.6
5.9
5.1
6.S
7.6
7.5
7.9
5.6
5.5
5.4
S.3
5.1
4.5
4.9
5.3
5.2
5.6
5.8
5.8
5.6
5.5
5.3
5.4
5.7
5.9
6.3
5.3
4.9
5.2
5.7
.5
.0
.9
.8
.4
.4
.2
.1
.5
6.2
7.2
7.2
6.2
6.2
5.3
4.9
6.2
C02
VOLX
MEAS
' ft ft ft ft ft ft 1
11.7
11.6
11.3
11.9
10.7
9.8
10.0
9.7
11.5
11.6
11.6
11.7
12.0
12.4
12.1
11.8
11.9
11.7
11.5
11.5
11.8
11.8
12.0
11. «
11.7
11.6
11. «
12.1
12.4
12.3
11.9
11.3
11.2
10.4
10.5
10.8
10.8
10.9
11.0
10.8
11.0
10.3
10.3
11.0
11.0
11.7
12.0
11.1
CO
PPMV
MEAS
ft ft ft ft ft ft 1
35
36
35
36
36
35
35
37
40
38
32
26
27
26
30
28
28
28
26
26
27
29
28
27
27
27
28
29
30
27
27
26
26
25
25
26
25
25
26
24
24
25
24
24
24
26
26
24
NO
PPMV
MEAS
t ****** 1
w w w w w w i
244
241
245
248
237
233
231
225
248
258
262
259
254
246
257
260
261
265
264
265
260
256
253
255
260
258
262
246
243
248
252
261
264
259
246
249
251
259
252
250
245
245
236
240
246
251
242
242
CO
PPMV
3X02
> 4 A * * A * i
' m W W W W W 1
40
42
41
40
44
47
46
50
46
44
36
32
30
30
33
32
31
32
33
33
31
33
32
31
31
32
34
33
33
30
31
32
31
31
31
32
30
30
31
29
29
32
31
29
29
29
29
29
NO
PPMV
3X02
• * A* * * *<
W w W W W 1
283
261
292
280
294
313
308
309
290
299
302
297
287
266
267
298
297
310
312
314
304
297
290
294
306
307
321
284
271
282
296
324
317
331
312
307
309
315
304
310
298
320
306
292
299
268
270
294
CO
NG/J
***** * ft/1
' W W W W " W 1
13
14
i«
13
15
15
15
17
15
14
12
10
10
10
11
10
10
10
11
11
10
11
10
10
10
10
11
11
11
10
10
10
10
10
10
10
10
10
10
10
9
10
10
9
9
10
9
9
NO ACOOE
NG/J
ftftftftftftftftftftftft
156
155
161
154
162
172
170
170
159
165
166
163
158
148
158
164
164
170
172
173
167
164
160
162
168
169
177
156
149
155
163
178
174
162
172
169
170
173
168
171
164
176
170
161
165
158
149
162
**
**
ft*
**
ft*
ftft
*** *
ft*
ft*
**
**
ft*
ft*
ft*
ft*
**
**
**
**
ft*
ft*
ft*
ft*
**
**
**
**
**
**
**
ft*
ft*
ft*
*«
ft*
ft*
ft*
' ***
ft*
**
ft*
ft*
ft*
ft*
**
**
ft*
ft*
ft*
• *
ft*
**
ft*
*ft
ft*
117
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
***********!
** 6/15/60
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
«* 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
ft* 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
*« 6/13/80
ft* 6/13/80
«* 6/13/80
** 6/13/80
«* 6/13/80
ft* 6/13/60
** 6/13/80
** 6/13/80
ft* 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
ft* 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
•* 6/13/80
15 MIN, DATA
DRY STACK GAS CONCENTRATION
TIME
. dk £ £ £ £ £
15
30
45
100
115
130
145
ZOO
215
230
215
300
315
330
345
400
415
430
445
500
515
530
545
600
615
630
645
700
715
730
745
800
815
830
B45
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MWTH
A A Ik A A A 1
10.5
10.5
10.0
10.8
9.4
e.5
8.5
8,8
8.8
9.1
8.5
8.2
12.6
13.2
U.7
10.3
e.s
8.2
8.5
9.1
8.2
7.9
7.9
7.3
7.3
7.6
10.3
8.8
10.8
8.8
7.9
7.9
8.8
8.8
7.9
9.1
11.7
13.2
13.5
H. 1
10.3
14.4
16.1
15.8
16.1
15.2
15.8
16.1
02
VOLX
MEAS
1 * * * * if * i
6.2
6.5
6.3
7.3
7.8
7.8
7.8
7.7
7.3
7.7
7.8
7.4
0.6
5.1
5.8
7.4
7.0
7.4
7.2
7.8
7.0
8.1
8.9
9.9
7.1
6.4
7.1
6.8
6.7
7.4
7.3
7.3
7.7
7.3
7.0
6.2
5.4
5.1
5.9
6.2
4.8
4.4
4.2
4.0
4.3
4.2
4.1
5.3
C02
VOLX
MEAS
, A ^ A A A A i
' W w W W W • 1
11.0
10.8
10.9
10.9
9.9
9.9
9.9
10.0
10.3
9.9
9,9
10.2
12.1
11.8
11.3
10.2
10.6
10.3
10.4
10.0
10.6
9.7
9.1
8,4
10.5
11.7
10.5
10.9
10.9
10.5
10.6
10.6
10.4
10.1
10.3
11.1
11.7
12.0
11.3
10.8
11.9
12.1
12.2
12.3
12.3
12.3
12.3
11.6
CO
PPMV
HEAS
f * * * * it *1
25
26
25
24
23
23
23
22
23
23
23
24
25
24
24
23
23
22
22
21
23
23
25
23
24
24
24
24
24
24
24
24
24
25
24
25
26
27
24
25
25
27
27
27
27
30
31
30
NO
PPMV
MEAS
1 it * * * ** i
241
238
239
242
230
226
229
227
231
230
226
225
235
247
247
239
238
235
237
244
235
224
191
195
224
235
244
246
256
240
239
245
252
239
237
249
247
247
254
250
248
244
247
248
246
245
244
247
CO
PPMV
3X02
:******!
30
32
30
31
31
31
31
29
30
31
31
31
27
27
28
30
29
29
28
28
29
32
37
37
31
29
31
30
30
31
31
31
32
32
30
30
30
30
28
30
27
29
28
28
29
32
33
34
NO
PPMV
3X02
k******4
293
295
293
318
314
308
312
307
304
311
308
298
258
279
292
316
306
311
309
333
302
313
284
317
290
290
316
312
322
318
314
322
341
314
305
303
285
279
303
304
275
264
264
262
265
262
259
283
CO
NC/J
If****** <
10
10
10
10
10
10
10
10
10
10
10
10
1
10
12
12
10
9
10
10
10
10
10
10
10
11
10
10
to
10
9
10
10
11
11
NO ACOOE
NG/J
r************^
161
16}
161
175
173
170
172
169
167
171
170
164
142
154
161
174
169
171
170
183
166
172
157
174
160
159
174
172
177
175
173
177
186
173
166
167
157
154
167
167
152
145
145
|44
146
144
143
156
ft*
ft*
**
**
**
ft*
r* * ft
**
**
**
**
ft*
**
**
**
**
**
**
**
ft*
**
**
**
ft*
**
ft*
**
**
**
ft*
ft*
ft*
**
**
**
**
**
ft*
ft*
**
ft*
**
**
**
**
• ft
**
ft*
**
**
ft*
**
• ft
ft*
**
118
KVBll-6015-1233
-------
**
**
**
ft*
**
** DATE
ftftftftftftftftftftft
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
•* 6/13/80
** 6/13/80
** 6/13/80
• * 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
•* 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/60
•* 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/60
** 6/13/80
** 6/13/80
** 6/13/80
** 6/13/80
15 HIN. DATA
DRY STACK GAS CONCENTRATION
TIME
b * ^ * * * *
V K W W W W W
1315
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
1645
1900
1915
1930
19<*5
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
MHTH
ft ft A ft A ft
14.6
11.7
12.6
10.8
10.0
8.8
10.0
9.1
9.4
11.7
12.3
12.3
11.7
13.2
13.5
13.2
12.9
12.3
10.3
10.6
10.6
10.8
11.1
11.1
10.6
10.6
10.3
11.1
9.4
10.3
10.0
10.0
9.7
9.
7.
7.
7.
7,
7.
7.
9.7
.4
.«
.1
.7
.7
9.7
9.7
02
VOLX
HEAS
ft ft ft ft ft Aft '
5.8
5.3
. 5.9
6.2
7.2
7.2
6.0
6.9
5.4
5.2
S.«
5.5
5.1
4.5
5.0
5.1
5.2
6.1
6.2
6.2
6.2
6.0
6.0
6.1
*.3
6.6
6.1
7.1
7.0
6.2
7.1
6.6
7.6
8.4
9.5
8.6
8.6
6.7
8.2
8.6
9.0
9.5
10.1
10.1
9.5
9.2
9.1
9.1
C02
VOLX
MEAS
[ ft ft ft ft ft ft 1
11.3
U.7
11.2
11.0
10.1
10.2
10.8
10.4
11.6
11.7
11.6
11. S
11.8
12.2
11.8
11.8
.7
.0
.9
.0
.0
.1
.2
.0
10.9
10.6
n.o
10.2
10.4
10.9
10.3
10,5
.9
.0
.3
.0
.0
8.9
9.4
9.0
8.6
8.2
7.6
7.6
8.2
6.5
8.6
8.5
CO
PPMV
HEAS
' ft ft ft ft ft ft '
28
29
26
27
27
29
30
28
29
29
29
29
30
30
26
26
30
27
28
27
27
29
29
29
29
29
28
26
26
26
27
27
26
29
40
26
26
25
26
26
26
25
26
25
26
26
27
27
NO
PPMV
MEAS
p A A A 4 4 4 i
T H H W w W m '
252
255
257
252
240
238
246
243
262
270
263
272
262
264
273
276
274
274
269
273
270
272
271
269
266
260
262
261
255
260
251
2S6
245
224
160
211
216
212
218
206
196
201
198
198
197
189
190
186
CO
PPMV
3X02
>**** + *'
r W H W W W W 1
33
33
31
32
35
37
37
35
33
33
33
33
33
32
31
31
34
32
34
32
32
34
34
35
35
36
33
33
33
34
35
34
34
41
62
37
37
36
36
37
39
39
43
41
40
39
40
40
NO
PPMV
3X02
I ft ft ft ft ft ft i
298
292
306
306
313
310
306
310
302
307
326
316
296
268
307
312
312
331
327
332
326
326
325
325
326
325
316
336
328
316
325
324
329
320
251
307
314
311
307
299
297
315
326
328
309
289
288
285
CO
N6/J
» A ** A ft ft 1
t WW WW »» w »
11
11
10
11
11
12
12
12
11
11
11
11
11
10
10
10
11
10
11
11
11
11
11
11
11
12
11
11
11
11
11
11
It
13
21
12
12
12
12
12
13
13
14
13
13
13
13
13
NO ACOOE
NG/J
fftftftftftftftftftftftft]
164
161
169
169
172
171
168
171
166
169
180
174
163
158
169
172
172
182
160
163
181
180
179
179
179
179
174
186
181
174
179
179
181
176
138
169
173
171
169
165
164
174
160
160
170
159
158
157
**
**
**
**
**
**
t ft ft ft
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
ft*
**
**
**
ft*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
119
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
************
** 6/14/60
** 6/14/80
** 6/14/80
*» 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
«* 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
»* 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
IS MIN, DATA
DRV STACK CAS CONCENTRATION
TIME
r******
15
30
45
100
115
130
145
ZOO
215
230
245
300
315
330
345
400
415
430
445
500
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
1145
1200
02
LOAD VOL9C
MWTH MEAS
*********^***-
7.0
6.7
6.7
0.7
7.0
6.4
6.4
6.7
6.7
6.7
6.4
6.4
6.4
6.4
6.7
7.0
6.7
6.7
6.2 1
6.4 1
6.4
6.4
6.4
6.4
7.3
6.4
7.3
7.6
9.1
13.2
16.8
15.8
.7
.2
.1
.0
.0
.6
.2
.1
.1
.2
.4
.5
.5
.4
.1
.1
.1
.2
.1
.2
.2
.«
.3
.2
.5
.8
.4
.2
.3
.0
.4
.7
14.6 4.9
12.9 5.4
13.5 5.5
14.1 4.9
17.0 4.5
18.5 4.3
13.2 5.3
14.9 4.8
10.0 6.8
8.8 7.5
7.6 7.5
7.3 8.0
7.3 10.0
7.3 9.3
7.3 9.5
7.6 8.6
C02
VOLX
NEAS
1 * * * It * * i
8.9
8.4
8.5
8.6
8.6
8.1
8.4
8.5
8.6
8.5
8.3
8.2
8.2
8.3
6.6
8.6
8.5
8.5
7.6
7.6
8.4
8.4
8.4
8.5
9.2
8.9
8.4
9.5
10.3
11.3
12,4
12.2
12.1
11.7
11.7
12.1
12.4
12.5
11.9
12.2
10.7
10.3
10.2
9.7
7.9
8.5
8.4
9.2
CO
PPMV
MEAS
' * ** *** '
28
27
26
25
25
24
27
26
25
25
25
26
26
26
26
26
27
27
25
26
26
27
26
26
27
25
26
27
28
29
31
28
28
27
28
28
29
30
28
29
28
27
28
27
25
25
25
26
NO
PPMV
MEAS
r ******'
191
191
192
198
204
203
203
206
206
207
206
206
203
195
192
193
191
194
201
191
193
198
207
206
224
229
226
254
252
257
265
272
275
268
264
265
260
273
280
262
263
256
253
244
234
253
236
242
CO
PPMV
3X02
********
41
41
39
37
37
38
41
39
37
38
38
40
40
40
39
39
40
41
41
43
39
42
40
39
38
36
40
38
36
34
33
30
31
31
32
31
31
32
32
32
35
36
37
37
41
38
39
37
NO
PPMV
3X02
********
280
292
291
297
306
321
310
312
312
316
320
326
318
303
291
292
289
296
333
319
295
306
319
315
323
338
351
357
331
308
287
300
307
309
306
296
283
294
321
291
333
341
337
338
364
390
373
352
CO
N6/J
********
13
13
13
12
12
12
13
13
12
12
13
13
13
13
13
13
13
13
13
14
13
14
13
13
13
12
13
12
12
11
11
10
10
10
10
10
10
10
10
10
11
12
12
12
13
12
13
12
NO ACOOE
NG/J
i************
154
161
160
164
169
177
171
172
172
174
176
160
175
167
160
161
159
163
183
176
162
169
176
173
176
186
193
197
182
170
156
165
169
170
169
163
156
162
177
160
164
166
166
186
211
215
206
194
**
**
**
**
**
**
»***
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
ft*
**
*«
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
120
KVB11-6015-1233
-------
**
**
**
**
**
** DATE
ftftftftftftftftftftft^
** 6/14X80
** 6/14/eo
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
»* 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
*• 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
*» 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
** 6/14/80
*• 6/14/80
*• 6/14/80
** 6/14/80
15 MIN, DATA
DRY STACK GAS CONCENTRATION
TIME
tftft*. ft ft ft
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
2330
2345
2400
LOAD
MWTH
ft ft ft ft ft ft 1
13.2
16.1
13.2
12.9
8.8
11.7
8.8
6.2
5.6
5.6
5.6
5.6
5.9
5.9
6.2
5.9
5.6
5.3
5.6
5.6
5.6
5.6
5.6
5.6
5.9
5.3
5.6
5.6
5.6
5.9
5.9
5,9
5.9
5.9
5.6
5.6
5.6
5.6
6.7
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
02
VOLX
MEA3
' ft ft ft ft ft ft 1
5.4
5.3
5.9
5.9
8.7
7.4
8.7
11.7
13.6
12.3
12.6
12.5
11.5
11.6
11.2
11.7
11.6
12.6
12.2
12.3
11.5
11.6
11.3
11.6
11.3
12.1
13.3
12.7
13.4
12.6
13.2
13.6
13.6
12.8
13.0
13.4
13.5
13.4
1 .9
.0
.0
.0
.0
.0
.0
.0
.0
.0
C02
VOLX
MEAS
t * * * * ** 1
w w w w w w i
11.8
11.8
11.4
11.3
9.2
10.0
9.1
6.0
3.8
5.1
4.9
5.0
6.2
6.1
6.6
6.1
6.1
5.0
5.4
5.3
6.2
6.1
6.4
6.0
6.4
5.5
4.1
4.8
4.0
4.9
4.2
3.7
3.7
4.7
4.2
3.9
3.7
3,9
5.7
- .0
- .0
- .0
- .0
- .0
- .0
- .0
- .0
- .0
CO
PPMV
MEAS
' A ***** i
, W W m W w W 1
27
28
27
28
25
27
25
27
59
27
28
28
25
27
25
25
26
28
28
28
27
25
25
26
25
65
177
57
65
56
69
76
78
57
59
68
75
74
50
NO
PPMV
MEAS
>******<
' K W W W W K l
246
253
248
243
240
249
246
200
151
171
166
166
186
183
192
185
186
168
174
171
184
184
188
183
186
172
138
154
146
154
145
139
137
148
145
139
135
137
156
-1
-1
-1
•1
•1
-1
•1
•1
-1
CO
PPMV
3X02
! ft ft ft ft ft ft 1
31
32
32
33
36
35
36
52
144
56
60
59
47
51
46
48
50
60
57
58
51
48
46
50
46
132
416
124
155
120
160
186
191
125
133
162
181
176
99
0
0
0
0
0
0
0
0
0
NO
PPMV
3X02
W ft/ft ft ft ft 1
284
290
295
289
352
330
360
389
370
355
357
353
354
352
354
359
357
362
357
355
350
354
350
352
346
349
325
336
348
332
337
340
335
327
328
331
326
326
310
0
0
0
0
0
0
0
0
0
CO
NG/J
k ****** 1
• W 11 W w * ™ *
10
10
10
11
12
12
12
17
48
18
20
20
IS
17
15
16
16
20
19
l»
17
16
15
16
15
44
139
41
52
40
53
62
64
42
44
54
60
59
33
0
0
0
0
0
0
0
0
0
NO
NG/J
1 ft ft1 ft ft ft 1
156
160
163
159
194
182
199
214
204
196
197
195
195
194
195
198
197
199
197
196
193
195
193
194
191
192
179
185
192
183
185
187
185
180
181
182
180
180
171
0
0
0
0
0
0
0
0
0
ACODE
tftftft*. ft
c
c
c
c
c
c
c
c
c
**
**
**
**
*»
**
kftft
**
ftft
«•
ft*
**
**
ft*
ft*
ft*
**
ft*
ft*
ft*
**
ft*
ft*
**
**
**
**
**
ft*
ft*
**
ft*
**
**
**
**
**
**
**
**
ft*
**
*«
**
**
**
**
ft*
ft*
**
ft*
ft*
**
ft*
ft*
121
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
***********<
** 6/16/60
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
**, 6/16/80
** 6/16/80
*« 6/16/80
** 6/16/80
** 6/16/60
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
»* 6/16/80
** 6/16/80
** 6/16/80
** 6/16/60
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
TIME
i******
IS
30
45
100
115
130
H5
200
215
230
245
300
315
330
345
400
415
430
445
500
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
1145
1200
DRV STACK
02 C02
LOAD VOLX VOLX
MMTH MEAS MEAS
ftftftft*6£ftft + **********»*>A
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
n n n »« w w
.0
.0
.0
.0
.0
.0
.0
,0
,0
.0
*o
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
5,9 10.9 7.9
6.7 7.6 10,4
11. 1 7.0 11.7
9.7 6.8 11.0
10.8 7.1 10.9
12.6 5.7 11.9
10,8 6.1 11.6
12.0 8.2 10.1
11.7 5.2 11.8
12.3 5.4 11.6
15.5 4.7 12.2
14.9 4.7 12.1
15.5 4.8 12.1
14.6 4.7 12.2
14.6 4.8 12.1
15.5 4.5 12.3
16.1 4.5 12.3
15.8 4.4 12.3
16.1 4.4 12.3
16.1 4.3 12.4
14.6 4.3 12.3
9.4 7.1 10.2
9.4 7.3 10.1
10,5 5.9 11.2
10,0 7.2 10,2
15 MIN, DATA
GAS CONCENTRATION
CO NO CO
PPMV PPMV PPMV
MEAS MEAS 3102
A A ft
w it K m ww m
wmKvwwirwwi
0
0
0
o
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
a
99 187 177
58 210 78
60 211 77
35 226 44
32 221 41
41 209 a8
32 219 38
29 215 40
29 223 33
32 226 36
33 230 36
31 246 34
31 224 34
31 250 34
39 233 43
32 237 34
31 237 33
30 235 32
31 232 33
29 242 31
29 248 31
22 242 28
24 236 31
27 238 32
24 236 31
NO
PPMV
3X02
********
0
0
0
0
0
0
0
0
o
0
o
0
o
o
0
0
o
o
0
0
o
0
o
334
282
271
286
286
246
264
303
254
260
254
274
249
276
259
258
258
254
251
260
267
313
310
264
310
CO
NG/J
*******!
0
0
0
0
0
0
0
0
o
0
o
0
o
0
0
0
0
0
0
0
0
0
o
59
26
25
14
13
16
12
13
11
12
12
11
11
11
14
11
11
10
11
10
10
9
10
10
to
NO
Ntt/J
k*****i
o
0
o
0
0
0
o
o
o
o
o
0
o
0
o
0
0
o
0
0
o
0
o
184
155
149
156
156
135
146
167
140
143
140
151
137
152
142
142
142
140
138
143
147
173
171
156
171
ACOOE
******
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
**
**
**
**
**
**
• **
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
ft*
ft*
**
**
**
**
ft*
*»
ft*
ft*
ft*
**
ft*
ft*
**
**
122
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
ftAAAAftftAftA£l
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/60
** 6/16/80
** 6/16/60
** 6/16/80
** 6/16/80
** 6/16/60
** 6/16/60
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/60
** 6/16/60
«* 6/16/80
•* 6/16/80
** 6/16/60
»* 6/16/60
** 6/16/80
** 6/16/60
** 6/16/60
** 6/16/80
** 6/16/60
** 6/16/80
** 6/16/80
** 6/16/60
** 6/16/80
** 6/16/80
»* 6/16/80
** 6/16/80
** 6/16/80
** 6/16/80
** 6/16/60
** 6/16/60
*• 6/16/80
*• 6/16/60
IS MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
ft £ £ fL £ £ Jf
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
1630
1845
1900
1«»15
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
MWTH
£ *j| Aft £ 4
9.4
10.3
10.3
10.3
12.0
13.5
12.3
10.0
14,6
13.6
11.1
12.9
14,6
16.4
12.0
13.5
11.7
8.8
9.7
10.0
9.7
11.1
10.3
10.5
10.0
11.1
11.1
10.6
10.8
9.7
10.3
9.4
10.3
".7
10.3
9.1
9.1
•».!
9.4
9.4
9.4
9.7
10,3
10.6
9.7
B.2
8.8
8.2
02
VOL 5!
MEAS
fc£ftftltltft4
7.0
6.4
6.5
6.8
5.1
5.0
5.6
6.9
5.4
5.3
6.4
5.4
5.1
0.3
5.5
5.1
6.3
7.1
7.0
6.4
6.9
5.6
6.6
6.2
6.6
5.9
5.9
6.2
5.7
7.0
6.2
7.2
6.7
6.9
6.6
7.2
7.4
7.1
7.2
6.9
7.2
6.5
6.1
7.2
7.6
7.4
7.1
7.1
C02
VOLX
MEAS
kft&£ltft£ri
10.3
10.9
10. fl
10.6
11.9
11.9
11.5
10.4
11.6
11.6
10.6
11.6
11.8
12.4
11.5
11.9
10.8
10.2
10.3
10.6
10.3
11.4
10.6
10.9
10.5
11.2
11.2
10.9
11.4
10.3
11.0
10.1
10.5
10.4
10.7
10.1
10.0
10.2
10.2
10.4
10.2
10.6
11.2
10.3
9.9
10.1
10.3
10.3
CO
PPMV
MEAS
kAAAAAA*
rWWllKlrWl
23
26
25
25
36
33
29
26
35
29
27
29
29
32
27
30
26
29
29
28
26
26
25
24
25
28
26
25
27
25
27
26
26
26
26
25
25
27
26
26
31
27
29
427
32
30
30
28
NO
PPMV
MEAS
b*A**A*4
rwwwwwifi
241
238
230
230
216
226
225
225
220
233
217
215
223
233
223
210
221
217
216
218
216
220
223
221
219
218
220
221
218
220
220
218
214
215
219
219
216
219
218
219
210
213
214
213
215
209
210
214
CO
PPMV
3X02
klkftftftftfti
29
32
31
31
40
37
33
35
40
33
33
33
32
34
31
33
34
37
37
34
33
30
31
29
31
33
31
30
31
32
32
33
35
33
32
32
33
35
33
33
40
33
35
557
43
39
38
36
NO
PPMV
3X02
kftftAAAAf
310
293
265
291
244
254
263
287
254
267
267
246
252
251
259
237
270
281
278
269
276
257
279
269
278
260
262
269
256
283
267
284
269
274
274
286
266
264
284
280
274
264
258
278
289
277
272
277
CO
NG/J
b***+**4
•WWWWWWJ
9
10
10
to
13
12
11
12
13
11
11
11
11
11
10
11
11
12
12
11
11
10
10
9
10
11
10
10
10
10
11
11
11
11
10
10
It
11
11
It
13
11
11
167
14
13
13
12
NO ACUDE
NG/J
bftmtAftftttftftftftAJ
171
162
157
161
134
140
145
156
140
147
147
136
139
138
142
131
149
155
153
148
152
141
153
148
153
143
144
148
141
156
147
157
148
151
151
157
157
156
157
154
151
145
142
153
159
152
150
153
• »
**
*ft
**
**
**
& * it *
**
**
**
**
**
*»
**
*«
**
*»
**
**
**
**
**
**
**
*•
*•
**
**
**
**
*•
**
*«
**
**
• *
**
**
*•
**
*»
**
**
**
**
**
ft*
**
**
**
• *
**
**
**
**
123
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
***********
»* 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/60
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/60
** 6/17/80
** 6/17/60
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/60
** 6/17/80
** 6/17/80
** 6/17/80
«* 6/17/80
«* 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
»* 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/60
** 6/17/60
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
«* 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
•* 6/17/80
** 6/17/80
** 6/17/80
15 WIN. DATA
DRY STACK GAS CONCENTRATION
TIME
*******
IS
30
45
too
115
130
145
200
215
230
245
300
315
330
345
400
415
430
445
SOO
515
530
545
600
615
630
645
700
715
730
745
800
815
830
645
900
915
930
9(15
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MHTH
*******
11.7
10.5
10.3
9.7
".4
11.7
14.1
13.5
10,5
.4
.6
.2
.4
.«
.4
.«
1 .0
.«
.1
.«
.«
7.0
7.6
8.8
10.0
10.5
10.3
10.3
9,1
9.1
8.8
9.4
12.3
12.6
l«.l
14.1
15.5
15.8
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.4
16. 1
14.6
02
VOLX
MEAS
r It ft ft ft ft ft 1
6.3
4.9
6.1
7.0
6.8
6.9
5.1
5.3
6.5
7.2
7.5
7.7
7.0
7.3
6.9
7.1
6.8
7.1
7.8
7.0
7.6
8.4
10.5
6.3
7.2
6.8
6.7
6.9
7.8
7.2
7.6
7.6
6.2
5.3
5.2
4.9
4.8
4.6
4.5
4.6
4.5
4.6
4.5
4.5
4.5
4.6
4.6
4.8
CQ2
VOLX
MEAS
r A ft it ft it A '
11.0
12.0
11.1
10.4
10,6
10.5
11.9
11.8
10.9
10.3
10.0
9,9
10,4
10,1
10.5
10.4
10.6
10.4
9,8
10.5
10.0
9.2
7.4
9.4
10.3
10.7
10.7
10.6
9.9
9.8
9.6
9.9
M.I
11.8
11.9
12.1
12.2
12.3
12.3
12.3
12.3
12.3
12.3
12.4
12.3
12.3
12.3
12.2
CO
PPMV
MEAS
[ ft ft ft ft ft ft '
30
29
27
26
27
30
30
30
28
26
27
25
26
26
27
26
27
27
26
26
25
27
27
30
28
26
26
26
25
0
25
27
30
32
35
33
34
34
34
32
32
31
34
33
34
33
33
34
NO
PPMV
MEAS
h ftft ft ftftftj
212
215
218
217
215
213
217
217
221
220
217
219
215
216
216
218
221
216
218
222
221
205
179
191
208
217
215
219
220
219
214
216
220
220
205
209
209
214
213
215
216
215
215
216
222
216
227
215
CO
PPMV
3X02
»******)
36
32
32
33
34
38
33
34
34
33
36
33
36
34
34
33
34
35
35
33
33
38
46
42
36
33
35
33
34
0
34
36
36
36
39
36
37
37
37
35
34
34
37
36
37
36
36
37
NO
PPMV
3X02
»******<
259
240
263
279
272
272
245
248
274
287
269
296
276
264
278
282
280
262
297
265
297
293
308
271
271
275
271
260
300
286
292
290
267
252
233
233
232
235
232
236
235
236
234
235
242
237
249
239
CO
NG/J
»******<
12
10
10
11
H
12
11
11
11
11
12
11
12
11
11
12
15
14
12
11
11
11
11
0
11
12
12
12
13
12
12
12
12
11
11
11
12
12
12
12
12
12
NO ACUDE
NG/J
*************
143
132
145
154
150
150
135
137
151
158
159
163
152
156
153
155
154
155
164
157
164
161
169
149
149
151
149
154
165
157
161
160
147
139
128
128
128
129
128
130
129
130
129
129
133
130
137
131
**
**
**
**
**
**
• ***
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
124
KVBll-6015-1233
-------
**
**
**
ft*
**
** DATE
ftftftftftftftftftftft
** 6/17/80
*• 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/60
** 6/17/80
** 6/17/80
** 6/17/60
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
ft* 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/BO
** 6/17/80
** 6/17/80
** 6/17/60
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
«* 6/17/80
** 6/17/80
** 6/17/80
** 6/17/80
15 MIN. DATA
DRV STACK CAS CONCENTRATION
TIME
F ft ft ft ft ft ft
1215
1230
1205
1300
1315
1330
1305
1400
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
2315
2330
2345
2400
LOAD
MWTH
ft It ft ft ft ft '
15.2
14.1
13.8
11.1
11.1
12.9
13.5
12.9
11. 7
11.7
9.4
10.3
10.8
10.0
8.8
10.5
11.7
10.8
11.1
H.7
11.1
10.8
10.3
10.5
10,8
10.8
H.I
11.1
11.1
10.6
10.3
10.0
14.6
13.8
14.1
15.5
14.1
11.7
10.3
9.4
9.4
9.4
10.5
10.0
11.7
13.8
10.8
8.8
02
VOLX
MEAS
F ft ft ft ft ft ft <
4.9
5.0
5.0
5.6
5.7
5.5
4.8
4.8
5.8
5.5
7.0
7.5
5.8
7.2
7.0
5.7
5.3
6.4
5.9
6.0
6.1
6.0
6.7
5.9
5.9
6.5
5.7
5.8
5.8
5.6
6.4
6.4
5.8
5.0
5.2
4.8
5.0
5.9
7.0
7.4
7.6
7.4
7.6
7.1
7.0
5.1
6.3
6.8
C02
VOLX
MEAS
r ft ft ft ft ft ft •
12.1
12.1
12.1
11.6
11.6
11.7
12.1
12.2
11,4
11.7
10.5
10,2
11.5
10.3
10.5
11.5
11.8
11.0
11. «
11.4
11.2
11.
10.
11.
11.
11.
11.
11.
11.
11.
11.
11.
11.
12.
12.0
12.3
12.2
11.6
10.6
10.5
10.3
10.4
10.3
10.7
10.8
12.2
11.3
11.0
CO
PPMV
MEAS
r ft ft ft ft ft ft *
35
35
35
30
31
17
34
33
31
30
25
25
31
26
30
35
31
24
27
28
26
27
26
29
28
27
31
32
30
30
27
27
32
32
30
31
32
30
27
26
30
25
25
23
26
27
24
25
NO
PPMV
MEAS
[ ft ft ft ft ft ft 1
208
207
205
211
210
206
202
205
206
209
210
207
205
211
210
203
208
214
212
210
213
212
214
211
211
209
207
204
208
206
211
209
206
217
206
204
203
210
210
214
207
213
212
216
209
211
218
219
CO
PPMV
3X02
f ft ft ft ft ft ftl
39
39
39
35
36
19
37
36
36
34
32
33
36
33
36
41
35
29
32
33
31
32
32
34
33
33
36
37
35
35
33
33
37
36
34
34
36
35
34
34
40
33
33
29
33
30
29
31
NO
PPMV
3X02
f ft ft ft ft ft ftl
232
233
230
246
247
239
224
227
244
242
270
276
243
275
270
239
238
264
252
252
257
254
269
251
251
259
243
241
246
241
260
258
244
244
234
226
228
250
270
263
278
262
285
280
269
239
267
278
CO
N6/J
k * A A A A*1
! •« ftft WW»
13
13
13
11
12
6
12
12
12
11
10
11
12
11
12
13
11
9
10
11
10
10
11
11
11
11
12
12
It
11
11
11
12
12
11
11
12
12
11
11
13
11
11
10
11
10
9
10
NO ACODE
NG/J
'ftftftftftftftftftftftft
128
128
127
136
136
132
123
125
134
133
149
152
134
152
149
131
131
145
139
139
142
140
148
138
138
143
134
133
135
132
143
142
134
134
129
125
126
138
149
156
153
155
157
154
148
131
1«7
153
**
ft*
**
**
**
**
r ft ft ft
»*
**
**
»*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
•*
**
**
**
**
**
**
**
**
**
**
**
**
~ **
**
**
**
**
**
**
•*
**
**
**
**
125
KVBll-6015-1233
-------
**
**
ft*
**
**
** DATE
ftftftftftftftftftftftd
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
*« 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
*• 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
*« 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
ft* 6/18/80
ft* 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
ft* 6/18/80
*« 6/18/80
** 6/18/80
ft* 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
15 MIN, DATA
DRY STACK GAS CONCENTRATION
TIME
ft ft ft ft ft ft
15
30
as
100
115
130
145
200
215
230
245
300
315
330
345
400
415
430
445
500
S15
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
MhTH
t ft ft ft ft ft ^
9,1
6,8
8.8
8.8
9.1
9.4
9.7
9.4
9.7
8.8
8,5
8.5
.«
.1
.4
1 ,0
.7
.7
10.5
14,6
12.6
10.0
9.1
8.8
10.3
13.2
10.8
9.7
12.3
12.3
-.3
13.8
13.8
12.0
12.3
10.0
10.8
10.3
9.1
12.3
13.2
15.2
14.4
15.2
15.2
15.2
16.4
15.2
02
VOLX
MEAS
ft ft ft ft ft ft 4
7.7
8.0
8.0
8.0
7.7
7.6
7.1
7.6
7.0
8.1
7.9
8.2
7.7
7.3
7.8
6.8
7.4
7.8
6.9
5.2
5.2
7.1
7.8
8.5
7.7
5.8
6.7
6.9
7.1
5.2
-1.0
5.3
5.0
5.0
5.3
6.4
6.2
6.6
6.9
5.8
4.7
4.5
4.7
4.7
4.5
4.4
4.4
4.5
C02
VOLX
MEAS
ft ft ft ft? ft ft 4
10.2
10.0
10.0
10.0
10,3
10.4
10.8
10.4
10.9
10.0
10.1
10.0
10.4
10.7
10.3
11.0
10.7
10.9
11.1
12,2
12.2
10.9
10.4
9.9
10.5
11.9
11.3
11.1
11.1
12.3
-1.0
12.3
12.0
11.9
11.8
10.9
11.1
10.8
10.5
11.4
12.2
12.3
12.2
12.2
12.4
12.4
12.4
12.3
CO
PPMV
MEAS
ft ft? ft ft ft ft 4
23
23
23
23
24
24
25
24
24
22
23
22
24
23
23
24
23
25
27
30
29
24
23
25
25
30
25
26
27
34
-1
34
32
34
34
27
29
25
25
29
29
29
29
29
30
31
31
30
NO
PPMV
MEAS
ft ft ft ft ft ft 4
219
219
219
218
217
218
218
217
219
220
220
221
221
228
225
224
209
214
211
209
201
209
215
207
214
206
214
216
210
209
-1
209
213
209
208
216
212
217
220
212
220
221
223
217
221
224
221
220
CO
PPMV
3X02
ft ft ft ft ft ft 4
31
31
31
31
32
32
32
32
30
30
31
31
32
30
31
30
30
34
34
34
33
31
31
36
33
35
31
33
35
38
0
39
36
38
39
33
35
31
31
34
32
31
32
32
32
33
33
32
NO
PPMV
3X02
ft ft ft ft ft ft f
296
303
303
302
294
293
282
292
282
307
302
311
299
300
307
284
277
292
269
236
229
271
293
298
290
244
269
276
272
238
0
239
239
235
238
266
258
271
281
251
243
241
246
239
241
243
239
240
CO
N6/J
** ** ft*4
• W w W " w»
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
11
11
11
11
10
10
12
11
11
10
11
11
13
0
13
12
12
13
11
11
10
10
U
10
10
10
10
10
11
11
10
NO ACODE
NG/J
ftftftftftftftftftftftft
163
167
167
166
162
161
155
161
155
169
167
171
165
165
169
156
152
161
148
131
126
149
161
164
160
134
IU6
152
150
131
0 C
132
132
129
131
147
142
149
155
138
134
133
135
132
133
133
132
132
**
**
**
**
**
**
t * * *
**
**
**
**
**
**
**
**
**
**
**
**
**
*«
• *
**
**
**
**
ft*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
126
KVBll-6015-1233
-------
ft*
ft*
ft*
ft*
ft*
** DATE
4tftltft£A£VtJtAJt
«* 6/18/80
ft* 6/18/80
ft« 6/16/80
ft* 6/18/80
** 6/18/80
** 6/18/80
«* 6/18/80
** 6/18/80
** 6/18/80
•* 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
«* 6/18/80
ft* 6/18/80
ft* 6/18/80
** 6/18/80
** 6/18/80
** 6/18/80
«* 6/18/80
** 6/18/80
** 6/16/80
** 6/16/60
•* 6/18/80
** 6/16/80
«* 6/18/80
** 6/18/80
** 6/18/80
** 6/18/60
*« 6/16/80
** 6/18/80
** 6/16/60
** 6/18/60
•* 6/16/60
*« 6/18/80
«* 6/18/60
** 6/18/80
** 6/16/60
• * 6/18/60
** 6/18/80
** 6/16/80
•* 6/18/60
IS HIM. DATA
DRY STACK GAS CONCENTRATION
TIME
t it *• *• A *• t
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
1630
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
HWTH
******<
w w w w w w 1
15.2
13.2
11.1
9.4
9.4
12.6
12.0
10.3
8.5
7.9
9.1
8.2
10.8
12.6
12.6
13.6
16.7
14.6
18. «
H.7
14.4
13.5
12.3
12.3
12.0
11.7
11.4
10.3
10.8
10.8
11.4
11.4
11.1
10.8
10.5
10.5
11.4
10.3
10.3
10.5
".7
8.5
9.1
9.4
9.7
13.5
12.6
10.6
02
VOLX
HEAS
> A 4 * * 4 * *
r W W W H w K
4.6
5.1
5.5
6.7
7.5
5.7
.8
.6
.3
.9
.7
.0
.0
.7
.7
.6
.1
.4
4.7
5.9
«.5
4.8
5.1
5.1
5.3
5.3
5.4
6.5
5.7
5.9
5.3
5.5
5.7
5.8
6.2
6.2
5.5
6.2
6.2
6.7
6.6
6.7
6.6
6.5
7.1
4.5
4.5
6.0
C02
VOLX
HEAS
r A ***** 4
V K K W WK II
12.3
11.8
11.5
10.6
10.0
11.5
10.5
10.6
10.0
10.2
10.4
10.1
11.0
12.0
12.0
12.1
12.4
12.2
12.0
11.0
12.2
12.0
11.8
11.7
1 .5
1 .5
1 .4
1 .6
1 .2
1 .0
1 .5
1 .5
1 .3
11.2
11.0
10.9
11.5
10.9
11.0
11.0
10.6
10.5
10.6
10.7
10.2
12.3
12.3
11.1
CO
PPMV
MEA3
t ft 1t It ^k */ *i '
29
29
27
26
25
31
29
28
30
32
32
29
32
34
30
32
31
30
30
28
31
30
29
26
30
30
31
26
27
26
26
29
29
28
27
27
32
30
30
30
32
29
29
27
25
38
34
29
NO
PPMV
MEAS
f *. 1t It */ *• 1k '
221
217
220
219
221
210
218
226
214
210
208
206
205
206
214
214
228
219
213
219
211
213
215
216
216
217
215
212
210
209
207
206
214
215
214
218
210
220
216
215
206
213
216
219
219
203
209
218
CO
PPMV
3X02
t *> *. ft ft ft ft '
31
32
31
32
33
36
36
35
39
40
40
37
38
37
33
35
33
32
33
33
33
33
32
31
34
34
35
32
31
31
32
33
34
33
32
32
37
36
36
37
40
36
36
33
32
41
37
34
NO
PPMV
3X02
t It it ft ft ft ft '
242
245
255
276
295
247
276
282
261
266
262
267
246
227
236
235
242
237
235
261
230
236
243
240
247
248
246
263
247
249
237
241
252
254
260
265
24U
267
263
271
260
266
270
272
284
221
228
261
CO
N6/J
»***<*; *; Al
f W * W W " ™ •
10
11
10
11
11
12
12
11
13
13
13
12
12
12
11
11
11
10
11
11
11
11
11
10
It
11
12
10
10
10
10
Jl
11
11
11
11
12
12
12
12
13
12
12
11
10
13
12
11
NO ACODE
NG/J
tftftftftftftftftftftftft1
133
135
141
152
162
136
152
155
155
148
144
147
135
125
130
129
133
131
129
144
126
130
134
134
136
137
136
145
136
137
130
133
136
140
143
146
134
147
145
149
143
148
149
150
156
122
125
144
*ft
ftft
**
**
**
**
F * * *
**
**
**
**
**
ft*
**
**
**
**
**
**
• *
**
**
**
**
**
**
**
**
• »
**
**
**
**
**
**
• *
**
**
**
**
*•
**
**
*ft
• ft
ft*
**
ft*
«*
**
**
**
**
**
**
127
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
*»«******»*<
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
•* 6/19/80
*• 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
*« 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
«* 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
•* 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
«* 6/19/80
** 6/19/80
*• 6/19/80
** 6/19/80
IS MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
kftft ft ftftft
15
SO
45
100
115
130
145
200
215
230
205
300
315
330
315
400
415
430
445
500
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
1145
1200
LOAD
MNTH
ft it ft ft ** •
10, 3
8.8
9.1
a. s
8.8
12. 3
13.2
12.3
10.5
9.7
8.2
8.8
8.8
.4
.1
.7
.7
.1
.1
10.3
10.0
7.3
8.2
8.8
10.3
10.8
10.0
«».7
12.0
10.8
10.5
11.1
14.9
15.5
13.5
12.3
13.8
12.0
11.1
7.0
5.9
8.8
6.7
15.8
14.9
13.5
12.3
12.3
02
VOLX
HEAS
[ £ £ £ £ Jf £ i
5.6
7.3
6.7
7.1
6.7
7.0
4.5
4.9
5.7
6.3
7.1
7.0
7.3
6.7
6.6
6.6
6.4
7.2
6.9
5.9
*.l
7.2
9.9
6.7
7.1
5.7
7.0
6.5
5.5
6.4
6.3
6.0
5.9
5.1
5.6
5.5
6.1
5.2
6.0
6.3
13.6
9.8
8.9
6.0
4.9
5.0
5.4
6.0
C02
VOLX
HEAS
r 4t ft ft A A ft *
11.4
10.0
10.6
10.2
10.5
10.3
10.3
12.0
U.I
10.9
10.2
10.3
10.1
10.6
10.6
10.6
10.8
10.2
10.4
11.3
u.i
10.2
7.6
10.6
10,3
11.5
10.5
10.9
.7
.0
.1
.4
.3
.9
.5
.6
.0
11.7
11.1
10.7
3.0
7.6
8,6
11.6
12.1
u.»
11.6
11.2
CO
PPMV
MEA3
r ft ft ft ft ft ft <
31
25
28
24
27
29
33
30
27
25
26
27
25
26
25
26
26
26
26
28
29
25
29
32
26
31
29
28
32
29
28
34
27
29
27
25
28
26
31
28
311
11
27
35
31
32
31
31
NO
PPMV
MEAS
rft ft ft ft ft ft i
218
216
212
217
217
216
210
212
219
220
219
216
222
220
215
212
212
210
212
210
212
213
183
205
213
214
214
218
210
219
216
204
219
228
214
216
213
233
210
202
103
182
198
229
214
210
215
212
CO
PPMV
3X02
bftftft ftft*i
36
32
35
31
34
37
36
33
31
30
33
34
32
32
31
32
32
33
33
33
35
32
47
40
33
36
37
34
37
35
34
40
32
32
31
29
33
31
37
34
762
17
40
42
34
36
35
37
NO
PPMV
3X02
iftftftftft ft<
255
284
267
281
273
278
229
237
257
269
284
278
292
277
269
265
261
274
271
250
256
278
297
258
276
252
275
270
244
270
264
245
261
258
250
251
257
265
252
247
252
293
295
275
239
236
248
254
CO
NG/J
k******l
12
11
11
10
11
12
12
11
10
10
11
11
11
11
10
10
10
11
11
11
11
10
15
13
11
12
12
11
12
12
11
13
10
11
10
9
11
10
12
11
255
5
13
14
11
12
12
12
NO
NG/J
k*****
140
156
147
155
150
153
126
130
142
148
156
153
161
152
148
146
144
151
149
138
141
153
164
142
tsa
138
151
149
134
149
146
135
144
142
138
138
142
146
139
136
139
161
162
151
132
130
136
140
********
*«
**
• *
• **
**
**
>*****
»*
**
• *
**
*•
**
**
' **
»»
**
«*
**
*•
«*
**
**
**
*•
**
«*
*•
»*
**
**
**
**
**
«•
**
**
**
**
*«
**
**
**
**
**
• *
**
**
**
**
**
**
**
**
»*
128
KVBll-6015-1233
-------
**
**
**
ft*
*ft
** DATE
AAAAAAAAAAA
** 6/19/80
•* 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
• * 6/19/80
** 6/19/80
«* 6/19/80
•* 6/19/80
** 6/19/80
** 6/19/60
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/60
•• 6/19/80
** 6/19/80
** 6/19/80
** 6/19/60
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/60
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/60
** 6/19/80
** 6/19/80
** 6/19/80
** 6/19/60
** 6/19/80
»* 6/19/80
•* 6/19/80
•* 6/19/80
** 6/19/80
** 6/19/80
** 6/19/80
15 MIN. DATA
DRV STACK GAS CONCENTRATION
TIME
t A A 1k A A 41
1215
1230
1205
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1615
1630
1845
1900
1915
1930
1905
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
MWTH
* * A A A A 1
W W W W w W 1
14,9
15,6
16.1
13.8
12.0
10.5
10.0
10.3
12.0
12.6
11.4
11.4
11.4
12.3
17,0
17.9
17.9
13.2
11.7
11.4
12.0
12.0
10.5
10.3
10.0
10.0
10.5
11.1
11.7
10.8
12.9
14.1
13.8
12.3
12.0
12.0
10.8
10,8
10.5
10.3
10.3
10.5
10.5
10.5
10.5
10.8
12.0
12.0
02
VOLX
MEAS
> £ * A w A A 1
4.7
4.7
«.7
5.4
5.6
6.7
7.2
6.0
5.6
4.9
5.9
5.8
5.7
5.4
4.4
4.2
4.2
5.0
5.9
5.9
5.6
5.5
6.5
6.6
.7
.7
.2
.0
.6
.6
.7
4.8
5.0
5.5
5.6
5.7
6.1
5.8
6.3
6.6
6.4
6.8
5.6
5.8
6.0
5.3
4.7
4.8
C02
VOLX
MEAS
t * A A A A A i
« W W W W W wl
12.2
12.2
12.3
11.8
11.7
10.9
10.0
11.1
11.5
12.0
11.2
11.3
11.3
11.6
12.4
12.5
12.5
.9
.2
.2
,5
.*
.«
10.7
10.5
10.6
11.0
11.2
11.5
11.4
11.0
12.1
12.0
11.6
11.5
11.5
11.1
11.4
10.9
10.7
10.9
10.6
11.5
11.4
11.2
11.7
12.2
12.2
CO
PPMV
MEAS
1 A A A A A A'
32
31
31
30
31
29
27
30
31
32
30
31
31
32
31
31
30
30
29
29
29
31
29
26
29
26
30
31
30
29
28
28
28
27
27
28
27
29
27
27
31
31
29
28
27
28
31
30
NO
PPMV
MEAS
1 A A A A A A i
216
216
243
217
216
222
225
223
221
228
230
231
232
226
241
254
252
235
232
235
233
230
226
221
221
223
223
223
226
231
229
229
226
231
231
230
232
230
231
236
227
224
231
225
221
222
212
215
CO
PPMV
3X02
1 A A A A A Ai
35
34
34
34
36
36
35
36
36
35
35
36
36
36
33
33
32
33
34
34
33
36
36
35
36
35
36
37
35
33
32
31
31
31
31
32
32
34
33
33
38
39
33
33
32
32
34
33
NO
PPMV
3X02
' A A A A A A*
236
238
268
250
255
279
293
267
256
255
274
273
273
260
261
272
270
264
276
2SO
272
267
280
276
278
281
271
267
264
270
269
254
254
268
270
270
260
272
263
295
260
284
270
266
265
254
234
239
CO
NG/J
b * * A A 4 A 1
[ W A A A« w "
11
11
11
11
12
12
11
12
12
12
12
12
12
12
11
11
10
11
11
11
11
12
12
11
12
11
12
12
11
11
11
10
10
10
10
11
10
11
11
11
12
13
11
11
10
10
11
11
NO ACODE
NG/J
!^4AA4***+***I
[WWWWWWKWWIIWW
131
131
146
136
140
154
162
147
142
140
151
150
150
143
144
150
146
145
152
154
ISO
147
154
152
153
155
149
147
145
149
148
140
140
148
149
149
154
ISO
156
162
154
156
149
147
146
140
129
131
**
• «
**
**
*»
ft«
r * A A
[WWW
**
**
**
**
**
**
**
**
**
**
**
**
**
«*
**
ft*
**
**
**
«»
**
• *
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
• *
**
**
ft*
**
**
**
**
**
**
129
KVBll-6015-1233
-------
**
**
**
**
ft*
** DATE
ft**********4
** 6/20/80
** 6/20/80
** 6/20/80
•* 6/20/60
** 6/20/80
** 6/20/80
*» 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
ft* 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
*« 6/20/80
** 6/20/80
** 6/20/80
»* 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
•* 6/20/80
** 6/20/80
** 6/20/60
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/60
** 6/20/80
15 HIN. DATA
DRY STACK GAS CONCENTRATION
TIME
*******
15
30
45
100
115
130
145
200
215
230
245
300
315
330
345
400
415
430
445
500
51S
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
******'
12.0
13.2
9.4
9.1
9.7
9.7
10,3
10.3
9.7
9.1
9.1
9.4
9.7
9.7
10.0
10.0
9.4
8.8
«,2
8.5
H.7
10.8
9.4
10.0
12.6
12.6
12.3
10.0
10.3
12.3
11.7
13.2
15.5
13.5
12.9
12.9
11.7
11.1
U.7
12.9
13.2
13.8
14.4
12,9
10.5
10.5
10.5
10.8
02
VOLX
MEAS
t ******'
4.9
4.8
6.8
7.0
6.8
6.4
5.9
6.3
6.3
6.8
7.5
6.4
6.5
6.0
5.9
6.3
6.5
7.4
7.4
7.1
5.5
5.5
6.6
7.4
5.4
5.4
5.4
6.3
7.3
5.8
5.7
4.8
.4
.6
.8
.1
.9
5.4
5.3
5.1
4.8
4.7
4.6
4.8
5.7
6.2
6.0
6.0
C02
VOLt
MEAS
[******'
12.1
12.2
10.5
10.4
10.5
10.9
11.3
11.0
10,9
10.5
9.9
10.9
10,8
n. a
11.3
11.0
10.8
10.0
10.0
10.3
11.6
11.6
10.8
10.1
11.7
11.7
11.7
11.0
10.1
11.6
11.5
12.2
12.4
12.3
12.2
11.1
12.1
11.6
11,7
11.9
12.1
12.2
12,3
12.1
11.4
11.0
11.2
11.1
CO
PPMV
MEAS
F 4 + + •*** 4
r W W w W w If
30
32
26
26
29
28
29
28
27
26
26
28
26
28
28
29
28
27
26
30
37
33
29
29
26
27
28
28
26
30
31
35
36
27
33
21
32
30
26
31
31
29
29
29
27
27
27
31
NO
PPMV
MEAS
!******]
219
216
225
224
226
232
226
226
230
231
230
230
228
231
228
230
233
224
219
217
209
219
223
219
231
232
236
242
233
236
237
224
224
222
229
244
233
234
235
230
229
231
229
236
240
240
233
223
CO
PPMV
3X02
r*** ***'
33
35
35
36
36
34
34
34
33
33
34
34
32
33
33
35
34
35
37
SB
43
38
36
38
32
31
32
34
34
35
36
38
39
29
36
25
35
34
32
35
34
32
31
32
31
32
32
37
NO
PPMV
3X02
k******1
245
240
285
286
286
286
269
279
261
293
307
263
263
277
272
261
269
297
290
261
242
254
279
290
266
267
274
296
306
279
279
249
243
243
254
295
260
270
269
260
254
255
251
262
282
292
279
267
CO
NG/J
tftft****<
It
11
11
12
12
11
11
11
11
11
12
12
13
14
12
12
12
10
to
10
11
11
11
12
13
13
9
12
6
12
11
to
11
11
10
10
10
10
11
10
12
NO ACQDE
NG/J
k************i
135
132
157
159
158
157
148
154
155
161
169
156
156
153
150
155
159
163
160
155
133
140
153
160
147
147
151
163
169
154
153
137
133
134
140
162
143
149
148
143
140
140
138
144
155
161
154
147
**
**
**
**
**
• •
*** *
**
**
**
**
**
**
**
ft*
**
ft*
**
ft*
**
ft*
**
**
**
**
**
**
ft*
**
**
**
**
ft*
ft*
**
«*
**
**
ft*
**
**
**
**
**
• *
• *
**
**
**
**
**
**
**
**
**
130
KVB11-6015-1233
-------
**
ft*
**
ft*
ft*
** DATE
AAAAAAAAAAA
** 6/20/eo
** 6/20/80
** 6/20/BO
** 6/20/80
** 6/20/80
•ft 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
ft* 6/20/80
** 6/20/60
ft* 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/SO
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
ft* 6/20/80
** 6/20/80
** 6/20/80
•* 6/20/80
ft* 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
•* 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
ft* 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
** 6/20/80
•* 6/20/80
15 HIN. DATA
DRY STACK GAS CONCENTRATION
TIME
L A * * + A *
[ W W W W W W
1215
1230
12U5
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1S45
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
2315
2330
2345
2400
LOAD
MWTM
A A A A A A '
14.4
16.4
16.7
12.3
14.1
12.9
11.7
13.2
11. «
10.0
9.7
10.3
10.3
'.7
9.4
9.4
13.2
12.9
10.3
10.8
10.5
9.7
9.1
9.1
10.3
10.3
10.3
10.3
10.3
10.0
9.7
9.7
9.7
10.3
10.8
10.8
10.8
9.7
10.0
10.0
10.3
10.3
10.3
10.8
10.3
10.0
9.4
9.1
02
VOLX
MEAS
I A A A A A; A '
4.7
4.3
4.2
5.0
5.5
5.9
6.2
5.3
5.2
.1
.6
.1
.5
.3
7.0
7.0
4.7
4.7
5.9
6.2
5.8
7.1
7.1
7.3
6,1
5.7
5.9
6.2
6.1
6.1
6.8
6.6
6.5
6.1
6.0
5.4
6.1
6.6
6.6
6.5
5.9
6.2
5.7
5.8
6.2
6.5
7.1
7.3
C02
VOLX
MEAS
r A A A A A A '
12.2
12.4
12.5
11.9
11.5
11.2
10.9
11.7
11.7
11.0
10.6
10.6
10.7
10.8
10.2
10.2
12.0
12.1
11.2
10.9
11.2
10.2
10.2
9.9
11.0
11.3
11.1
tl.O
11.0
11.)
10.5
10.6
10.7
11.1
11.2
11.6
U.I
10.6
10.6
10.7
1.2
1.0
1.4
1.3
0.9
10.7
10.2
10.0
CO
PPMV
MEAS
f A A A A A A '
33
32
31
29
29
29
26
31
29
26
27
13
27
26
26
26
32
30
26
24
26
23
24
23
25
26
26
26
26
26
24
23
23
22
22
24
23
22
23
23
27
24
25
25
25
25
23
23
NO
PPMV
MEAS
[ A A A A A Al
216
220
234
231
243
234
241
230
239
250
247
224
230
235
233
232
216
223
236
232
227
230
229
230
229
231
231
227
226
225
228
232
238
239
235
236
238
240
234
234
230
232
230
235
236
237
235
235
CO
PPMV
3X02
r A A * A 4 A 1
' W W W W W K 1
36
34
33
32
33
34
34
35
33
31
33
15
33
31
33
33
35
33
31
29
30
29
31
30
30
30
31
31
31
31
30
28
26
26
26
27
27
27
28
28
32
29
29
29
30
31
29
30
NO
PPMV
3X02
, ^ A * * * A t
' W • H 11 W IV 1
238
237
250
260
262
279
293
263
272
302
309
270
265
286
300
298
240
246
281
282
269
298
297
302
276
272
275
276
273
272
289
290
295
269
262
272
287
300
292
290
274
282
270
278
287
294
304
309
CO
NG/J
> A A A A 4 Al
' W W W 11 w w 1
12
11
11
10
11
11
11
11
11
10
11
5
11
10
11
11
11
11
10
9
10
10
10
10
10
10
10
10
10
10
10
1
10
10
10
10
NO ACODE
NG/J
lAAAAAAAAAAAAi
131
130
136
143
155
153
161
145
150
166
170
149
157
156
165
164
132
135
155
155
148
164
163
166
152
150
152
152
150
150
159
160
163
159
155
150
156
165
161
160
151
155
149
153
156
162
168
170
**
**
**
**
**
*«
i ft ft ft
**
**
**
**
**
**
**
**
**
**
**
**
ft*
**
**
**
**
**
**
**
**
ft*
**
**
**
**
*•
ft*
**
**
**
**
**
**
«*
**
**
**
**
**
**
**
**
**
**
**
**
**
131
KVBll-6015-1233
-------
ft*
ft*
**
**
**
**
**!
ft*
ft*
ft*
ft*
**
ft*
ft*
**
ft*
**
**
**
**
**
**
**
**
**
**
**
**
ft*
**
**
**
**
ftft
ft*
**
**
**
**
**
**
ftft
**
**
ft*
**
**
**
**
**
**
**
**
**
**
15 MIN, DATA
DRY STACK GAS CONCENTRATION
DATE
rftftftftftftftftl
6/21/80
6/21/80
6/21/80
6/21/80
6/21/60
6/21/80
6/21/80
6/21/80
6/21/80
6/21/80
6/21/80
6/21/60
6/21/80
6/21/80
6/21/60
6/21/60
6/21/80
6/21/80
6/21/80
6/21/60
6/21/80
6/21/80
6/21/80
6/21/80
6/21/80
6/21/80
6/21/80
6/21/80
6/21/60
6/21/80
6/21/80
6/21/80
6/21/60
6/21/80
6/21/80
6/21/80
6/21/80
6/21/80
6/21/60
6/21/60
6/21/60
6/21/60
6/21/80
6/21/80
6/21/60
6/21/60
6/21/60
6/21/80
TIME
ft ft ft ft ft ft
15
30
45
too
115
130
145
200
215
230
245
300
315
330
345
400
415
430
445
500
515
530
545
600
615
630
645
700
715
730
745
600
815
830
845
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1 145
1200
LOAD
MMTH
A ik * * A A 4
» W W W W W 1
8.6
9.1
9.1
9.7
9.4
8.6
7,9
7.9
7.6
7.6
6.2
10.3
9.7
6.8
7.9
7.9
8.5
8.2
6.2
7.0
6.4
6,4
5.9
5.9
7.3
7.3
7.6
7.3
7.6
10.5
16,1
10.8
10.8
11."
10.8
10.6
17,0
20.2
19,6
16.7
15.2
14.6
10.5
9.7
9.1
8.6
6.2
6.2
02
VOLX
MEAS
' ft ft ft ft ft ft 1
7.0
6.6
6.4
6.3
6.9
7.6
7.5
7.5
7.5
7.5
6.1
5.8
6.9
7.5
7.4
7.5
7.2
7.1
7.4
7.8
11.4
9.6
10.7
10.7
8.4
7.5
7.7
7.6
7.1
4.6
4.0
6.0
5.2
4.9
5.3
4.5
4.0
4.0
4.3
4.5
4.3
5.5
6.7
7.0
7.3
7.4
7.3
7.3
C02
VOLX
MEAS
ft ft ft ft ft ft 1
10.3
10.7
10,9
10.9
10.4
9.8
9.8
9.8
9.8
9.7
11.1
11.3
10.4
9.9
9.9
9.9
10.1
10.2
10.0
9.6
5,5
7.5
6.8
6.8
8.8
9.7
9.6
9.5
10.2
12.3
12.6
11.2
11.9
12.1
11.6
12.4
12.8
12.7
12.6
12.4
12.5
11.7
10.5
10.3
10.1
9.9
10.0
10.0
CO
PPMV
MEAS
1 ft ft ft ft ft ft 1
23
24
24
23
22
22
23
23
23
24
26
26
24
24
23
23
23
22
22
22
143
40
43
44
39
23
23
23
24
27
24
22
27
27
25
26
25
25
25
24
26
25
23
23
21
20
20
20
NO
PPMV
MEAS
! ft ft ft ft ft ft 1
234
236
236
238
239
234
230
231
231
229
230
233
235
233
231
232
234
237
235
229
139
179
171
175
209
230
234
230
226
232
249
237
226
226
230
243
304
289
258
239
230
238
241
236
231
231
236
239
CO
PPMV
3X02
ft ft ft ft ft ft 1
29
30
29
28
28
29
30
30
30
32
31
30
30
32
30
30
30
28
29
30
267
63
75
77
55
30
31
31
31
29
25
26
30
30
26
28
26
26
26
26
26
29
28
29
27
26
26
26
NO CO
NO ACODE
PPMV NG/J NG/J
3X02
t^^AAAAAA^,^A^A.^j
fftftftftftftftftftftftll*"** m m m. m mm m m rt m m m. i
301 9 166
295 10 162
291 9 160
291 9 160
305 9 166
314 9 173
307 10 169
308 10 170
306 10 170
305 10 168
276 10 153
276 10 152
**
**
ft*
**
**
ft*
r A «k «b
r w K M
**
**
**
**
**
**
**
**
**
**
**
**
300 10 165 **
311 10 171 ft*
306 tO 168
309 10 170
305 10 166
307 9 169
311 9 171
312 10 172
261 89 144
263 21 156
300 25 165
307 25 169
299 10 165
307 10 169
317 10 174
314 10 173
295 10 163
254
263
264
259 1
252 1
263
265
321
306
278
260
246
276
303
303
304
140
145
156
143
139
145
146
177
168
153
143
136
152
167
167
167
306 6 166
313 8 172
314 6 173
**
**
**
**
**
**
*•
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
132
KVBll-6015-1233
-------
**
**
**
ft*
ft*
** DATE
AAAAAAAAAAA'
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
•* 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
*» 6/21/80
•* 6/21/60
** 6/21/80
»* 6/21/80
** 6/21/80
»* 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
»* 6/21/80
** 6/21/80
** 6/21/80
•* 6/21/80
** 6/21/60
** 6/21/80
** 6/21/80
ft* 6/21/80
** 6/21/80
** 6/21/80
•* 6/21/80
** 6/21/80
ft* 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
** 6/21/80
15 HIN. DATA
DRY STACK GAS CONCENTRATION
TIME
r 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
1800
1615
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
MtuTH
A A A AA Al
8.2
9.4
10.0
10.0
12.9
12.9
12.3
6.4
5.6
5.9
,2
.2
.2
.2
.2
5.9
5.9
6.2
6.2
6.2
6.2
6.2
5.9
5,
5.
5.
5.
5.
5.
6.2
6.2
6.2
*.?
6.2
6.2
6.2
6,2
6.2
6,2
6.2
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
02
VOLX
HEAS
' A A A A A A 1
7.3
5.8
6,1
4.5
4.6
4.7
10.6
12.7
11.8
10.3
10.1
9.8
9,9
9.6
10.1
10.8
10.0
9.8
9.7
9.9
9.7
10.3
11.0
11.1
11.8
12.2
13.1
12.8
12.8
13.1
12.9
12.6
13. 1
12.6
13.0
13.1
13.2
13.1
13.1
13.4
1.0
1.0
1.0
.0
.0
.0
.0
.0
C02
VOLX
HEAS
r A A A A A Ai
10.1
11.3
11.1
12.3
12,3
12.3
6,1
3,8
4.8
6.7
6.9
7.2
7.0
7.4
6.7
5.9
6.9
7.1
7.3
7.0
7.2
6.5
5.6
5.4
4.6
4.1
2.7
3.4
3.5
3.0
3.5
3.8
3.1
3.7
3.7
3.9
3.8
3.9
3.9
3,5
.0
.0
.0
.0
.0
.0
.0
.0
CO
PPHV
HEAS
r A A A A A Al
21
23
23
27
26
26
46
65
72
25
25
24
22
22
21
61
21
21
22
22
22
28
49
49
136
160
172
164
164
237
201
169
226
154
156
129
148
140
143
221
NO
PPHV
HEAS
! A A A A A A]
236
242
240
224
218
218
171
139
130
193
199
201
200
204
198
171
198
200
202
198
198
189
157
155
136
142
124
128
129
116
122
129
118
129
128
131
126
128
128
121
1
1
CO
PPHV
3X02
r A A A A A Al
27
27
27
29
28
28
79
185
141
42
41
38
35
34
34
108
34
33
35
35
35
47
88
89
267
329
394
362
362
543
449
364
518
332
353
296
344
321
328
527
0
0
0
0
0
0
0
0
NO
PPHV
3X02
' A A A A A A 1
313
286
290
244
239
240
297
303
255
325
329
324
325
323
328
303
325
322
322
322
316
319
283
283
267
292
284
282
285
266
272
278
270
278
290
300
292
293
293
288
0
0
0
0
0
0
0
0
CO
NG/J
b * * * * 4 * (
1 • A w W W W P
26
62
47
14
13
12
12
11
11
36
11
11
11
12
11
15
29
30
89
110
132
121
121
182
150
122
174
111
118
99
115
107
110
177
0
0
0
0
0
0
0
0
NO
NG/J
1 A A A A Al
172
158
160
134
132
132
163
167
141
179
181
178
179
178
180
167
179
177
178
177
174
175
156
156
147
161
156
155
157
146
ISO
153
149
153
159
165
161
161
161
159
0
0
0
0
0
0
0
0
ACODE
t A A A A A
c
c
c
c
c
c
c
c
ft*
**
**
ft*
*«
**
ft***
• ft
ft*
**
• ft
**
**
**
**
ft*
**
**
**
**
**
**
**
**
**
/ **
**
**
ft*
*«
**
**
**
*«
**
**
**
**
**
**
**
**
*•
• *
**
**
**
ft*
**
**
**
**
**
**
133
KVBll-6015-1233
-------
**
• ft
**
**
**
**
15 MIN. DATA
DRY STACK GAS CONCENTRATION
02 C02 CO NO
LOAD VOL* VOLX PPMV PPMV
DATE
TIME
MHTH MEAS MEAS MEAS MEAS
CO
PPMV
3X02
NO
PPMV
3X02
CO
NG/J
NO
NG/J
ACODE
**
**
**
**
**
ft*
***"************************************ft***ft****ft***««***ft**ft»ftft*»**ftft****ftftft*********»ftft
ft*
**
**
**
**
**
**
**
**
ft*
**
**
**
**
**
**
*ft
**
ft*
ft*
*»
**
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
**
**
ft*
ft*
**
ft*
• ft
*«
ft*
ft*
**
ft*
**
ft*
ft*
**
**
ft*
6/23/80
6/23/60
6/23/80
6/23/80
6/23/60
6/23/80
6/23/80
6/23/80
6/23/60
6/23/80
6/23/80
6/23/80
6/23/80
6/23/80
6/23/60
6/23/80
6/23/80
6/23/80
6/23/80
6/23/80
6/23/80
6/23/60
6/23/60
6/23/60
6/23/80
6/23/80
6/23/60
6/23/60
6/23/80
6/23/80
6/23/60
6/23/80
6/23/80
6/23/60
6/23/80
6/23/60
6/23/60
6/23/60
6/23/60
6/23/80
6/23/80
6/23/80
6/23/80
6/23/80
6/23/80
6/23/60
6/23/80
6/23/60
IS
30
45
100
115
130
145
200
215
230
245
300
315
330
345
400
415
430
445
500
515
530
545
600
615
630
645
700
715
730
745
600
815
830
845
900
-------
**
**
**
**
ft*
** DATE
ftft/ftrftftftftftftftft
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/60
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/60
** 6/23/80
** 6/23/60
** 6/23/80
** 6/23/60
** 6/23/80
*ft 6/23/80
ft* 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/60
** 6/23/60
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/80
** 6/23/60
** 6/23/60
** 6/23/60
** 6/23/60
15 MIN, DATA
DRY STACK GAS CONCENTRATION
TIME
t ft ft ft ft ft 11
1215
1230
1245
1300
1315
1330
13a5
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
2330
2345
2400
LOAD
MWTH
ft ft ft ft ft ft '
12.0
12.0
11.1
11.7
10.5
9.1
7.9
7.6
7.6
6.2
10.6
13.2
12.9
12.9
12.3
12.6
13.5
11.4
15.2
16.2
15.5
14.9
14,4
»«.!
11.4
10.3
9.7
'.7
10.8
14.4
15,6
12. »
12.0
11.1
10.3
10.0
10.0
10.0
10.5
».7
10.3
10,8
10,0
10.0
12.6
11.4
11.7
10.0
02
VOLX
MEAS
r ft ft ft ft ft ft '
6.1
5.8
5.9
5.6
6.1
7.1
7.6
8.3
6.1
7.4
5.6
5.3
5.5
5.6
5.5
5.1
6.9
6.6
5.2
5.5
6.0
6.1
6.0
6.4
6.8
7.1
7.5
7.2
6.8
6.0
5.9
6.4
6.6
6.7
6.8
6.8
7.1
6.9
6.8
6.9
7.0
6.8
7.3
6.8
6.5
6.8
6.8
7.1
C02
VULX
HEAS
t ft 1t ft ft ft ft '
II. 1
11.4
11.3
11.5
11.2
10.7
9.6
9.1
9.7
10.0
11.6
11.6
11.
11.
11.
11.
10.
10.
11.
11.
11.2
11.1
11.2
10.9
10.5
10.3
9.9
10.2
10.5
11.2
11.3
10.9
10.7
10.7
10.5
10.5
10.3
10.5
10.5
10.5
10.4
10.5
10.1
10,6
10,9
10.6
10.6
10.3
CO
PPMV
HEAS
[ ft ft ft ft ft ft
28
30
31
32
34
32
30
28
24
28
26
25
25
25
25
36
23
23
26
26
23
23
22
21
20
20
20
20
21
21
22
21
21
22
21
22
20
20
19
20
20
20
18
19
19
20
20
20
NO
PPMV
HEAS
t ft ft A ft ft ft '
236
230
232
230
231
233
230
225
235
230
244
249
251
252
251
231
262
259
221
242
273
266
257
264
259
256
252
258
256
257
257
260
262
261
251
252
251
252
256
257
256
260
253
256
260
255
259
257
CO
PPMV
3X02
(ft ft ft ft ft ft '
33
35
36
37
41
41
40
39
33
37
30
28
29
29
29
40
29
28
31
30
27
27
26
25
25
25
26
26
26
25
26
25
26
27
26
27
25
25
24
25
25
25
23
24
23
25
25
25
NO
PPMV
3X02
rft ft ft ft ft ft1
285
272
276
269
279
302
309
319
326
304
265
285
291
294
291
26]
334
324
251
281
327
321
308
325
328
332
336
337
324
308
306
320
327
329
318
319
325
322
324
328
329
330
332
327
323
323
326
333
CO
NG/J
b A A A * * * 1
r ft ft • w w w>
it
it
12
12
13
13
13
13
11
12
10
9
9
9
9
13
9
9
10
10
9
9
8
8
8
8
8
8
8
6
8
8
8
9
8
9
8
8
8
a
8
8
7
6
7
8
6
8
NO ACOOE
NG/J
>*A4* + ***4*4*<
[HWwWWwHWWWWWl
157
150
152
148
154
166
170
176
181
168
157
157
160
162
160
144
184
178
138
155
180
177
170
179
161
163
185
185
179
170
169
176
180
181
175
176
179
177
179
181
181
182
183
180
178
178
181
183
**
**
**
**
**
**
> 4 A *
r W m •
**
*«
**
**
**
**
**
**
**
**
**
• *
**
*•
ft*
ft*
**
«*
ft*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
«*
**
**
**
**
**
**
**
**
**
135
KVBll-6015-1233
-------
**
**
**
**
ft*
** DATE
ft***********
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/BO
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
ft* 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
*« 6/24/80
ft* 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
ft* 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
«* 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
ft* 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
ft* 6/24/80
** 6/24/80
** 6/24/80
•* 6/24/80
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
tftft* * ftft
15
30
45
100
115
130
145
200
215
230
245
300
315
330
345
400
415
430
445
500
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
1145
1200
LOAD
MWTH
it ft ft ft~ft ft'
9.7
9.7
9.4
9.1
9.1
9.4
9.7
10.0
10.0
10.0
.1
.1
.1
.1
.4
.<*
,4
.7
10.0
10.0
9.7
7.9
12.3
10.8
7.6
7.9
10.3
10.3
9.7
8.2
10.0
11.7
12.3
14.6
14.1
13.5
13.8
14,9
15.5
14.6
10.5
12.6
14.4
13.8
11.7
9.1
8.5
e.5
02
VOLX
MEAS
r ft A ft ft ft ft
7.4
7.6
7.4
7.7
7.5
7.0
7.1
6.9
6.9
7.4
7.5
7.7
7.5
7.3
7.4
7.1
7.1
6.8
7.1
6.8
7.7
7.7
6.5
7.7
7.7
7.5
6.9
6.9
7.7
8.4
6.9
6.5
5.7
5.4
5.6
5.7
5.5
4.8
4.8
5.4
6.4
5.0
«.9
5.1
6.1
6.9
7.1
6.5
CQ2
VOLX
MEAS
b *k tfr th * 4 *fr <
• W W ft W W W 1
10.0
9.8
10.0
9.7
9.9
10.3
10.3
10.4
10,5
10.0
9.9
9.7
9.9
10.0
9.9
10.2
10.3
10.6
10.2
10.5
9.8
9.8
10.8
9.7
9.7
9.9
10.5
10.5
9.8
9.1
10.5
10.8
11.5
11.8
11.7
11.6
11.7
12.3
12.3
11.8
11.0
12.1
12.1
11.9
11.1
6.9
10.2
10.7
CO
PPMV
MEAS
'ft ft ft ft ft ft 1
20
19
19
18
18
18
18
19
19
18
19
19
19
20
20
20
20
19
18
19
20
19
19
19
21
20
20
21
20
19
21
20
20
20
20
20
21
21
23
28
27
27
24
27
25
26
25
26
NO
PPMV
MEAS
kftftft ft* ft j
251
250
253
244
248
254
258
252
251
252
243
242
245
240
247
251
252
256
256
258
242
248
264
248
243
251
258
254
246
232
245
255
246
257
241
240
247
245
246
246
243
239
229
225
231
229
228
229
CO
PPMV
3X02
*******<
26
25
25
24
24
23
23
24
24
23
25
25
25
26
26
25
25
24
23
24
27
25
23
25
28
26
25
26
27
27
26
24
23
23
23
23
24
23
25
32
33
30
26
30
30
33
32
32
NO
PPMV
3X02
k******<
332
336
335
330
331
327
334
322
320
334
324
328
327
315
327
325
326
324
332
327
328
336
328
336
329
335
329
324
333
332
313
316
289
296
281
282
287
272
273
284
299
269
256
254
279
292
295
284
CO
NG/J
»******<
8
8
8
8
8
7
7
8
8
8
8
8
8
8
8
8
8
8
7
8
9
8
7
8
9
8
8
9
9
9
9
8
7
7
7
7
8
7
8
10
11
10
9
10
10
11
10
10
NO ACODE
NG/J
i************
183
185
184
182
182
180
164
177
176
184
170
180
180
174
180
179
180
179
183
180
180
IBS
180
185
181
184
181
179
183
183
172
174
159
163
155
155
158
150
150
156
165
148
141
140
154
161
163
156
**
**
**
**
**
ft*
»***
ft*
**
**
**
**
**
**
**
**
**
**
ft*
**
*ft
**
**
**
ft*
**
*•
ftft
**
**
ft*
**
**
**
**
**
**
ft*
ft*
**
*«
**
**
**
**
**
**
**
**
**
**
**
**
**
136
KVBll-6015-1233
-------
**
**
ft*
ft*
ft*
•* DATE
ftft/ftjftftftftftftftft
** 6/21/80
** 6/24/80
** 6/20/80
** 6/24/80
** 6/24/80
ft* 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/60
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
** 6/24/80
*ft 6/24/80
** 6/24/80
•* 6/24/80
** 6/24/80
** 6/24/80
•* 6/24/60
** 6/24/80
** 6/24/80
** 6/24/60
** 6/24/80
** 6/24/80
•* 6/24/80
** 6/24/60
** 6/24/80
** 6/24/60
** 6/24/80
** 6/24/80
** 6/24/60
15 WIN. DATA
DRY STACK GAS CONCENTRATION
TIME
k ft ft ft ft ft M
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
1630
1645
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
MKTH
Jb £ £ £ £ £ ,
8.5
8.2
7.9
6.8
10.5
8.8
7.9
9.4
9.7
9.4
13.5
18.8
16.2
17.9
16.4
18.8
16.8
17.0
14.4
12.3
11. t
11.1
10.0
10.0
9.7
10.3
10.5
10.3
10.5
10.3
10.3
9,7
9.7
10,0
10.3
10.5
10.0
10.0
9.1
8.8
8.6
9.7
9.7
9,7
9.7
e.8
8.8
B.8
02
VOLX
HEAS
' It ft It ft ft/ ft '
7.0
7.1
7.0
5.5
6.2
7.1
6.9
5.5
6.1
5.6
4.9
5.3
5.0
5.2
5.0
5.6
5.0
5.8
5.6
6.1
6.2
6.5
6.7
7.2
6.5
6.3
.3
.1
.0
.3
.2
.8
.5
.2
.2
.1
.0
.8
7.1
7.3
7.1
6.5
6.7
6.4
6.4
7.1
7.1
7.0
C02
VOLX
MEAS
r ft ft ft ft ft ft '
10.2
10.2
10.2
11.6
11.0
10.2
10.3
11.5
11.0
11.4
12.0
11.7
12.0
11.8
12.0
11.5
11.9
11.3
11.4
11.1
10.9
10,7
10.5
10.1
10.7
10.8
10.8
11.0
11. 1
10.9
11,0
10.4
10.7
10.9
11,0
11.0
11.1
10.4
10.2
10.0
10.2
10.7
10,5
10.6
10.8
10.2
10.2
10.2
CO
PPMV
HEAS
1 ftft ft ft ft ft '
24
23
22
30
25
24
27
25
26
26
38
26
27
23
31
23
26
23
29
24
20
20
19
19
20
20
20
20
21
19
20
19
20
21
20
20
20
19
19
20
20
20
19
20
20
19
19
18
NO
PPMV
HEAS
r It ft ft 1t It ft i
229
229
227
224
236
231
225
234
239
240
222
223
223
235
225
230
215
239
235
245
251
253
250
249
249
252
253
252
248
245
246
245
249
246
249
246
242
245
243
243
245
242
243
246
244
239
236
235
CO
PPMV
3X02
rft ft ft ft ft ft :
30
29
28
34
30
31
34
29
31
30
42
29
30
26
34
26
31
27
33
29
24
24
23
24
24
24
24
24
25
23
24
24
24
25
24
24
24
24
24
26
25
24
23
24
24
24
24
23
NO
PPMV
3X02
t ftft ft ft ft ft '
294
297
292
260
289
299
287
271
289
280
248
255
251
267
253
269
242
283
274
296
305
314
315
325
309
308
310
304
297
300
299
311
309
299
303
297
290
311
315
319
317
300
306
303
301
310
306
302
CO NO ACDDE
NG/J NG/J
rftftftftftftftftft/ftftftftftftftftftftl
10 162
10 163
9 161
11 143
10 159
10 165
11 156
9 149
10 159
10 154
14 136
10 141
10 136
8 147
11 139
9 148
10 133
9 156
11 151
9 163
6 168
173
173
179
170
170
171
168
164
165
165
171
170
165
167
164
160
171
173
176
175
165
6 168
8 167
6 166
a 170
8 168
7 166
**
**
**
• *
**
**
r* ft ft
ft*
**
ft*
**
**
ft*
ft*
**
**
**
**
**
**
**
**
ft*
ft*
**
**
**
ft*
**
**
• ft
ft*
**
**
ft*
**
**
**
**
**
ft*
ft*
**
**
ft*
• ft
• ft
**
*«
ft*
ft*
**
**
**
**
137
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
***********<
«* 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
«* 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
»* 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
»* 6/25/80
** 6/25/80
** 6/25/80
** 6/25/60
** 6/25/60
** 6/25/80
** 6/25/60
** 6/25/80
** 6/25/60
** 6/25/80
** 6/25/80
** 6/25/80
«* 6/25/80
•* 6/25/80
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
t******
15
30
45
100
115
130
145
200
215
230
245
300
315
330
345
400
415
430
445
500
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
1145
1200
LOAD
MWTH
*******
19.0
17,0
13.2
9.4
9.7
9.4
6.8
10.3
8.8
9.«
9.7
9.7
'.7
9.7
8.2
6.2
9.1
9.1
9.7
9.7
».2
6.7
6.2
5,6
6.4
7.3
7.6
7.9
10.0
7.0
10.8
14.6
16.1
16.1
13.2
12.6
13.5
10.3
10.3
10.0
11.1
6.8
11.7
11.7
10.6
10.3
11.1
10.0
02
VOLX
MEAS
F ft ft ft ft ft ft •
4.7
6.0
6.7
6.7
6.7
7.4
7.6
7.0
7.6
6.7
6.8
6.9
6.6
6.7
7.6
7.7
6.9
6.9
6.6
6.9
7.1
8.4
10.8
10.6
9.8
7.4
7.9
8.6
7.5
9.4
7.3
6.5
6.6
5.6
5.7
5.6
5.5
6.6
7.0
6.9
7.1
.1
.3
.3
.5
.7
.4
6.6
C02
VULX
MEAS
r ft ft ft ft ft ft •
12.2
11.2
10.5
10.5
10.5
9.9
9.7
10.3
9.7
10.5
10.4
10.4
10.6
10.5
9.7
9.6
10.3
10.3
10.7
10.3
10.2
8.8
6.1
6.1
7.2
9.7
9.3
6.6
9.8
7.7
10.0
10.7
10.7
11.5
11.4
11.6
11.6
10.6
10.3
10.4
10.2
".1
11.0
11.0
10.8
10.6
10,8
10.7
CO
PPMV
MEAS
i * * * *; * A '
41
19
18
19
20
19
19
20
18
18
17
17
17
17
16
16
17
17
19
19
19
20
24
26
24
21
23
17
20
16
21
28
38
34
34
42
35
36
32
30
26
24
26
27
26
26
27
27
NO
PPMV
MEAS
r ft A ft A A A
203
244
257
244
247
243
244
243
239
243
243
240
249
249
248
246
254
259
252
252
250
236
185
184
19a
234
239
244
234
216
232
226
221
230
224
212
223
215
218
224
235
239
254
260
251
250
249
250
CO
PPMV
3X02
t ft ft ft ft ft; ft '
45
22
22
23
25
25
25
25
24
22
21
21
21
21
21
21
21
21
23
24
24
28
42
45
38
27
31
24
26
28
27
34
47
39
40
49
40
47
41
38
33
33
31
33
32
32
33
33
NO
PPMV
3X02
tftftftft ftftl
224
293
323
307
311
322
328
312
321
306
308
306
311
313
333
333
324
331
315
322
324
337
327
319
312
310
329
355
312
336
305
280
276
269
263
248
259
269
280
286
304
334
311
318
312
315
307
312
CO
NG/J
********
15
7
7
8
7
7
7
7
7
7
7
7
7
7
8
8
9
14
15
12
9
10
8
6
9
9
11
15
13
13
16
13
IS
13
12
11
11
10
11
10
11
11
11
NO ACUDE
NG/J
k************i
123
161
178
169
171
177
181
172
177
168
170
169
171
173
184
183
179
162
173
177
178
186
180
176
172
171
181
195
172
185
168
154
152
146
145
136
142
148
154
157
168
184
171
175
172
173
169
172
**
**
**
**
**
**
t***
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
138
KVBll-6015-1233
-------
*ft
ft*
ftft
*«
**
** DATE
AAAAAAAAAAAI
** 6/35/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
ft* 6/25/80
ft* 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
•* 6/25/80
ft* 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/60
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
** 6/25/80
«* 6/25/80
** 6/25/80
** 6/25/80
TIME
r A A A A A A
1215
1230
1205
1300
1315
1330
13U5
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
2330
2345
2400
LOAD
HMTH
A A A Aft A'
9.7
10.3
11.7
10.5
9.4
10.0
7.0
7.9
7.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
".3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
".3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
".3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
02
VOLX
HEAS
*******
7.4
6.4
6.2
7.0
8.2
7.2
9.5
8.0
9.1
- .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
• .0
• .0
- .0
• .0
- .0
-1.0
DRY STACK
C02
VOLX
HEAS
rAAAAAAAAti
9.9
10.8
11.0
10.3
9.0
10.1
7.6
9.3
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
- .0
- .0
• .0
15 MIN. DATA
CAS CONCENTRATION
CO NO CO
PPMV PPMV PPMV
MEAS HEAS 3X02
*******************!
27 248 35
28 251 34
26 259 31
27 250 34
24 244 33
25 245 32
22 223 34
25 240 34
23 231 34
-1
•
•
•
•
•
•
-
-
•
•
.
•
•
•
-
•
•
•
•
•
«•
•
•
•
•
•
•
•
•
•
•
m
-
m
m
.
•
•
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
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
PPHV
3X02
1 1l ***** 1
328
309
315
321
343
320
350
333
350
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
CO
NG/J
bAAAAAAl
' w W W W W W »
12
11
10
11
11
10
11
11
11
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
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
NG/J
A * A **1
181
170
173
177
169
176
193
183
193
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
ACOOE
* A A A A
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
**
ft*
**
ftft
ft*
ft*
»**
ft*
ft*
**
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
**
**
ft*
ft*
ft*
**
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
**
**
ft*
ft*
**
**
**
ft*
**
ft*
**
**
**
**
ft*
ft*
ft*
ft*
139
KVBll-6015-1233
-------
**
**
»*
**
**
** DATE
***********!
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/60
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
«* 6/26/80
** 6/26/80
** 6/26/80
** 6/26/8Q
** 6/26/80
** 6/26/80
** 6/26/8Q
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/60
*• 6/26/80
** 6/26/80
** 6/26/60
** 6/26/80
** 6/26/80
** 6/26/80
»* 6/26/80
** 6/26/8JO
** 6/26/80
TIME
*******
15
30
45
100
115
130
145
200
215
230
245
300
315
330
315
400
415
430
445
500
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
1145
1200
DRY STACK
02 C02
LOAD VOLX VOLX
MWTH MEAS MEAS
**********************
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
".3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
3.2 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
.0
.0
.0
.0
.0
.0
.0
.3 6.1
3,2 13.7 3.0
3.5 13.6 2.9
3.8 13.6 2.
4.4 11.5 5.
5.9 8.5 8.
7.3 6.5 10.
8.5 6.4 10.
7.6 8.3 .2
7.3 8.2 .3
7.0 8.0 .5
7.6 7.4 .8
7.0 7.6 .7
6.4 8.8 8.4
7.0 7.4 10,1
12.3 5.0 12.1
15.2 4.6 12,4
14.6 4.8 12.2
13,5 4.7 12,3
14.4 5.1 11.9
11. 5.7 11.5
12, 5.0 12,1
11. 6.6 10.7
*», 7.0 10.4
11. 5.3 11.8
11. 5.4 11,7
10,0 6.4 10.6
9.4 6.7 10.6
15 MIN, DATA
GAS CONCENTRATION
CO NO CO
PPMV PPMV PPHV
MEAS MEAS 3X02
* * *
f W W W W IV If
VWWWWWWWK1
0
o
o
0
0
o
o
o
0
o
o
o
o
0
9
o
o
o
o
0
74 198 137
258 141 641
303 131 742
317 130 777
0 175 0
31 225 44
44 235 54
36 242 44
25 239 35
26 238 36
27 238 37
90 235 119
33 224 44
29 216 42
38 223 50
58 219 65
51 221 56
38 234 42
49 221 54
40 233 45
34 234 40
42 226 47
18 243 22
32 240 41
37 232 42
38 236 43
35 243 43
34 244 42
NO
PPMV
3X02
>******i
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
0
o
o
369
350
321
318
333
324
292
298
339
335
330
311
301
319
295
246
242
260
244
263
275
254
304
309
266
272
299
307
CO
NC/J
>******«
0
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
46
215
249
260
0
15
18
14
11
12
12
40
14
14
16
21
18
14
18
15
13
15
7
13
14
14
14
14
NO
NG/J
>*****i
o
o
o
o
o
o
o
o
o
o
o
o
o
o
203
193
177
175
163
179
161
164
167
164
182
171
166
176
163
135
133
143
134
145
151
140
167
170
146
150
165
169
ACUDE
******
c
r
*»
r
V
r
1*
c
r
W
c
r
W
c
c
r
V
r
V
r
W
r
Vt
r
(•
r
W>
r
W
r
W
P
V
**
**
**
**
**
**
***
**
**
**
**
**
**
**
**
**
»»
**
**
**
**
«*
• *
**
**
**
**
**
**
**
**
**
**
**
• *
«*
**
**
»*
**
**
**
**
**
**
»«
**
**
**
**
»*
**
**
**
**
140
KVBll-6015-1233
-------
**
**
«*
**
**
** DATE
************
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/60
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/60
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
** 6/26/80
TIME
tft ft ft ftft ft
1215
1230
1245
1300
1315
1330
13«5
1400
1U15
1430
1445
1500
1515
1530
15
-------
**
**
**
**
**
** DATE
************
** 6/27/80
** 6/37/80
** 6/27/flO
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/60
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
«* 6/27/80
** 6/27/80
** 6/27/80
»* 6/27/80
** 6/27/80
*• 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/60
»* 6/27/80
•* 6/27/80
** 6/27/80
** 6/27/60
** 6/27/80
** 6/27/80
«* 6/27/60
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
TIME
k** *** *
15
30
45
too
115
130
145
200
215
230
245
300
315
330
345
000
415
430
445
500
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
1145
1200
LOAD
M*TH
******
-.3
-.3
-.3
".3
-.3
".3
-.3
-t3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
2.9
3.2
3.2
3.5
5.0
7.0
9.7
10.5
7.6
7.9
8.8
7.6
•».!
9.4
8.5
10,5
«».l
3.2
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
DRY STACK
02 C02
VOL* VOLX
MEAS MEAS
t**********A*A^"*-
- .0
- .0
- .0
- .0
- .0
" .0
" .0
- .0
- .0
- .0
• .0
- .0
- .0
- .0
- .0
- .0
" .0
• .0
• .0
- .0
" .0
w m m m w «*
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
13.8 2.7
13.7 2.7
13.6 2.7
13.2 3.3
10.3 7.1
7.9 9.5
6.9 10.5
5.5 11.7
7.9 9.6
7.7 9.8
6.5 10.9
7.6 9,8
7.4 10.0
6.4 10.9
7.7 9.7
5.9 11.3
6.8 10.4
1 .7 3.7
- .0 - .0
• .0 - .0
• .0 - .0
- ,0 - .0
- .0 • ,0
- .0 - .0
- .0 • .0
- .0 - .0
- .0 - .0
15 HIN. DATA
GAS CONCENTRATION
CO NO CO
PPMV PPMV PPMV
MEAS MEAS 3X02
****A**********jk***i
0
m
.
.
•
.
•
•
.
.
•
.
•
.
•
4.
»
«
•
_
.
•
*
m
m
m
m
m
m
m
m
m
m
9
*
•
•
•
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
718 119 1810
668 111 1660
650 107 1593
446 120 1036
38 209 64
34 233 46
37 233 47
40 238 46
30 245 41
34 242 46
42 245 52
31 247 41
39 231 51
38 236 46
30 235 40
37 237 44
32 238 40
347 147 675
0
0
0
0
0
0
0
0
0
NO
PPMV
3X02
rftft ft* ft ftf
0
0
0
0
0
0
0
0
0
o
0
0
0
0
0
0
0
0
0
0
0
300
275
262
278
352
320
297
276
337
328
304
332
306
291
318
282
302
286
0
0
0
0
0
0
0
0
0
CO
NG/J
********
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
607
557
534
347
21
15
15
15
13
15
17
14
17
15
13
14
13
226
0
0
0
0
0
0
0
0
0
NO
NG/J
k**ft **1
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
165
152
144
153
194
176
164
152
186
180
167
183
168
160
175
155
166
157
0
0
0
0
0
0
0
0
0
ACUOE
k*****
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
**
**
**
**
**
ft*
***
»*
ft*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
ft*
**
**
**
**
**
ft*
**
**
**
**
**
ft*
ft*
142
KVBll-6015-1233
-------
ft*
ftft
»*
**
**
** DATE
AAAAAAAAAAAi
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/60
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/BO
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
*» 6/27/80
** 6/27/80
** 6/27/80
»« 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
«* 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/80
** 6/27/60
TIME
r A A A A A A
1215
1230
1205
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1630
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
MWTH
* A * A A A 1
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
".3
-.3
".3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
02
VOLX
MEAS
: A A A A A 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
- .0
• .0
- .0
- .0
- .0
• .0
- .0
" .0
- .0
• .0
- .0
• .0
" .0
" .0
• .0
DRV STACK
C02
VOLX
MEAS
AAAAAAAAA
-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
- .0
• .0
• .0
- .0
• .0
- .0
- .0
- .0
- .0
- .0
-1.0
-1.0
-1.0
-1.0
-1.0
15 MIN. DATA
GAS CONCENTRATION
CO NO CO
PPMV PPMV PPMV
MEAS MEAS 3X02
A A A ^
•
*
-
m
•
m
m
m
m
-
•
•
•
•
*
•
*
•
•
m
m
m
m
m
»
m
m
m
•
»
•
•
.
•
-
•»
•
•
•
•
•
-
•
•
*
•
[^WMMMM*
•
*
•
•
•
•
•
•
•
•
•
•
m
m
•
•
m
«
•
•
•
V
•
•
•
•
•
m
m
m
m
•
•i
•
-
*
•
•
•
•
•
•
•
•
-
• 1
* J •
wwwviwwMwn
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
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
3X02
A A A A A Ai
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
CO
NG/J
»****AA1
• W It W W W *
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
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
NG/J
A it A A A 1
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
u
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
ACUDfc
A ft A A A
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
c
**
• ft
**
**
**
**
»**
**
**
**
**
**
**
**
**
**
**
**
• ft
• ft
**
ft*
• *
• ft
ft*
**
**
**
**
**
*»
*•
**
**
**
ft*
ft*
ft*
ft*
**
**
**
**
**
**
**
**
ft*
ft*
**
**
**
*ft
**
**
143
KVBll-6015-1233
-------
**
**
**
**
**
*• DATE
***********
** If 9/60
** 7/ 9/60
*• 7/ 9/80
** 7/ 9/80
»* 7/ 9/80
** 7/ 9/60
** 7/ 9/80
** 7/ 9/60
** 7/ 9/80
** 11 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
*« 7/ 9/80
** 7/ 9/80
*« 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/60
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
»* 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/60
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
AAAAAA.A..A..*..*..*..*
TIME
****** *
15
30
45
100
115
130
las
200
215
230
245
300
315
330
345
400
415
430
445
500
515
530
545
600
615
630
645
700
715
730
745
600
815
830
845
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MWTH
******
-.3
-.3
-.3
".3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
".3
-.3
-.3
".3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
14.9
16.8
17.9
19.0
19. b
17.9
17.6
17,9
18.2
16.2
16.7
15.8
14.9
15.2
15.2
02
VOLX
MEA3
^ ***** 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
5.0
5.0
4.3
4.0
4.5
4.6
3.9
4.0
3.9
4.0
5.0
4.6
5.1
4.8
5.7
DRY STACK
C02
vouz
MEAS
>^*44*+A^A
rwwwwwwwwv
- .0
- .0
- .0
- .0
- .0
" .0
- .0
• .0
- .0
• .0
" .0
- ,0
- .0
- .0
- .0
• .0
• .0
- .0
- tO
- tO
- .0
" .0
- .0
- .0
" tO
• .0
- .0
" ,0
- .0
- .0
- .0
- .0
" .0
1 .8
12.2
12.6
12.9
12.5
12.5
13.1
13.0
13.0
13.0
12.1
12.2
12.0
12.3
11.4
15 MIN, DATA
GAS CONCENTRATION
CO NO CO
PPMV PPMV PPMV
MEA3 MEAS 3X02
**********
»
•
.
.
.
.
.
.
.
_
.
•
.
•
.
.
.
.
.
m
.
•
.
.
w
.
.
•
.
.
•
.
•1
»« WWW WW VIM
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
35 209 39
26 226 31
33 210 35
39 200 41
57 213 62
30 232 32
31 219 32
29 220 30
33 217 34
30 216 31
33 210 37
31 215 34
29 223 32
29 213 32
32 215 37
NO
PPMV
3X02
********
0
o
0
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
0
o
o
o
o
o
o
o
o
o
o
o
0
235
254
226
211
232
254
230
233
226
230
236
239
252
236
253
CO
NG/J
k******4
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
o
0
0
13
10
H
13
20
1 1
10
10
11
10
12
11
11
10
12
NO
NG/J
»*****!
o
o
o
o
o
o
o
o
o
o
o
o
(I
o
o
o
o
o
o
o
o
o
o
I)
o
o
o
o
o
o
o
o
o
129
140
124
116
126
140
127
126
125
127
130
131
139
130
139
ACUDE
k*****
c
c
c
c
c
c
c
r
»»
r
V
c
r
\e
r
V
c
c
c
c
c
c
c
c
c
c
c
c
r
\f
c
c
c
c
c
c
c
c
**
**
**
**
**
**
***
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
»*
**
**
**
**
**
**
**
**
**
**
**
• *
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
144
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
15 HIM. DAT*
DRY STACK GAS CONCENTRATION
TIME
LOAD
MfcTH
02
VOL 5!
MEAS
C02
VOLZ
MEAS
CO
PPMV
MEAS
NO
PPMV
MEAS
CO
PPMV
3X02
NO
PPMV
3X02
CO
N6/J
NU ACUOE
NG/J
**
**
**
**
**
**
******************************************************************************************
** It 9/80
** 11 9/80
** It 9/80
** 11 9/80
** It 9/80
** 11 9/BO
** 7/ 9/80
** 11 9/80
** It 9/80
** 11 9/80
** 7/ 9/80
** 11 9/80
** If 9/60
** 7/ 9/60
** If 9/80
** 7/ 9/80
** If 9/60
** It 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
»* 7/ 9/80
** If 9/80
** 7/ 9/80
«* It 9/60
** 7/ 9/80
** It 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** 7/ 9/80
** It 9/80
** It 9/80
** 7/ 9/80
** It 9/80
** 7/ 9/80
** It 9/80
** It 9/80
** 7/ 9/60
** It 9/60
** 7/ 9/80
** 11 9/80
** It 9/80
** 7/ 9/60
** It 9/80
** 7/ 9/80
** It 9/80
** 11 9/80
1215
1330
1245
1300
1315
1330
1345
1400
1415
1430
144S
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
2330
234S
2400
12.9
10.5
10.5
10.3
11,4
9.4
6.7
7.3
8.2
12.0
12.6
11.7
11.1
12.3
13.8
12.0
10.8
H.7
12.0
11.7
11.7
11,1
10.3
10.5
10.0
11. «
10.8
10.3
10.8
14.9
15.8
14.6
13.2
12.9
10.5
10.3
10.5
10.5
10.0
".7
'.1
9.4
9.4
10.0
9.7
•».7
10.5
12.6
5.6
7.7
6.2
7.5
7.0
7.6
10.0
8.5
6.9
5.6
5.8
6.0
6.1
5.2
5.4
6.0
6.0
5.8
5.6
5.6
6.0
<>.5
6.8
6.7
6.5
6.3
6.3
6.7
5.8
4.7
5.0
5.2
5.8
6.0
6.7
6.9
6.4
6.6
7.3
7.0
6.9
6.7
6.7
6.5
6.3
6.5
6.3
5.0
11.5
9.4
11.0
9.6
10.1
9.5
6.4
6.4
10.2
11.4
11.2
11.0
10.9
11.6
11.4
10,7
10.7
11.0
11.2
11.0
11.0
10.5
10.2
10.3
10.5
10.7
10.7
10.3
11.1
12.1
11.9
11.7
11.1
10.9
10.2
10.1
10.5
10.4
9.6
10.0
10.0
10.2
10.3
10.5
10.6
10.5
10.7
11.9
30
31
31
31
31
30
36
39
31
23
19
26
24
24
25
23
22
22
22
22
22
20
21
22
21
24
21
21
21
20
21
21
23
22
20
21
23
22
20
23
21
22
22
23
22
21
21
23
213
167
199
185
195
186
160
178
190
228
227
222
218
225
220
216
213
216
215
212
217
211
211
214
211
210
204
204
204
225
216
212
208
207
197
197
199
200
200
194
189
190
186
183
188
184
186
192
35
42
37
41
39
40
59
56
39
26
22
31
29
27
26
27
26
26
25
26
26
24
26
27
26
29
25
26
24
22
23
23
27
26
25
26
28
27
26
29
26
27
27
28
26
26
25
25
249
253
242
2«7
251
250
262
256
242
266
269
266
263
256
254
259
255
256
251
251
260
262
267
269
262
257
250
257
241
248
243
241
246
248
246
251
245
250
263
249
241
239
234
227
230
226
226
216
11
14
12
13
13
13
19
18
13
9
7
10
9
9
9
9
8
8
8
8
8
a
6
9
8
9
6
8
8
7
7
8
8
8
8
137
139
133
136
138
136
144
141
133
147
148
147
145
141
140
143
141
141
138
138
143
144
147
148
144
141
137
141
133
137
134
133
135
137
136
138
135
138
145
137
133
132
129
125
127
126
125
119
**
**
*•
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
145
KVB11-6015-1233
-------
**
**
**
**
**
«* DATE
***********i
** 7/10/80
«* 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
»* 7/10/80
** 7/10/80
** 7/10/80
** 7/10/8Q
** 7/10/60
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/60
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/60
** 7/10/60
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/60
** 7/10/60
** 7/10/80
** 7/10/80
** 7/10/60
** 7/10/60
*» 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
•* 7/10/80
15 MIN, DATA
DRY STACK GAS CONCENTRATION
TIME
r ******
15
30
45
100
115
130
145
200
215
230
245
300
315
330
345
400
415
430
445
500
515
530
545
600
615
630
645
700
715
730
745
600
815
830
845
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MWTH
******'
11.4
10,5
10.0
9.4
9.1
9.1
9.4
10.0
10.0
9.7
10.0
10.0
10.0
10.0
10.0
10.0
10.8
10.5
14.6
13.2
12.3
10.5
8.2
8.8
6,8
7.6
«>.l
7.0
8.2
11.7
13.2
10.0
13.5
l«.l
16.1
10.0
10.3
12.3
11.7
14.4
11.7
11.1
12.3
ll.«
11.1
12.6
12.0
10.8
02
VOLX
MEA3
r ******
5.6
6.1
6.6
7.2
7.3
7.0
6.6
.7
.1
.5
.4
.3
.7
.6
.3
.6
5.6
6.1
4.9
«.e
5.4
5.7
8.0
7.5
6.9
7.8
6.7
7.7
7.9
5.6
5.0
8.5
4.8
4.8
4.3
6.8
7.9
5.4
6.6
5.0
5.9
6.3
5.5
5.6
6.2
5.3
5.7
6.2
C02
VOLX
MEAS
r ******'
11.4
11.0
10.4
9.7
9.7
9.9
10.2
10.3
10.8
10.5
10.6
10.6
10.2
10.4
10.6
10.4
11.4
10.9
12.0
12.0
11.6
11.3
8.8
9.5
10.1
«».l
10.3
9.1
8.9
11.0
11.9
9.0
12.2
12.1
12.6
10.6
9.4
11.7
10.7
12.0
11.2
10,9
1 .6
.3
.0
.7
.5
.0
CO
PPMV
MEAS
r ****** i
24
21
19
21
21
21
21
22
23
23
24
23
23
24
25
24
25
23
24
25
26
25
28
22
23
25
25
25
25
28
26
16
36
36
36
32
31
33
32
36
32
36
37
37
36
39
40
39
NO
PPMV
MEAS
r *******
209
210
213
205
201
210
209
207
208
200
204
206
202
206
202
205
206
204
214
214
210
213
192
203
198
191
200
194
192
202
217
193
230
233
232
230
221
238
229
233
232
224
229
229
229
-1
•1
• 1
CO
PPMV
3X02
k* A****1
28
25
23
27
27
27
26
27
27
26
29
28
26
30
30
30
29
27
26
27
30
29
38
29
29
30
31
33
34
32
29
23
40
40
38
40
42
38
40
40
38
44
43
43
43
44
47
47
NO
PPMV
3X02
k******<
244
253
266
267
264
270
265
260
251
248
251
252
254
257
247
256
241
246
239
237
242
250
266
271
253
260
252
263
264
236
244
278
255
259
250
291
304
274
286
262
276
274
266
271
278
-1
• 1
•1
CO
NG/J
********
9
8
7
10
10
10
9
9
9
9
10
9
13
9
9
11
10
11
11
10
9
7
13
13
13
13
14
12
13
13
12
14
14
14
14
15
15
15
NO ACOOE
NG/J
************
134
140
147
147
145
149
146
143
138
137
136
139
140
142
136
141
132
136
132
131
133
138
146
149
139
143
139
145
145
130
134
153
141
142
137
161
167
151
158
144
152
151
146
149
153
0 0
0 D
0 D
**
**
**
**
**
**
*****
**
**
**
**
**
**
**
»*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
*•
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
146
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
ftftftftftftftftftftft
«* 7/10/60
** 7/10/80
** 7/10/BO
** 7/10/80
** 7/10/80
** 7/10/BO
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/60
** 7/10/60
** 7/10/80
** 7/10/60
** 7/10/80
** 7/10/80
•* 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/60
** 7/10/60
• * 7/10/80
** 7/10/60
** 7/10/80
** 7/10/60
** 7/10/80
** 7/10/60
•* 7/10/80
** 7/10/60
** 7/10/80
** 7/10/80
** 7/10/60
** 7/10/80
«* 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
** 7/10/80
IS MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
k A A A A * A
1215
1230
1205
1300
1315
1330
13a5
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
2330
2345
2400
LOAD
MWTH
ft ft ft ft ft ft
n.l
9.4
8.8
14.6
9.4
9.7
e.2
7.9
10.8
14.1
10.3
10.3
13,8
»3.5
11.4
11.1
12.0
11.4
11.1
11. T
12.0
10.5
13.2
12.6
10.0
10.0
'.7
10.0
10.5
10.5
14.4
15.2
14.4
12.6
12.3
11.1
11,7
12.0
12.0
12.0
12.0
10.8
9.4
10.0
9.4
9.4
10.8
12.3
02
VOL*
MEAS
r ft ft ft ft ft ft
-1.0
"1.0
-1.0
4.6
7.8
6.9
8.1
6.2
6.4
6.1
7.2
7.2
5.2
5.5
6.4
6.6
6.0
6.4
6.8
6.1
5.8
6.7
7.1
7.7
7.4
7.2
7.6
6.9
6.4
6.4
5.7
4.9
5.0
5.7
5.8
6.2
5.8
5.9
5.8
6.6
6.6
8.0
9.5
8.7
9.2
9.2
8.1
6.9
C02
VULX
MEAS
i 4 A 4 * * * i
• W K W W Jf W i
11.3
10.0
9.1
12.3
9.6
10.3
9.3
9.3
10.9
11.2
10.5
10.5
12.0
11.7
11.0
10.6
11.4
H.l
10.7
11.2
11. «
10,7
10.5
10.0
10.3
10.4
10.1
10.7
11.0
11.0
11.6
12.1
12.1
11.6
.4
.2
.5
.4
.6
.0
.4
10.9
9.9
10.5
10.2
10.2
11.0
11.7
CO
PPMV
MEAS
! ft ft ft ft ft ft
40
36
35
38
35
30
25
25
25
25
26
27
31
30
29
27
28
29
28
29
30
27
27
25
27
28
27
28
28
27
27
27
28
29
28
27
26
25
25
25
24
24
22
22
22
22
25
26
NO
PPMV
MEAS
t ft ft ft ft ft ft *
-i
-i
-i
-i
219
215
209
206
220
228
224
226
227
232
227
226
226
228
232
233
233
236
233
229
232
226
231
228
231
230
230
226
231
229
229
225
228
228
224
221
224
222
225
224
222
224
219
227
CO
PPMV
3*02
r ft ft ft ft ft ft i
32
29
28
41
47
38
34
35
30
30
33
35
35
34
35
33
33
35
35
35
35
34
35
33
35
36
36
35
34
33
31
30
31
34
33
32
30
29
29
31
30
33
34
32
33
33
34
33
NO
PPMV
3X02
1 ft ft ft ft ft ft ':
0
0
0
-1
299
274
292
293
271
275
292
295
258
269
260
265
271
281
294
281
276
297
302
310
307
297
310
291
285
263
270
255
260
269
271
273
270
272
265
276
280
308
353
320
339
342
306
290
CO
N6/J
rft ft ft ft ft ft '
10
9
9
l«
16
12
11
11
10
10
11
11
11
11
12
11
11
12
11
11
11
11
11
11
12
12
12
12
11
11
10
10
10
11
11
11
10
10
9
10
10
11
11
10
11
11
11
11
NO ACOUE
NG/J
[ftftftftftftftftftftftft
0 G
0 G
0 G
0 D
165
151
161
161
149
152
161
162
142
148
154
157
149
155
162
155
152
164
166
171
169
164
171
160
157
156
149
140
143
148
149
151
149
150
146
152
154
169
194
181
187
188
168
160
**
**
**
**
**
**
r * * *
**
**
»*
«*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
*»
**
**
**
**
**
**
«*
**
**
**
**
**
• *
ft*
ft*
**
**
**
**
*»
**
**
147
KVB11-6015-1233
-------
**
**
**
**
**
«* DATE
***********i
** 7/11/80
** 7/11/80
** 7/11/80
«* 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/60
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
«* 7/11/80
** 7/11/80
«* 7/11/80
** 7/11/80
** 7/11/60
•* 7/11/80
»* 7/11/80
** 7/11/60
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
** 7/11/80
»* 7/11/80
15 MIN, DATA
DRY STACK GAS CONCENTRATION
03 COS CO NO CO
TIME
*******
15
30
45
too
115
130
145
200
215
230
2«5
300
315
330
345
400
415
430
445
500
515
530
545
600
615
630
645
700
715
730
745
800
815
830
8«5
900
•MS
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MXTH
** *****
10.5
10.3
10.0
9.4
9.7
9.4
9.4
9.1
9.1
8.8
8.5
8.5
8.5
8.5
8.8
8.6
10.3
10.0
'.1
9.7
9.1
9.4
9.1
8.8
8.8
10.0
13.2
13.8
13.2
10.8
13.2
13.2
14.1
13.2
13.8
10.1
20.5
16.4
15. 6
16.1
14.6
12.0
12.0
10.8
10.5
11.7
12.0
12.9
VOLX
MEAS
F ft ft ft ft ft ft
5.9
6.6
6.7
7.3
7.1
7.1
7.2
7.4
7.2
7.5
8.3
7.9
7.9
8.1
7.7
7.5
6.2
6.3
7.5
6.4
7.2
6.8
7.3
7.7
7.7
7.5
5.5
5.6
6.2
6.7
5.3
5.4
5.5
5.1
5.4
4.8
1.4
4.5
4.4
4.4
4.4
7.0
5.8
6.2
6.8
5.9
5.9
5.6
VOLX
MEAS
t ft ft ft ft ft ft 1
11.2
10.7
10.5
10.0
10.2
10.2
10.1
9.9
10.1
9.8
9.1
9.5
9.5
9.3
9.7
9.8
11. 1
10.9
9.8
10.8
10.1
10.4
10.0
9.7
9.7
9.8
1 .6
.5
.1
.6
.6
.5
.5
.«
1 .7
12.1
12.4
12.2
12.3
12.3
12.3
10.0
11.1
10.7
10.2
U.I
11.1
11.5
PPMV
MEAS
' * * A 4 * * 4
1 W w If W H W
25
24
23
22
22
21
22
21
20
20
19
21
22
21
22
21
24
23
20
26
21
23
22
21
23
22
24
26
24
25
29
28
28
28
29
50
82
U6
40
40
36
32
30
29
28
30
30
31
PPMV
MEAS
r ft ft * ft ft ft i
229
222
222
219
215
217
215
215
217
214
209
208
207
214
210
212
217
216
213
206
206
207
206
204
205
207
220
227
225
210
215
215
216
220
216
217
209
229
224
227
230
219
222
223
220
223
222
221
PPMV
3X02
Fft ft ft ft ft ft 1
29
30
26
28
28
27
28
27
26
26
26
28
30
29
29
28
29
28
26
32
27
29
28
26
31
29
27
30
29
31
33
32
32
31
33
55
88
50
43
43
41
41
35
35
35
35
35
36
NO
PPMV
3X02
tft ftft ft ftftft
273
277
279
286
278
281
280
265
283
265
296
286
285
299
284
263
264
264
284
254
269
262
271
276
277
276
255
265
273
264
246
246
253
249
249
241
226
249
243
246
249
282
263
271
279
266
264
258
**
**
*«
CO NO ACUDF **
NG/J NG/J
****************
10 150
10 IS)
1
1
i
1
154
158
153
155
154
157
156
157
163
157
157
165
157
156
145
146
156
140
146
144
149
152
153
152
141
10 146
9 151
10 145
11 136
10 136
10 139
10 137
11 137
18 133
29 125
16 137
14 133
14 135
13 137
13 155
11 145
11 149
11 154
12 146
12 146
12 142
**
**
*******
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
«*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
148
KVBll-6015-1233
-------
**
**
**
**
ft*
**
* *'
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
ft*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
ft*
**
**
**
**
**
**
**
**
15 MIN, DATA
DRV STACK GAS CUNCENTRATION
DATE
rftftftftftftftft'
7/11/80
7/11/80
7/11/80
7/11/80
7/11/60
7/11/80
7/11/80
7/11/80
7/11/80
7/11/60
7/11/80
7/11/60
7/11/80
7/11/60
7/11/60
7/11/80
7/11/60
7/11/60
7/11/80
7/11/80
7/11/60
7/11/80
7/11/80
7/11/80
7/11/80
7/11/80
7/11/80
7/11/80
7/11/80
7/11/80
7/11/80
7/11/80
7/11/80
7/11/80
7/11/80
7/11/60
7/11/80
7/11/80
7/11/80
7/11/80
7/11/60
7/11/80
7/11/80
7/11/80
7/11/80
7/11/80
7/11/80
7/ll/BO
TIME
t ft ft ft ft ft ft
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
1630
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
MUTH
ft ft ft ft ft ft '
15.2
15.8
17.0
13.5
13.2
-.3
-.3
8.2
9,7
12.0
10.0
10.5
10.0
10.8
10.3
11.1
12.3
15.2
17.6
13.2
12.6
12.3
10.0
10.5
10.3
9.4
8.6
9.7
9.7
10.3
10.3
10.0
10.0
9.1
10.0
10,0
10.6
10.3
10.0
9.7
B.5
8.8
9!4
9.4
9.4
9.4
9.4
02
VOLX
MEAS
rft ftft ft ft ft '
5.1
4.6
5.2
6.1
6.3
-1.0
-1.0
7.0
7.4
5.9
7.3
6.8
7.2
6.4
6.4
6.3
6.0
4.6
4.7
5.2
5.6
5.8
6.8
6.6
6.8
7.B
8.1
7.3
7.3
6.1
6.7
6.8
6.5
6.9
.8
.5
.9
.1
.7
.9
.8
7.2
8.4
7.7
7.4
7.3
6.9
6.9
C02
VOLX
MEAS
rftft ftft ftft'
11.9
12.2
11.6
11.1
10,9
-1.0
-1,0
10.0
9.6
11,0
9,8
10.3
9.9
10.6
10.6
10.7
10,9
12,0
11.9
11.6
11.4
11.2
10.4
10.5
10.3
9.4
9.0
9.8
9.8
10.9
10.4
10.2
10.5
10.1
10.3
10.6
11.2
10.9
10.5
10.3
10.4
10.0
8.9
9.6
9.8
9.9
10.3
10.3
cu
PPMV
MEAS
[ft ft ft ft ft ft
41
43
54
29
29
-1
-1
28
28
26
24
24
24
24
25
25
27
39
31
29
30
30
28
27
26
27
27
27
26
28
25
24
24
23
23
24
25
23
23
22
23
22
20
21
22
22
22
22
NO
PPMV
MEAS
rftft ft ft ft ft i
222
235
226
234
236
•1
-1
186
203
216
212
212
211
214
213
219
216
225
234
225
224
224
216
216
216
213
211
210
210
217
219
223
216
217
218
218
219
223
220
222
221
221
211
215
216
224
220
220
CO
PPMV
3X02
tft ft ft ft ft ft 1
46
47
61
35
35
0
0
36
37
31
31
30
31
29
30
30
32
42
34
33
35
35
35
33
35
36
37
35
34
33
31
30
29
29
29
29
29
27
28
28
29
28
28
28
29
28
28
28
NO CO
NO ACODE
PPMV NG/J NG/J
3X02
bAAAAA^AA^^^^^j
**
**
**
**
**
**
Iftftftftftftftftftftftfcwwwwwwww mmmmmmmmmm
251 15 138 **
256 15 142
257 20 142
263 11 156
289 11 159
0 0 0 C
0 0 0 C
242 12 133
269 12 148
257 10 142
279 10 153
269 10 146
275 10 152
264 9 145
262 10 144
266 10 148
259 10 143
247 14 136
258 11 142
256 11 141
262 11 144
265 11 146
276 11 152
270 11 149
274 I
1 151
291 12 160
295 12 162
276 11 152
276 1
1 152
262 11 144
276 10 152
263 10 156
270 10 149
277
276
270 1
261 1
269
277
283
260
288
302
291
286
294
281
281
152
152
149
144
146
152
156
154
159
166
160
157
162
155
155
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
*«
**
**
**
**
**
**
**
**
**
**
**
149
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
ftftftftftftftftftftftl
** 7/12/80
** 7/12/60
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
«* 7/12/80
** 7/12/80
** 7/12/80
*» 7/12/80
** 7/12/80
»* 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
«* 7/12/60
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
«* 7/12/80
** 7/12/80
•* 7/12/80
** 7/12/80
** 7/12/60
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
«* 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
15 MIN. DATA
DRY STACK GAS CONCENTRATION
TIME
ft ft ft ft ft ft
15
30
45
100
115
130
115
200
215
230
245
300
315
330
345
400
ai5
430
445
500
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.
1145
1?00
LOAD
M*TH
It ft ft A A ft i
9.7
12.0
11.1
14.1
15.2
12.9
11.1
10.0
9.1
8.8
6.8
8.8
8.8
8.8
9.4
9.4
10.0
9.7
9.7
fl.B
6.5
6.5
10.3
11.1
13.2
13.5
12.3
10.8
10.5
11.1
12.6
12."
9.4
6.6
6.8
8.5
11.7
10.8
10.5
10.5
10.8
10.5
10.5
10.3
12.0
11.7
12.3
13.5
02
VOL*
MEAS
ft ft ft ft ft ft 1
7.2
7.3
7.2
5.5
6.0
«.9
4.8
5.4
7.2
7.3
8.2
8.0
8.0
7.7
8.2
7.7
7.1
7. a
6.6
7.0
7.6
7.9
8.3
7.7
7.1
5.8
5.4
5.4
6.2
6.5
6.7
6.2
5.6
5.7
5.9
6.0
6.1
6.4
5.9
6.7
6.5
6.8
6.4
6.9
6.8
6.7
5.6
5.9
C02
VOLX
MEAS
' ft ft ft ft ft ft 1
10.1
9.9
10.0
11.6
11.1
12.1
12.1
11.7
10.1
10.0
9.0
9.3
9.3
9.6
9.1
9.7
10.2
9.9
10.7
10.4
9.7
9.5
9,0
9.6
10.2
11.3
11.6
11.6
11.0
10,9
10.7
.1
.6
.5
.a
.3
.2
.0
.3
10.7
10.9
10,5
10.9
10.5
10.5
10.6
11.6
11.3
CO
PPMV
MEAS
1 ft ft ft ft ft ft 1
21
21
22
24
26
25
24
25
22
22
20
21
20
21
21
20
21
20
23
23
22
22
21
22
30
26
25
24
23
24
23
24
25
24
24
24
25
25
26
23
25
23
24
23
24
23
26
25
NO
PPMV
MEAS
ft ft ft ft ft ft t
222
222
221
225
216
234
235
227
224
214
219
217
217
215
214
220
219
223
221
221
215
211
214
215
214
229
232
239
232
227
226
228
229
233
229
233
228
229
231
234
226
230
228
231
228
228
228
232
CO
PPMV
3*02
' ft ft ft ft Aft; 1
27
27
28
27
31
27
26
28
28
28
28
29
27
26
29
27
27
26
28
29
29
30
29
29
38
30
28
27
28
29
26
29
29
28
28
28
30
30
31
26
31
29
29
29
30
28
30
29
NO
PPMV
3X02
ft ft ft ft ft ft 1
290
292
288
261
259
261
261
262
292
281
306
301
301
291
301
298
284
295
276
264
269
290
304
291
277
271
267
276
282
282
264
277
267
274
273
279
275
282
275
294
260
291
281
295
289
287
266
276
CO
NG/J
» A A * A ft *i
ft ft ft ft >• ™ 1
9
9
9
9
10
9
8
10
10
10
13
10
1
9
9
9
10
10
10
9
10
9
9
9
10
9
10
10
NO ACODE
NG/J
iftftftftftftftftftftftft
159
161
159
144
143
144
144
144
161
155
170
166
166
160
166
164
156
163
152
156
159
160
167
160
153
149
147
152
155
155
157
153
147
151
150
154
152
155
152
162
154
161
155
162
159
156
147
152
**
**
**
**
**
«*
t * A *
[ W W •
**
• *
**
• •
**
**
**
**
**
• *
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
««
*•
**
**
*•
150
KVBll-6015-1233
-------
**
**
**
**
**
** DATE
ftftftftftftftftftftft
** 7/12/80
** 7/12/80
** 7/12/80
»• 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
•* 7/12/80
** 7/12/80
** 7/12/80
•* 7/12/60
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/80
»* 7/12/80
»* 7/12/80
** 7/12/60
** 7/12/80
** 7/12/60
** 7/12/80
** 7/12/60
** 7/12/60
** 7/12/80
** 7/12/80
** 7/12/80
ft* 7/12/80
** 7/12/80
** 7/12/60
** 7/12/60
** 7/12/60
** 7/12/80
** 7/12/80
** 7/12/80
** 7/12/60
** 7/12/80
** 7/12/80
• ft 7/12/80
•* 7/12/60
** 7/12/80
** 7/12/60
»* 7/12/80
** 7/12/80
** 7/12/80
** 7/12/60
** 7/12/80
15 HIM, DATA
DRY STACK GAS CONCENTRATION
TIME
b ft ft ft ft ft 4
1215
1230
1245
1300
1315
1330
1345
1400
1«15
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
2330
2345
2400
LOAD
MWTH
^ A + A A A
W Jf W W K 11
12.0
11.7
11.7
11.7
9.4
8.8
9.4
8.2
8.5
6.5
8.8
9.4
10.0
11.1
11.7
12.9
10.5
9.7
9.7
9,7
10.0
8.8
8.8
8.6
6.8
8.6
.«
.«
.<•
.«
.7
.2
8.8
8.2
8.8
7.9
7.3
6.4
6.7
6.4
6.7
6.2
6.7
6.7
6.7
6.4
6.7
9.4
02
VOLX
MEAS
t ft ft ft ft ft ft
5.8
5.4
6.0
6.0
6.1
6.1
7.8
8.4
7.6
9.0
8.2
8.6
8.3
7.4
6.9
6.1
6.2
5.9
7.4
8.0
7.2
7.8
7.3
8.7
8.2
8.3
7.6
7.4
7.0
7.2
7.«
7.8
7.6
8.7
8.1
6.6
8.3
8.8
9.6
10.4
9.7
10.3
10.3
9.5
9.7
9.8
10.2
7.8
C02
VOLX
MEAS
r ft ft ft ft ft ft '
1.4
1.7
1.3
1.2
1.2
1.1
9.6
9.1
9.8
8.4
9.2
8.7
9.0
10.0
10.4
11.1
11.0
11.3
9.9
9.4
10.1
9.6
10.1
8.8
9.2
9.1
9.8
10.0
10.4
10.1
10.0
.6
.7
.8
.3
.7
.2
.7
7.6
6,9
7.6
6.9
6.9
7.8
7.6
7.5
7.0
9.6
CO
PPMV
MEAS
r ft ft ft ft ft ft '
26
25
25
25
25
25
21
22
21
22
21
21
22
22
23
23
23
24
24
33
28
26
26
28
29
35
26
24
22
27
24
23
22
19
20
19
19
20
20
21
21
21
22
21
22
21
23
26
NO
PPMV
MEAS
[ft ft ft ft ft ft '
229
235
233
231
237
236
228
216
228
211
231
230
231
233
235
239
243
258
237
209
214
212
215
198
203
196
222
227
221
219
234
234
233
218
222
219
223
216
194
160
192
183
162
201
191
195
187
228
CO
PPMV
3X02
r ft ft ft ft ft ft 1
30
28
30
30
30
30
28
31
28
33
29
30
31
29
29
27
28
28
31
45
36
35
36
41
40
49
34
31
28
35
31
31
29
27
27
28
26
29
32
35
33
35
37
32
35
33
38
35
NO
PPMV
3X02
1 ft, ft ft ft ft ft'
271
271
279
277
266
265
311
312
306
317
325
334
326
308
300
289
295
307
314
290
279
289
282
290
286
278
298
300
264
286
310
319
313
319
310
323
316
319
312
306
306
309
307
315
305
314
312
311
CO
NG/J
I ft ft ft ft ft ft 1
10
9
10
10
10
10
9
10
9
11
9
10
10
10
15
12
11
12
13
13
16
11
10
9
11
10
10
9
9
9
9
9
9
10
12
11
11
12
11
11
11
12
11
NO ACOUE
NG/J
k******ft***ft*
149
149
154
153
158
157
171
172
169
175
179
184
160
170
165
159
163
169
173
159
154
159
156
160
157
153
164
165
156
157
171
176
172
176
171
178
174
176
172
169
169
170
169
174
168
173
172
171
**
**
**
**
**
**
& ** *
**
**
**
**
**
**
**
**
**
**
ft*
**
**
**
**
**
**
**
**
**
*«
*«
**
ft*
**
**
**
**
»*
**
ft*
*•
**
**
**
**
**
**
**
ft*
**
**
**
**
**
**
**
**
151
KVBll-6015-1233
-------
**
**
**
**
ft*
** DATE
*A+*+A***+*4
• WIfWHWWIiWWWil
** 7/13/80
• * 7/13/80
** 7/13/80
** 7/13/80
*» 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
*« 7/13/80
** 7/13/80
»* 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/60
** 7/13/80
»* 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
** 7/13/80
15 HIN. DATA
DRY STACK GAS CONCENTRATION
TIME
[ A A A A A A '
15
30
IS
100
115
130
145
200
215
230
2«5
300
315
330
315
400
U15
430
445
500
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
1145
1200
LOAD
MfcTH
A A A 1t A 1t 4
9.4
12.3
10.8
7.6
7.0
6.4
6.4
6.2
6.4
6.2
6.4
6.2
6.4
6.4
6.7
6.4
6.7
6.2
7.0
6.7
6.4
6.4
6.2
6.4
8,8
10.8
10.3
8.5
8.5
9.4
13,5
11.7
9.7
11.7
12.9
10.5
9.4
7.9
7.0
6.4
6.4
*.«
7.3
7.6
7.9
8.2
8.2
7.0
02
VOLX
HEAS
I A A A A A A 41
7,4
6.4
6.3
8.8
9.3
10.9
10.0
10.6
9.8
10.6
9.8
10.4
9.9
9.9
9.8
10.0
9.7
10.1
9.3
9.6
9.4
10.5
9.5
10.4
8.9
6.7
6.3
8.3
8.9
8.1
6.0
6.4
8.0
8.1
6.2
7.0
8.0
8.9
9.3
9.5
11. 0
10.6
9.9
9.1
9.2
9.0
8.7
9.9
C02
VOLX
HEAS
! A A A A A A 4
10.1
11.0
11.1
8.7
8.2
6.3
7.3
6.5
7.5
6.5
7.5
6.7
7.3
7.3
7.5
7.2
7.6
7.1
8.0
7.7
8.0
6.7
7.9
6.8
8.5
10,8
11.1
9.3
8.7
9.5
11. «
11. 0
9.6
9.6
11.2
10,5
9.6
8.7
8.3
8.0
6.2
6.5
7.4
8.3
8.2
8.5
8.7
7,5
CO
PPMV
MEAS
f A A A A A A 4
28
23
22
21
21
25
23
24
23
23
23
23
23
22
23
23
23
23
25
24
24
23
25
23
33
26
22
20
21
21
22
21
23
22
21
20
19
19
20
21
22
20
20
19
20
20
20
20
NO
PPMV
MEAS
I A A A A A AH
234
242
240
221
210
175
188
175
190
174
189
177
187
187
189
182
188
180
195
190
192
175
189
175
195
229
239
224
208
219
246
240
216
221
257
243
231
223
213
202
185
195
207
221
220
223
227
210
CO
PPMV
3X02
[ A A A A A A t
37
28
26
31
32
44
37
41
37
39
37
39
37
35
37
37
36
38
38
38
37
39
39
39
49
32
26
28
31
29
26
25
31
30
25
25
26
28
30
32
39
34
32
28
30
30
29
32
NO
PPMV
3X02
F A A A A A A4
310
298
294
326
324
313
308
304
306
302
304
301
304
304
304
298
300
298
300
300
298
301
296
298
290
288
293
318
310
306
295
296
299
309
312
312
320
332
328
317
334
338
336
335
336
335
333
341
CO
NG/J
i * A * * A * 4
r W W W w ~ ~ 1
12
9
9
10
10
15
12
13
12
13
12
13
12
12
12
12
12
12
12
12
12
13
13
13
16
n
9
9
10
9
8
8
10
10
8
8
8
9
10
11
13
11
10
9
10
10
9
10
NO ACODE
NG/J
tAAAAAAAAAAAAl
171
164
162
100
178
172
170
167
168
166
168
166
167
167
168
164
165
164
165
165
164
166
163
164
160
159
161
175
171
168
162
163
165
170
172
172
176
183
181
174
184
186
185
184
185
184
183
188
**
**
**
**
**
**
t A A A
**
**
*•
**
•*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
•*
**
**
«*
**
**
**
**
**
**
**
**
**
**
**
*«
**
**
**
**
**
**
**
**
**
**
**
**
152
KVB11-6015-1233
-------
**
**
**
ft*
• ft
ft*
A it
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
«*
**
**
**
**
**
**
**
**
**
**
**
**
•«
**
**
**
**
**
**
**
**
**
**
**
DATE
tAA&AAAAA
7/13/80
7/13/80
7/13/80
7/13/60
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/60
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
7/13/80
02
LOAD VOLX
TIME MWTH MEAS
tAAAftftAAAAAAAAAAAA A '
1215 7.9 8.5
1230 8,2 8.1
1215 7,6 9.0
1300 8,2 8.6
1315 7.6 8.9
1330 6.7 9.7
1345 7.0 9.2
1UOO 6.2 10.5
1415 6.2 10.7
1430 7.0 9.3
1445 6,7 9.6
1500 6.7 9.6
1515 7.6 8.7
1530 7.3 9.0
1545 7.3 9.2
1600 7.3 9.4
1615 .3
1630 .
1645 .
1700 .
1715 .
1730 .
1745 .
1800 ,3
1815 .3
1830 .3
1845 .3
1900 ,3
1915 .3
1930 .3
1945 .3
2000 .3
2015 .3
2030 .3
2045 -.3
2100 -.3
2115 -.3
2130 -.3
2145 -.3
2200 -.3
2215 -.3
2230 -.3
2245 -.3
2300 -.3
2315 -.3
2330 ..3
2345 -.3
2400 -.3
.0
.0
.0
.0
.0
.0
.0
.0
.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 STACK
C02
VOLX
MEA3
tAAAAAAAAA
8.9
9.4
8.5
9.0
8.7
7.7
8.2
6.6
6.4
8.1
7.8
7.8
8.7
8.5
8.3
8.0
•1.0
•1.0
-1.0
•1.0
-1.0
-1.0
-1.0
• 1.0
•1.0
-1,0
•1.0
-1.0
-1.0
-1.0
-1.0
-1.0
-1.0
-1.0
-1.0
-1.0
-1.0
-1.0
-1.0
-1.0
-1.0
-1.0
-1.0
-1.0
-1.0
•1.0
•1,0
-1.0
15 "IN. DATA
GAS CONCENTRATION
CO NO CO
PPMV PPMV PPMV
HEA3 MEAS 3X02
AAAAAAAAAAAAAAAAAAAi
21 218 30
20 226 27
19 222 28
19 221 27
18 221 26
19 210 30
19 219 29
20 192 34
15 180 26
22 213 33
21 209 33
22 208 34
22 220 32
21 221 31
21 219 32
21 218 32
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
NO
PPMV
3X02
1 A A A A A A'
314
316
333
321
329
335
335
330
315
326
331
329
322
332
335
339
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
CO
NG/J
F AA A A A A1
10
9
9
9
9
10
9
11
8
11
11
11
10
10
to
10
0
0
0
0
0
0
0
0
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
NG/J
t A A A A A i
173
174
184
177
181
185
184
182
174
181
182
161
177
163
184
167
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
ACODE
1 A A A A A
B
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
C
ft*
ft*
ft*
• ft
ft*
ft*
>**
**
ft*
ft*
**
**
ft*
**
**
**
**
**
**
**
**
**
**
ft*
**
**
ft*
**
**
ft*
ft*
ft*
**
ft*
**
• ft
ft*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
ft*
**
ft*
ft*
153
KVBll-6015-1233
-------
TECHNICAL REPORT DATA
(Pleat read faxructions on the reverse before completing}
1. REPORT NO.
EPA-600/7-81-095a
2.
3. RECIPIENT'S ACCESSION NO.
4. TITLE AND SUBTITLE
Thirty-day Field Tests of Industrial Boilers: Site 5
Gas-fired Low-NOx Burner
5. REPORT DATE
May 1981
6. PERFORMING ORGANIZATION CODE
AUTHOH(S)
8. PERFORMING ORGANIZATION REPORT NO.
W. A. Carter and H. J. Buening
KVB11-6015-1233
. 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
14. SPONSORING AGENCY CODE
EPA/600/13
is.SUPPLEMENTARY NOTES ffiRL-RTP project officer is Robert E. Hall, Mail Drop 65. 919/
541-2477. EPA-600/7-80-085a through -085d are similar reports for Sites 1-4.
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 the
combustion modification techniques which were effective for short-duration tests
are feasible for a longer period. The report gives results of a 30-day field test of a
24.9 MW (85,000 Ib steam/hr) water tube boiler with low-NOx burners. The 30-day
test was conducted with the unit firing natural gas. The mean NO emission level was
33 ng/J with a geometric dispersion of 1.12 at the high load condition.
17.
KEY WORDS AND DOCUMENT ANALYSIS
a.
DESCRIPTORS
b.lDENTIFIERS/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
Low-NOx Burners
13 B
2 IB
13A
07A
2 ID
07B
07C
13. DISTRIBUTION STATEMENT
Release to Public
19. SECURITY CLASS (This Report)
Unclassified
21. NO. OF PAGES
154
20. SECURITY CLASS (This page)
Unclassified
22. PRICE
EPA Farm 2220-1 O-73)
154
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EPA-335
Publication No. EPA-600/7-81-095a
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