xvEPA
United States Industrial Environmental Research EPA-600/7-80-085b
Environmental Protection Laboratory April 1980
Agency Research Triangle Park NC 27711
Thirty-day Field Tests of
Industrial Boilers: Site 2
Residual-oil-fired Boiler
Interagency
Energy/Environment
R&D Program Report
-------
RESEARCH REPORTING SERIES
Research reports of the Office of Research and Development, U.S. Environmental
Protection Agency, have been grouped into nine series. These nine broad cate-
gories were established to facilitate further development and application of en-
vironmental technology. Elimination of traditional grouping was consciously
planned to foster technology transfer and a maximum interface in related fields.
The nine series are:
1. Environmental Health Effects Research
2. Environmental Protection Technology
3. Ecological Research
4. Environmental Monitoring
5. Socioeconomic Environmental Studies
6. Scientific and Technical Assessment Reports (STAR)
7. Interagency Energy-Environment Research and Development
8. "Special" Reports
9. Miscellaneous Reports
This report has been assigned to the INTERAGENCY ENERGY-ENVIRONMENT
RESEARCH AND DEVELOPMENT series. Reports in this series result from the
effort funded under the 17-agency Federal Energy/Environment Research and
Development Program. These studies relate to EPA's mission to protect the public
health and welfare from adverse effects of pollutants associated with energy sys-
tems. The goal of the Program is to assure the rapid development of domestic
energy supplies in an environmentally-compatible manner by providing the nec-
essary environmental data and control technology. Investigations include analy-
ses of the transport of energy-related pollutants and their health and ecological
effects; assessments of, and development of, control technologies for energy
systems; and integrated assessments of a wide range of energy-related environ-
mental issues.
EPA REVIEW NOTICE
This report has been reviewed by the participating Federal Agencies, and approved
for publication. Approval does not signify that the contents necessarily reflect
the views and policies of the Government, nor does mention of trade names or
commercial products constitute endorsement or recommendation for use.
This document is available to the public through the National Technical Informa-
tion Service, Springfield, Virginia 22161.
-------
EPA-600/7-80-085b
April 1980
Thirty-day Field Tests of Industrial
Boilers: Site 2 Residual-oil-fired Boiler
by
W.A. Carter and R.J. Tidona
KVB, Inc.
P.O. Box 19618
Irvine, California 92714
Contract No. 68-02-2645
Task No. 4
Program Element No. EHE624
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
-------
ABSTRACT
This is a final report on a test program to evaluate the long term
effectiveness of combustion modifications on industrial boilers. During
previous programs short term tests have been performed on industrial boilers
to determine the effect of combustion modifications on air pollutant emis-
sions such as NO , SO , CO, HC, and particulate. The objective of this
X X
program was to determine whether the combustion modification techniques
which were effective for short duration tests are feasible for a longer
period. This report presents results of a 30-day field test of a 26.4 MW
output (90,000 Ib steam/hr) residual-oil-fired boiler. The NO control
x
technology employed on this unit was staged combustion air. The as found
concentration of NO was 130 ng/J (235 ppm at 3% O , dry). Firing in the
X 2f
low NO mode, with staged combustion air, resulted in a reduction in NO
X X
emission of approximately 23 percent to 100 ng/J (181 ppm at 3% O , dry).
KVB 6017-1216
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CONTENTS
Section Page
ABSTRACT i
1.0 SUMMARY 1
1.1 Objective and Scope 1
1.2 Results 2
1.3 Conclusions 5
2.0 INSTRUMENTATION AND PROCEDURES 6
2.1 Emissions Measurement Instrumentation 6
2.1.1 Gaseous Emissions 6
2.1.2 Particulate Emissions 13
2.1.3 Polycyclic Organic Matter (POM) Emissions 13
2.1.4 Opacity Measurement 15
2.2 Boiler Description and Characteristics 16
2.3 Daily Test Activity 17
3.0 TEST RESULTS 19
3.1 Continuous-Monitor Certification Tests 19
3.2 Residual-Oil-Fired Boiler Tests 22
3.2.1 Gaseous Emissions 23
3.2.2 Particulate Emissions 27
3.2.3 POM Emissions 27
3.2.4 Boiler Efficiency
3.2.5 Data Reduction
APPENDICES:
A. EFFICIENCY MEASUREMENTS 47
B. DATA RECORDING FORMATS 54
C. CONTINUOUS MONITOR CERTIFICATION DATA SHEETS 72
D. PERFORMANCE SPECIFICATIONS AND SPECIFICATION 90
TEST PROCEDURES FOR MONITORS
S. SUMMARY OF PREVIOUS DATA FROM SITE 2 106
F. TABULATION OF 15-MINUTE DATA HI
ii KVB 6017-1216
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FIGURES
Section ga9e
1-1 Site 2 - Residual Oil Field Boiler-Staged Combustion Air 4
(BOOS)
2-1 Photograph of KVB Continuous Monitor for Measuring 7
Gaseous Emissions
2-2 Schematic of Continuous Monitor Sampling and 10
Conditioning System
14
2-3 Mark III Adsorbent Sampling System
3-1 The Effect of Excess Oxygen on NO Emission 27
Site 2 - Residual-Oil-Fired Boiler
3-2 Particulate Loading vs. Stack Excess Oxygen for 29
30-day Test Location 6017-2
35'
3-3 Format of 15-Minute Emissions Data
36
3-4 Summary of 24-Hour Average Data
3-5 Normal-Probability Plot of 24-Hour Averages of NO 38
Emissions from a Residual Oil Fired Boiler
3-6 Log Probability Plot of 24-Hour Averages of NO 41
Emissions from a Residual Oil Fired Boiler
3-7 Log Probability Plot of 24-Hour Averages of NO 42
Emissions from a Residual Oil Fired Boiler
43
3-8 Daily Plot of NO Emissions
44
3-9 Daily Plot of Excess C>2
iii KVB 6017-1216
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TABLES
Section Page
1-1 Summary of 24-Hour Average Gaseous Emissions 3
2-1 Analytical Instrumentation 8
2-2 Schedule of paily Events - Site 2 18
3-1 Schedule of Certification Test Events 20
3-2 Instrument Specifications and Performance 21
3-3 Summary of Observations, Comments and Gaseous and 24
Particulate Emissions Site 2, Residual-Oil-Fired Boiler
3-4 Particulate Data Summary for Site 2, Residual-Oil-Fired 28
Boiler
3-5 Summary of POM Analyses for Site 2, Residual-Oil-Fired 31
Boiler
3-6 Summary of Fuel Oil Analyses from Site 2, Residual- 32
Oil-Fired Boiler
3-7 Summary of Boiler Efficiency Calculations for Site 2, 33
Residual-Oil-Fired Boiler
3-8 NO Emissions Frequency Data, Site 2 37
3-9 Frequency Data for Site 2 Boiler with SCA 40
iv KVB 6017-1216
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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 in air pollutant
emissions during short-term tests are feasible for longer periods. In addi-
tion, boiler performance and reliability were monitored. The combustion
modifications have previously been shown to be effective on industrial
boilers. (Reference 1 and 2).
The program scope provided for thirty-day field tests of a total of
seven industrial boilers with design capacities ranging from 14.65 to 73.25 MW
output (50,000 to 250,000 Ib steam/hr). This final report is for the second
of the seven, a 26.4 MW output (90,000 Ib steam/hr) residual-oil-fired boiler
using staged combustion air and low excess air as the NO emission control
technology.
During the test period,- continuous-monitor certification tests were
performed concurrently with low NO testing. Emissions measured were
particulate, NO, CO , CO, and O_. Boiler efficiency was measured several
times during the program to determine the effect of combustion modification
on boiler efficiency.
This is a final report on the thirty-day test documenting the test
equipment, a summary of the test data, and a discussion of the data in
relation to the control technology employed for this type of boiler.
KVB 6017-1216
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1.2 RESULTS
The initial task of this program was to select industrial boiler test
sites which fit the categories set forth in the statement of work. Further,
it was desired to find a site which had previously been tested to minimize
the setup time and eliminate the need for extensive combustion modification
testing. A survey of previous test sites was made to locate a residual-oil-
fired boiler which employed staged combustion air and low excess air as the
NO control technologies. Boilers which were tested by KVB under previous
programs (cited in the document footnoted on the previous page) were reviewed.
The boiler which best met the above criteria was selected for testing.
Following test site selection, the KVB continuous monitor was shipped
to the site and installed. Continuous-monitor certification tests, as outlined
in Performance Specifications 2 and 3, 40 CFR 60, Appendix B, were then begun.
The 30-day field test was begun after the continuous monitor certifica-
tion tests were completed. The test was performed according to "Plan for
Performing Source Evaluation Tests in Support of the NSPS for Industrial
Boilers." Emissions of NO, CO, CO_ and O. were measured continuously. Partic-
ulate measurements were made in triplicate at the start, midpoint and conclusion
of the test' period. Triplicate particulate measurements were also made with
the boiler in the as-found condition. Measurements of polycyclic organic matter
were made in both the modified and as-found conditions.
The results of the 30-day test are discussed in detail in Section 3.0.
Table 1-1 is a summary of the 24-hour averages of gaseous emissions
compiled from the analyzer strip chart recordings and plant steam flow
charts. An analysis of the field test data was prepared. A log-probability
plot of 24-hour averages is presented in Figure 1-1 for the low NO condition.
The mean value for the NO is 1QO ng/J with a geometric dispersion of 1.12.
KVB 6017-1216
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TABLE 1-1. SUMMARY OF 24-HOUR AVERAGE GASEOUS EMISSIONS
SITE 2
24 HOUR DATA
OUT
DA7£
3/15/7*
3/16/7*
3/17/79
3/18/79
3/19/79
3/20/79
3/21/79
3/22/79
3/23/79
3/2«/79
3/25/79
3/26/79
3/27/79
3/28/79
3/29/79
3/30/79
3/31/79
4/ 1/79
«/ 2/79
«/ 3/79
4/ 4/79
«/ 5/79
* 4/ 6/79
4/ 7/79
«/ 8/79
4/ 9/79
4/10/79
4/11/79
4/12/79
4/13/79
4/14/79
4/15/79
4/16/79
4/17/79
4/18/79
4/19/79
02 C02 MO
LOAD VOLX VQUI PPKV
»»TH Wt
A3 HEA3 NEA3
HO
PPMV
3X0'
NO
NG/J
**«<**««***<«*.*
15.2
16.0
15.4
15.3
18.1
.7 8.7 181.
.0 9.2 183.
.5 10.
.1 11.
.1 10.
16,5 7.7 11.
16.7 7.6 12.
16.6 7.5 11.
16.5 7.6 10.
16.5 7.6 10.
16.4 7.9 9.
16,3 8.5 9,
16,4 8.0 9.
16.6 7.8 10.
16.6 7.9 10.
11.2 10.5 8.
12.9 10.5 7.
13.9 10.1 8,
13,6 10.8 7.
15.7
16.1
16.0
16.3
16.8
17.2
20.6
20.7
17.8
13.9 1
17.3
19.2
18.5
.2 ».
.1 ».
163.
157.
196.
162.
152.
132.
121.
119.
132.
135.
132.
111.
119.
0.
125.
133,
121.
127.
117.
.3 10,1 123.
.3 10.1 126.
.1 10.1 123.
.8 10.4 153.
.7 10.5 163.
.3 10.6 187,
.8 10,5 181,
.1 8.2 132,
.1 9.6 165.
.8 9.3 158.
.7 10.1 181.
|8.9 7.2 10.0 166.
19,5 7.4 to.l 173.
17.0 7.7 10.0 161.
16,8 7.9 9.9 137.
16.7 9.2 9.7 121.
266.
274.
236.
220.
273.
219.
204.
175.
163.
160.
182.
195.
183.
151.
164.
0.
216.
220.
214.
196.
163.
176.
165.
160.
194.
205.
229.
230.
218.
231.
234.
229.
218.
230.
218.
19$.
184.
147,
151.
130.
121.
151.
121.
112.
97.
90.
88.
100.
107.
101.
83.
90.
0.
119.
121.
118.
108.
90.
97.
91.
88.
107.
113.
126.
127.
120.
127.
129,
126.
120.
127.
120.
105.
101.
.»
**
*
*
**
**
«
*
«
t*
«
KVB 6017-1216
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Ol
o
-J
I
to
H
ffi
1000
900
800
700
600
500
400
300
200
£ 100
"" 90
O 80
a 70
60
50
40
30
20
10
\ V
IT
TT
x = 100 ng/J
g = 1.12
I I I I II I
I I I I I I I
I I
I I
II
.01.05.1 .2 .5 1
10 20 30 40 50 60 70 80 90 95 9a yy 99.3 yy.9 99.99
PERCENT LESS THAN
Figure 1-1. Site 2 - Residual Oil Fired Boiler-Staged Combustion Air (buuS)
-------
1.3 CONCLUSIONS
Based on the results of this 30-day field test, several important
conclusions can be drawn.
I. Staged combustion air (SCA) is an effective NOX control technology
for residual-oil-fired boilers. Staged combustion air was achieved
by removing one burner from service in a triangular burner pattern.
Removing one burner from service resulted in an NO emission
level of 100 ng/J (178 ppm at 3 percent O , dry). This level
represents a reduction of approximately 23 percent from the
condition where all burners are firing. All burners firing
produce NO emissions of 130 ng/J (232 ppm at 3 percent 0 dry).
It was not possible to operate the entire test with one burner
out of service due to steam demand. As a result, the average
NO emission level for the 30-day test was 110 ng/J <196 ppm at
3 percent O , dry).
2. Operation of the boiler in the low NO mode resulted in 48
percent higher particulate emissions than did normal operation.
The particulate emission level with all burners firing was
25.6 ng/J (0.0594 lb/106 Btu), while the low N0x mode with
one burner out of service resulted in 37.8 ng/J "(0.0878 lb/
106 Btu).
3. Boiler operation with one burner out of service results in reduced
capacity for the boiler due to oil supply pressure limitations.
In order to operate at full capacity with two burners, new oil
tips would be required. These were not available for this test.
4. The continuous-monitor system utilizing an extractive sample
system provided accurate, reliable data. The NO analyzer was
out of service for two days during the duration of the test. The
CO analyzer was out of service 23 days during the same period.
5. POM measurements showed a slight decrease when operating in the
low NOX mode. Total POM in the baseline condition were
7.6 <11.36 yg/m and 4.6 <9.7 yg/m in the low NOX mode.
KVB 6017-1216
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SECTION 2.0
INSTRUMENTATION AND PROCEDURES
This section presents a description of the instrumentation used to
measure the gaseous and particulate emissions, the test procedures, the
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 133 m high (48"W x 30"D x 72"H). A photograph of the continuous
monitor is shown in Figure 2-1. Gaseous emission measurements were made
with the analytical instruments listed in Table 2-1.
Total particulate measurements were made using an EPA Method 5 sampling
train manufactured by Western Precipitation Division of Joy Manufacturing
Company. Samples for measurement of polycydic organic matter (POM) were
obtained using an XAD-2 module supplied by Battelle Columbus Laboratories.
These modules were returned to Battelle for analysis following the test.
2.1.1 Gaseous Emissions
The continuous monitor is equipped with analytical instruments to
measure concentrations of NO, CO, C02/ and Q^ The sample gas is delivered
to the analyzers at the proper condition and flow rate through the sampling
KVB 6017-1216
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NOx
Two Pen
Chart
Recorders
Figure 2-1. Photograph of KVB Continuous Monitor for Measuring
Gaseous Emissions
KVB 6017-1216
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TABLE 2-1. ANALYTICAL INSTRUMENTATION
Emission Species
Nitrogen Oxides
Oxygen
Carbon Dioxide
Carbon Monoxide
Opacity
Manufacturer
Thermo Electron
Beckman Instrument
Horiba Instrument
Horiba Instrument
Dynatron
Measurement
Method
Chemiluminescent
Polarographic
NDIR
NDIR
Transmissometer
Model No.
IDA
742
PIR-2000
PIR-2000
1100
K7B 6017-1216
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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 in-
strumentation .
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 cf NO and O to form NO in an
excited state. Light emission results when excited NO molecules revert to
their ground state. The resulting chemiluminescence is monitored through
an optical filter by a high sensitivity photomultiplier tube, the output of
which 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 accom-
plished by means of a small bellows pump mounted on the vent of the instru-
ment downstream of a separator which insures that no water collects in the
pump.
The basic analyzer is sensitive only to NO molecules. To measure
NO (i.e., NO + NO ), the NO is first converted to NO. This is accomplished
X 2. £
by a converter which is included with the analyzer. The conversion occurs
as the gas passes through a thermally insulated, resistance heated, stain-
less 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
X «
obtained by the difference in readings obtained with and without the con-
verter in operation.
Specifications
Accuracy: 1 percent of full scale
Span drift: ± 1 percent of full scale in 24 hours
Zero drift: 1 1 ppm in 24 hours
KVB'6017-1216
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r | «.. --. - - -- ^
Proba 1 ^ ' V )
Filter --.in Filter N^^ , f
Orop-Out 7" Sample
Flask PumP
(Refri
Coiul
Opuratlng Calibration
Instrument Rantfu Gases
°2 0-10» 5%/9.27%
CO 0-1000 ppm 500 ppm/900 ppn
C02 0-20» 104/17. 8%
'«> 0-250 ppm 120.5 ppm/234 ppro
Drier
ge rat ion
euser)
~H^1 Valve
-O !""
Gauge
f>4J u. Relief
^^ Valve
cn
o
M
o>
"ero^Ef pan Zerc(%]Span Zeroftfcspan 7,orcri« Span
Vent
Vent
Vent
Figure 2-2. Schematic of continuous monitor sampling and conditioning system.
Vent
Vacuum
Pump
-------
Power requirements: 115 ± 10V, 60 Hz, 1000 watts
Response: 90 percent of F.S. in 1 sec (NO^_ mode); 0.7 sec (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, 10,000 ppm F.S.
Only the NO concentration was measured during this program. Because
of the added complexity of heated sample lines and controllers necessary
for measuring NO2 and the small percentage of NO2 in the flue gas, based
on previous tests (Reference 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 refrigerated
condenser.
3. Carbon Monoxide and Carbon Dioxide
Carbon monoxide (CO) and carbon dioxide (C02) concentrations were
measured by Horiba Instruments PIR-2000 short-path-length nondispersive
infrared analyzers. These instruments measure the differential in infrared
energy absorbed from energy beams passed through a reference cell (containing
a gas selected to have minimal absorption of infrared energy in the wave
length absorbed by the gas component of interest) and a sample cell through
which the sample gas flows continuously. The differential absorption appears
as a reading on a scale of zero to 100 percent and is then related to the
concentration of the species of interest by calibration curves supplied with
the instrument. A linearizer was supplied with the CO analyzer to provide a
linear output over the range of interest. The operating ranges for the CO
analyzer are zero to 500, zero to 1000, and zero to 2000 ppm, and the ranges
for the C0_ 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
11 KVB 6017-1216
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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
Warmup time: 30 minutes
Output: 0-10 MV
C. Oxygen
A Beckman Model 742 oxygen analyzer was used to continuously deter-
mine the oxygen content of the flue gas sample. The oxygen measuring element
contains a silver anode and gold cathode that are protected from the sample
by a thin membrane of Teflon. An aqueous KCl solution is retained in the
sensor by the membrane and serves as an electrolytic agent. As Teflon is
permeable to gases, oxygen will diffuse from the sample to the cathode in
the following oxidation-reduction reaction:
Cathode reaction: O + 2H O + 4e -» 4OH
Anode reaction: 4Ag + 4C1 * 4AgCl + 4e
With an applied potential between the cathode and anode, oxygen will
be reduced at the cathode, causing a current to flow. The magnitude of this
current is proportional to the partial pressure of oxygen present in the
sample. The instrument has operating ranges of zero to 1 percent, zero to
10 percent, and zero to 25 percent oxygen.
Specifications
Accuracy: ± 1 percent of full scale or ± 0.05 percent $2
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 ± 10 VAC, 60 Hz
12 KVB 6017-1216
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2.1.2 Particulate Emissions
Particulate samples were taken from ports on the vertical side of the
rectangular duct at the boiler outlet. The boiler had no port. Four ports
were located 0.28 m (11 inches) apart up the side of the duct. The samples
were taken using a Joy Manufacturing Company portable effluent sampler. This
system, which meets the EPA design specifications for Test Method 5 (Determination
of Particulate Emissions from Stationary Sources, Federal Register, Volume 42, No.
160, page 41754, August 18, 1977) , is used to perform both the initial velocity
traverse and the particulate sample collection. Dry particulates are collected
in a heated case that contains, first, a cyclone to separate particles larger
than 5 microns and, second, a 100-mm glass-fiber filter for retention of
particles as small as 0.3 micrometer. Condensible particulates are collected
in a train of four Greenburg-Smith impingers in a chilled water bath.
2.1.3 Polycyclic Organic Matter (POM) Emissions
Particulate and gaseous samples for analysis of POM were taken at the
sample port used for Method 5 particulate tests. The sampling system is a
modified Method 5 sampling train developed by Battelle Columbus Laboratories.
A combination of conventional filtration with collection of organic vapors by
means of a high-surface-area polymeric adsorbent (XAD-2) has proved to be highly
efficient for collection of all but the more volatile organic species. The
modified sampling system consists of the standard EPA train with the adsorbent
sampler (Figure 2-3) located between the filter and the impingers. With this
system, filterable particulate can be determined from the filter catch and
the probe wash according to Method 5; the organic materials present can be
determined from the analysis of the filterable particulate and the adsorbent
sampler catch. The impingers are only used to cool the stream and protect
the dry-gas meter, and their contents are discarded.
13 KVB 6017-1216
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GLASS WATER
JACKET
8-MM GLASS
COOLING COIL
ADSORBENT
GLASS WOOL PLUG
RETAINING SPRING
28/12 BALL JOINT
FLOW DIRECTION
GLASS FRITTED
DISC
FRITTED STAINLESS STEEL DISC
15-MM SOLV-SEAL JOINT
Figure 2-3. Mark III adsorbent sampling system.
14
KVB 6017-1216
-------
2.1.4 Opacity Measurement
Stack opacity was measured with a Dynatron Model 1100 Opacity Monitor-
ing System. The Model 1100 opacity monitor is a double pass transmissomecer
which measures the light transmittance through a flue gas. The transceiver
unit contains the light source, the detector, and electronic circuitry. A
reflector is mounted in the end of a slotted probe which is attached to the
transceiver and is inserted into a stack or duct through a conventional stack
sampling port. The probe causes negligible flow disturbance, and an air purge
keeps the optical window and reflector clean. The transceiver output is
transmitted to a portable control unit which displays either opacity or
optical density automatically correlated from differences between the path
length of the transmissometer and the mean diameter of the stack outlet.
Specifications
Peak spectral response: 500 to 600 nm
Mean spectral response: 500 to 600 nm
Relative response: < 10 percent
Angle of view: < 4 degrees
Angle of projection: < 2 degrees
Calibration error: < 2 percent
Response time: 1 second
Zero drift: < 1 percent (24 hours)
Calibration drift: < 1 percent (24 hours)
Operational test period: 168 hours
Output: 0 to 1 VDC
Power requirements: 115 VAC/60HZ
Temperature range: 40°F to 125°F
Weight: 27 pounds (approximate)
The transceiver lenses are cleaned daily, and an air purge is used to
keep the lenses free of dirt while inserted in the stack.
15 KVB 6017-1216
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2.2 BOILER DESCRIPTION AND CHARACTERISTICS
The boiler at Site 2 was manufactured by Babcock and Wilcox in 1935.
It is an integral furnace watertube boiler with an original rated capacity of
26.4 MW (90,000 Ib steam/hr). The current top load capability of 79,000 Ib
steam/hr is limited by the fan. The furnace wall consists of watertubes
76 mm (3 inches) in diameter spaced 260 mm (10.25 inches) on centers. The
wall exposure between the tubes consists of refractory; the furnace was
rebricked in 1972. The boiler operates at a nominal steam pressure of
2.2 MPa (320 psig) and a steam temperature of 493K (428°F).
The boiler is fired with three B&W steam-atomized burners arranged
in a triangular pattern with the top burner spaced directly above the center
of the lower two burners. The vertical spacing is 0.91 m (36 inches); the
horizontal spacing is 0.94 m (37 inches). The oil guns use a B&W Y-jet steam
atomizer with the steam pressure at the burner nominally 0.24 MPa (35 psi)
greater than the oil pressure. The boiler fires No. 6 oil, and the temperature
of the oil at the burner was approximately 367K (200°F). The nominal oil
pressure at top load was 0.58 MPa (85 psi). The boiler is outfitted with a
tubular air heater to preheat the combustion air.
The test boiler was situated in the main power plant of a. chemical
process plant and was one of four boilers used for supplying process steam.
The NO control technology employed at this test site was staged combustion
X
air, which was shown previously to be effective for reducing NO emissions
from this boiler. Staged combustion was achieved by removing the upper
burner (#1) from service. This does not upset the symmetry of the furnace
because of the triangular arrangement of the burners. By terminating the
fuel flow to the #1 burner and leaving the air register 100 percent open,
the excess air to the active burners was reduced to two-thirds of its original
value with all burners in service, because the remaining one-third of the air
was injected through the out-of-service burner port. When firing with one
burner out of service, the maxinnm steam flow possible was 17.6 MW thermal
16 KVB 6017-1216
-------
output (60,000 Ib/hr). The load was restricted to this value by fuel pressure.
A maximum fuel pressure of 0.689 MPa (100 psi) was available which, coupled
with the oil gun orifices, limited the fuel flow.
2.3 DAILY TEST ACTIVITY
This section describes the daily test activity at Site 2 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 O ) were
continuously recorded on strip chart recorders. Gaseous data were read five
times daily and recorded on the form shown in Figure B-6, Appendix 3. These
data were subsequently used for verification of the data reduced from the
strip charts for analysis. Boiler operating data were recorded periodically
by KVB personnel. Daily charts of steam flow for the entire test period
were provided by the boiler operators. The strip chart recorders recorded
gaseous emissions 24 hours per day, 7 days per week. No control room data
were recorded on weekends; however, the technician did calibrate the
instruments on the weekend.
Daily tasks consisted of (1) instrument calibration and recording of
control room and emissions data; (2) consultation with boiler operators
regarding boiler operation in the low NO mode; (3) periodic maintenance of
2C
instruments and sample system; (4) visual inspection and troubleshooting of
the sampling system and instrumentation console; and (5) procuring supplies
and equipment for the particulate and Method 7 tests.
17 KVB 6017-1216
-------
TABLE 2-2. SCHEDULE OF DAILY EVENTS - SITE 2
Time Event
0800 Calibrate (zero and span) gaseous
analyzers (NO, C0_, CO, and O ).
Record gaseous emissions data. Record
boiler control room data. Consult with
operators concerning boiler operation.
0845 Calibrate opacity monitor.
0900 Perform daily systems checkout.
1000 Calibrate and record gaseous emissions
data.
1200 Calibrate and record gaseous emissions
data. Record control room data.
1400 Calibrate and record gaseous emissions
data.
1600 Calibrate and record gaseous emissions
data. Record control room data.
1700 Calibrate analyzers prior to departing
plant. Perform visual check of sampling
systems and boiler operation. Leave
instructions with operators.
18 KVB 6017-1216
-------
SECTION 3.0
TEST RESULTS
This section summarizes the emission and efficiency data collected on
the residual-oil-fired boiler. The NO control technology employed on this
boiler was staged combustion air. The boiler was tested in the as-found
condition initially and in the low NO mode for 32 days. The boiler fires
X
No. 6 fuel oil. The results presented herein summarize the gaseous and
particulate emissions data, efficiency, and present conclusions for the
boiler operating under low NO conditions for extended duration.
3.1 CONTINUOUS-MONITOR CERTIFICATION TESTS
The continuous monitor described in the previous section was used
to measure the boiler gaseous emissions. Following shipment to the test
site, the monitoring system was installed and certification tests performed
in accordance with Performance Specifications 2 (PS2) and 3 (PS3), 40 CFR 60,
Appendix B (reproduced here as Appendix D). This appendix establishes
minimum performance specifications that the NO monitoring system must meet
in terms of eight parameters: accuracy, calibration error, 2- and 24-hour
zero drifts, 2- and 24-hour calibration drifts, response time, and operational
period.
The continuous-monitor system was installed and instruments were
initially calibrated on March 13, 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.
Also shown in the table are the monitor specifications extracted from PS2 and
PS3. Included in this table is the performance of the CO analyzers which is
19 KVB 6017-1216
-------
TABLE 3-1. SCHEDULE OF CERTIFICATION TEST EVENTS
Date
3/14/79
3/15/79
3/1S/79
3/15/79
3/15/79
3/15/79
3/15/79
3/15/79
3/16/79
3/16/79
3/16/79
3/16/79
3/16/79
3/17/79
3/18/79
3/19/79
3/19/79
3/19/79
3/19/79
3/19/79
3/19/79
3/19/79
3/19/79
3/19/79
3/19/79
3/19/79
3/19/79
3/19/79
3/19/79
3/20/79
3/20/79
3/20/79
3/20/79
3/20/79
3/21/79
4/19/79
Time
1000
1000
1200
1400
1600
1800
2000
1000
1200
1400
1600
1800
1000
1000
1000
1000
105O
1150
1200
1250
1355
1400
1455
1555
1600
1655
1755
1800
1855
1000
1100
1200
1400
1500
10OO
4930
Event
Initial 24-hour zero and span reading.
Initial 2-hour zero and span reading.
1st 2-hour zero and span drift point.
2nd 2-hour zero and span drift point.
3rd 2-hour zero and span drift point.
4th 2-hour zero and span drift point.
5th 2-hour zero and span drift point.
1st 24-hour zero and calibration drift
point. Initial 2-hour zero and calibra-
tion reading - 2nd day.
6th 2-hour zero and span drift point.
7th 2-hour zero and span drift point.
3th 2-hour zero and span drift point.
9th 2-hour zero and span drift point.
2nd 24-hour zero and calibration drift
point.
3rd 24-hour zero and calibration drift
point.
4th 24-hour zero and calibration drift
point.
5th 24-hour zero and calibration drift point.
1st sat of relative accuracy samples taJcen.
2nd set of relative accuracy samples taken.
10th 2-hour zero and span drift point.
3rd set of relative accuracy samples taken.
4th set of relative accuracy samples taken.
llth 2-hour zero and span drift point.
5th set of relative accuracy samples taken.
6th set of relative accuracy samples taken.
12th 2-hour zero and span drift point.
7th set of relative accuracy samples taken.
8th sac of relative accuracy samples taken.
13th 2-hour zero and span drift point.
9th set of relative accuracy samples taken.
6th 24-hour zero and calibration drift
point.
Instrument response rim tests.
14th 2-hour zero and span drift point.
15th 2-hour zero and span drift point.
Calibration error determination.
7th and final 24-hour zero and calibration
drift point.
Relative accuracy samples taken < 3/19
series duplicated.
20
KVB 6017-1216
-------
TABLE 3-2. INSTRUMENT SPECIFICATIONS AND PERFORMANCE
Parameter
Specifications*
Performance
A. Thermo Electron Series 10 NOx Analyzer
1. Accuracy
2. Calibration error mid
high
3. Zero drift (2 -hour)
4. Zero drift (24-hour)
5. Calibration drift (2-hour)
6. Calibration drift (24-hour)
7 . Response time
8. Operational period
B. Horiba Instruments PIR 2000 C02
1. Zero drift (2-hour)
2. Zero drift (24-hour)
3. Calibration drift (2-hour)
4. Calibration drift (24-hour)
5. Response time
6. Operational period
C. Beckman Instruments Model 742 O
1. Zero drift (2- hour)**
2. Zero drift (24- hour)**
3. Calibration drift (2-hour)
4. Calibration drift (24- hour)
5. Response time
6. Operational period
D. Horiba Instruments PIR 2000 CO
1. Calibration error mid
high
2. Zero drift (2-hour)
3. Zero drift (24 -hour)
4. Calibration drift (2 -hour)
5. Calibration drift (24 -hour)
6. Response time
7. Operational period
^ 20% of mean ref. value
- 5% cal gas value
5 5% of cal gas value
2% of span
2% of span
2% of span
2.5% of span
1.5- minute maximum
16 8- hour minimum
Analyzer
< 0.4 pet CO2
< 0.5 pet CO2
< 0.4 pet C02
^0.5 pet C02
10 minutes
168- hour minimum
Analyzer
< 0.4 pet O2
< 0.5 pet O2
< 0.4 pet O2
< 0.5 pet 02
10 minutes
168- hour minimum
Analyzer
S 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
8.72%
4.30%
3.40%
0.88%
1.68%
1.68%
1.08%
5.5 sec.
0 %
0.04%
0.13%
0.34%
4.2 sec.
DNA
DNA
0.09
0.25%
10.1 sec.
4.8%
1.4%
0.12%
0.23%
0.17%
0.39%
8.5 sec.
*Performance specifications from 40 CFR 60, Appendix B, reproduced here
as Appendix D.
**Instrument has no zero adjustment.
21 KVB 6017-1216
-------
not covered by the performance specification. The CO analyzer is used to
monitor the combustion conditions in the boiler since it is a very sensitive
indicator of combustion performance. Tables C-l through C-18, Appendix C,
show the performance of each of the analyzers for the certification tests.
The data presented in Table 3-2 show analyzers in the continuous
monitor bettered the performance specification values for each parameter
for each instrument.
Certified calibration gases were obtained from Scott Environmental
Technology Inc. The calibration gases included 50 percent and 90 percent
span gases for the NO, CO^, CO, and O analyzers, and a zero gas. In addi-
tion to the certified analysis supplied by the vendor, sample flasks were
taken for each calibration gas and sent to an independent laboratory for
analysis.
Relative accuracy tests for the NO analyzer were performed as outlined
in PS2 using EPA Reference Method 7 (phenoldisulfonic acid [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 were taken. All sample
flasks were returned to an independent laboratory for analysis. The results
of the relative accuracy determination are shown in Tables C-17 and C-18 for
the start and end of the 30-day tests. Both tests showed that the NO instru-
ment greatly bettered the accuracy requirements of PS2. The relative accuracy
of the Thermo Electron NO analyzer was about 8 percent based on the first test
series and about 10.5 percent based on the final test series. The relative
accuracy requirement published in PS2 is < 20 percent of mean reference value.
3.2 RESIDUAL-OIL-FIRED BOILER TESTS
The continuous monitor was installed by KVB personnel on March 13, 1979,
at Site 2, a residual-oil-fired water tube boiler. A single unheated 9.5 mm
(3/8-inch) nylon sample line was strung from the duct downstream of the
combustion air preheater to the continuous monitor. A single stainless steel
filter was installed on the centerline of the duct. Particulate samples were
taken from three ports on the side of the duct.
22 KVB 6017-1216
-------
The boiler was initially tested in the as-found condition on
March 15, 1979. The boiler load during this test was 16.1 MW thermal input
(55,000 Ib steam/hr). All burners were in service at this time.
Following the tests in the as-found condition, boiler operation was
adjusted, under KVB supervision, to the low NO configuration. The top
burner in the triangular arrangement was taken out of service. All air
registers remained 100 percent open.
Triplicate Method 5 particulate tests were completed after boiler
operation in the low NO mode stabilized. Triplicate Method 5 measurements
under low NOx operation were also made at the end of the 30-day test period.
Method 5 particulate tests were also conducted with all burners in service.
During one low NO particulate test and one baseline test, samples were
collected for POM analysis. The method for collecting this sample was
described in paragraph 2.1.3.
Fuel oil samples were collected periodically and submitted to an
independentlaboratory for analysis. Fuel samples were taken each time a
particulate test was made and each time an oil delivery or change of tanks
occurred.
A daily summary of the gaseous emissions observations is presented
in Table 3-3 for each day of testing. In addition to the strip chart recording
of each analyzer, readings were taken five times daily beginning at 0800.
Boiler operating data were recorded four times daily and a 24-hour record
of steam flow was obtained. A control room data sheet for this test site
is included in Appendix B.
3.2.1 Gaseous Emissions
The boiler at Site 2 was tested during a previous EPA-sponsored
program (Reference 1). During the-previous tests the effect of boiler load
on NOx emissions was determined over a range of thermal output of 11.7 to
23 KVB 6017-1216
-------
TABLE 3-3. SUMMARY OF OBSERVATIONS, COMMENTS AND GASEOUS AND PARTICULATE EMISSIONS SITE 2,
RESIDUAL-OIL-FIRED BOILER
K>
Ch
O
a\
Oat*
1-14
1-15
1-16
1-17
1-18
1-19
1-20
1-21
1-22
1-11
1-24
1-25
1-26
1-27
1-28
1-29
1-10
l-ll
4-1
4-2
4-1
4-4
4-5
4-6
4-7
4-8
4-9
4-10
4-11
4-12
4-11
4-14
4-15
4-16
4-17
4-18
4-19
Steal* Flow
HM 101 lb/hr
16.4 56.0
16.1 55.0
16.0 54.7
15.1 52.2
18.1 61.8
16.4 56.9
16.6 56. a
16. « 56.5
16.4 56.0
16.6 **
16.4 &6.0
16.1 55.8
16.4 56.0
16.6 56.8
16-5 56.1
»» 11.0
12.6 4J.O
U-9 47.4
13-6 46.4
15.8 51.8
16.1 55.0
16.0 54.8
16.0 54.5
16.1 55.8
17.2 58.7
20.6 70.1
21.2 '2.5
20.2 69.0
11.9 47.5
16.1 55.7
19.6 66. 8
18.5 63.1
18.9 64.5
19.7 67.1
16.4 56.0
16.8 57.5
16.5 56.1
i
°2
» dry
a. a
a. 9
8.1
7.J
B.I
7.8
7.6
7.}
7.6
1.6
8.1
8.1
7. B
7.9
7.9
10.7
10.1
10.2
11.2
8.0
8.6
7.1
7.2
6.9
7.1
6.1
6.55
7.7
10.0
7.6
9.2
7.0
7.1
7.5
7.6
8.1
8.0
» dry
B.S
9.5
11.2
12.2
9.6
12.0
12. B
10.5
10.2
9.9
9.7
9.7
10.2
10.4
10.2
7.7
a.a
8.2
7.4
9.7
9.9
10.1
10.1
10.2
10.4
10.5
10.7
9.9
7.9
10.0
8.4
10.0
10.1
10.1
9.9
9.7
9.8
NO
PP» ng/J
281 158
252 142
186 104
219 114
240 115
194 109
167 94
165 91
170 96
166 91
194 109
118 77
iao 101
148 81
180 101
I.O.O.8. -
220 124
218 122
226 127
161 90
1.0.0.8. -
161 90
161 92
161 90
187 105
210 129
221 125
214 112
212 110
216 121
241 117
252 141
209 117
242 116
224 126
165 91
164 92
CO
PP» ng/J
Instrument
out of
Service
21
7
19 6
11 6
22 B
20 7
21 8
19 6
19 6
25 9
25 9
Psrtlculal*
lb/104 Dlu ng/J
0.0551 21.676
0.0475 20.40*
0.0849 16.521
0.0760 12.666
0.065J 28.O84
.
0.0757 12.557
0.1088 46.785
0.1018 44.650
0.0882 17.941
Opacity
0
a
4
1
0
0
0
0
4
0
4
0
1
1
0
0
1
7
9
9
a
10
1
11
4
2
Temp
r
440
440
458
460
455
415
428
428
419
Comment*
Baseline, all burners firing
Baseline, part test 1-1, 1-2,
all burners firing
Baseline of BOOS*
Particular, test 2-1
BOOS, All burner* firing
P articulate tests 1-1, 1-3, PDS,
BOOS
BOOS
BOOS
BOOS
BOOS
BOOS
BOOS
Technician ill, BOOS
Vacuisa pump out NO 5 hr avg, BOC
Vacuun punp out, low load, BOOS,
Low load. High O2> BOOS
Low load, High O}
Low load, High o^, BOOS
BOOS
BOOS
BOOS
BOOS
BOOS
All burner* firing
All burners firing
High load
High load, »11 burner* tiring
High load. High o^, DOGS
High load, all burners firing
High load, all burners firing
All burners firing
All burners firing
All burners firing
All burner* firing partlculate/
POM 1-1
Partlculate/POH test 2-4, BOOS
Partlculate 2-5, 2-6, BOOS
POS flasks
-------
23.1 MW (40,000 to 79,000 Ib/hr steam flow). These data are shown in
Figure D-l in Appendix D which shows that the maximum NO levels occur at
approximately 19.6 MW (67,000 Ib/hr steam flow). The maximum NO level
measured was 245 ppm (3 percent 0 , dry). The NO level at 17.6 MW
A, X
(60,000 Ib/hr), the test condition for one burner out of service, was
240 ppm.
During this program, no provision was included for evaluating the
effect of various operating parameters on NO emissions. Instead, the
X
conditions previously determined to yield low NO operation were duplicated
X
as nearly as possible. The boiler was tested in the as-found condition at
the initiation of the test program. Since the maximum capacity of the boiler
with one burner out of service is approximately 16.4 MW (56,000 Ib/hr steam
flow) the boiler was tested in the as-found conditions at this load.
The effect of excess oxygen on NO emissions is shown in Figure 3-1
X
for the boiler at Site 2. Excess oxygen was not intentionally varied, but
normal operation resulted in some variation in excess oxygen due to operator
technique and the lack of sufficient instrumentation and controls to
accurately hold a given excess air condition. The lower curve corresponds
to operation with one burner out of service (staged combustion air). The
upper curve represents the condition where all burners are firing normally.
The solid points in the upper curve are at a higher load condition: 19.6 to
21.1 MW (67,000 to 72,000 Ib steam/hour). As the previous data showed,
operation at higher load resulted in about a 5 ppm increase over the test
load condition.
Over the 30-day period during which the test was performed, there
were occasions where the demand was greater than the boiler could provide
with one burner out of service. The operators then put the third burner
back, in service. As a result, the 30-day average represents operation in
the low NO mode except for the periods when steam demand precluded staged
combustion.
25 KVB 6017-1216
-------
400
300
ro
en
a\
o
I
H
to
H
cr>
o
t»
200
100
Solid Figures Represent High
Load Conditions
Fuel: No. 6 Oil
All Burners In Service
O.
One Burner Out of Service
10
EXCESS OXYGEN, %
Figure 3-1. The Effect of Excess Oxygen on NO Emissions
Site 2 - Residual-Oil-Fired Boiler.
-------
3.2.2 Particulate Emissions
The results of the particulate tests conducted at Site 2 are presented
in Table 3-4 for the baseline and low NO test conditions. Two of the tests
were also used for collecting samples for analysis of polycylic organic
matter (POM) by modifying the EPA Method 5 train as described in paragraph
2.1.3. The average particulate loading for baseline conditions, all burners
firing, was measured at 25.6 ng/J (0.0594 lb/10 Btu). The average particulate
in the low NO condition, one burner out of service, was 37.8 ng/J (0.0878
6 X
lb/10 Btu). The average particulate loading increased 48 percent due to
operation in the low NO mode.
Visual inspection of the particulate filter in the sampling train
showed a much darker particulate deposit, indicating that the particulate
contained considerable unburned carbon in the low NO mode.
X
The particulate data for this test site were plotted as a function of
excess oxygen in the stack. Figure 3-2 shows particulate loading as a function
of stack excess oxygen. The data indicate that particulate loading is not
a function of excess oxygen alone. It can also be seen from these data that
operation in the low NO mode with one burner out of service results in higher
particulate loading.
3.2.3 POM Emissions
Samples were collected for analysis of polycyclic organic matter (POM)
using a Method 5 sampling train with XAD-2, a POM absorber, inserted. Sample
time was extended to two hours to provide a large enough sample for Battelle
to analyze. Following the sampling period, the organic resin module was sealed
and returned to Battelle Columbus Laboratories for analysis. The sampling
probe and glassware were washed with a 50-50 mixture of methylene chloride and
methanol per Battelle instructions. The filter and wash were also sent to
Battelle following weighing.
These samples were analyzed by capillary-El GC-MS utilizing a 30M SE-52
column with hydrogen as a carrier gas. All data were collected by single ion
monitoring to improve selectivity and sensitivity.
27 KVB 6017-1216
-------
TABLE 3-4. PARTICULATE DATA SUMMARY FOR SITE 2
RESIDUAL-OIL-FIRED BOILER
Load
Test No.
1-1
1-2
2-1
2-2
2-3
1-3
2-4
2-5
2-6
Date
1979
3-15
3-15
3-16
3-19
3-19
4-17
4-18
4-19
4-19
MW
16.1
16.1
16.1
16.4
16.4
16.4
17.0
16.4
16.4
103 Ib/hr
55
55
55
56
56
56
58
56
56
°2
8.9
9.0
8.1
7.7
7.4
7.6
8.1
7.8
8.0
Opacity
0
0
3
2
2
11
3
2
2
Particulate
ng/ J
20.4
23.7
36.5
28.1
32.7
32.6
46.8
44.6
37.9
lb/106 Btu
0.0475
0.0551
0.0849
0.0653
0.0760
0.0757
0.1088
0.1038
0.0882
Description
Baseline
Baseline
Low NO
X
Low NO
X
Low NO
X
Baseline/POM
Low NO /POM
X
Low NO
X
Low NO
X
en
o
-------
K)
IQ
CTi
O
H
J
V
IO
O
.-1
^v
XI
H
h>
->x
G
g
H
9
H
1
d.
DU.U
(0.140)
50.0
(0.116)
40.0
(0.093)
30.0
(0.070)
20.0
(0.047)
10.0
(0.023)
0
I | 1 1 I i I
Load (NOM) - 16.4 MW (56,000 Ib steam/hour
_ Fuel - No. 6 Oil
0°
- -
^T~\
*^
Q^\
«» "~"
O
A
A
/\ Baseline conditions
O Low-NO conditions
x
(LEA + BOOS)
A 1 1 1 1 1 1 1
0 6.0 7.0 8.0 9.0 10.0 11.0. 12.0 13. (
EXCESS OXYGEN, %
Fiaure 3-2. Particulate Loadinq vs. Stack Excess Oxygen for 30-Day Test
Location 6017-2
-------
The results of the analyses are presented in ug per total sample. The
quantitative detection limit was 0.5 ug; thus samples with POM present at levels
lower than this are reported as <0.5 ug (the standard deviation at lower levels
was prohibitively high for accurate quantification). Samples reporting POM values
of ND (none detected) are at a level of less than 0.1 Ug (the approximate
qualitative detection limit). The standard deviation on points around 0.5 ug
averaged ±20 percent. At levels around 5 ]ig it averaged ±15 percent, and at
levels above 12 ug the standard deviation averaged ±10 percent.
The results of the Battelle analyses are presented in Table 3-5 for
the low N0x and baseline operating conditions. The first three columns present
the data for the low NO test; the last three columns represent the baseline
condition. The XAD-2 module was analyzed separately, with the filter and probe
wash samples combined for analysis.
The data indicate a slightly lower (18 to 30 percent) concentration of
POM when operating in the low NO mode. The only components with significant
levels are phenanthrene, anthracene, and methyl anthracenes/phenanthrenes.
POM accounted for less than 0.01 percent of the total particulate.
3.2.4 Boiler Efficiency
Boiler efficiency calculations were made for as-found and low NO
X
operating conditions. The ASME Abbreviated Efficiency Test method was used
to determine the boiler efficiency- This test method is described in Appendix A.
Fuel oil samples were collected during each particulate test and when
oil shipments were received or tanks changed. Fuel oil samples were submitted
to an independent laboratory for ultimate and heating value analyses. The
results of the fuel oil analyses are tabulated in Table 3-6. The data,
tabulated chronologically, indicate that oil properties did not change
significantly during the test period.
Table 3-7 presents a summary of boiler efficiency measurements made
at baseline and low NO conditions. The average boiler efficiency under
baseline conditions (all burners firing) was 81.9 percent; average efficiency
under low NO conditions (one burner out of service) was 82.6 percent or an
average increase of 0.7 percent.
30 KVB 6017-1216
-------
Table 3-5. SUMMARY OF POM ANALYSES FOR SITE 2 - RESIDUAL-OIL-FIRED BOILER
o
M
^1
M
K)
I'OM
Mufnanthruiui
Anthraceru;
Methyl /Vnthracuiius/Pttenanthreiiuti
Fluora«tl,u,«
Pyrtjnu
Methyl Pyruiie/Pluuranlhunu
Hunzo| c] i>huniinthren&
bun;: |d)antlti jcene
Chryiiuno
Methyl Chrysencs
t)i me thylbunz anthracenes
Uunzo Muo ran L hurt es
Benz | u) pyrerui
Benzlalpyi.,..,,
1'ury June
liideiio-|>y_reiie
J-IU-lh/Kholantlirun.;
Dihun^.inlhr iiculieb
Dilju-nzjjyi i;iu 11
CotOh-jll..
XAD-2
MODULE
I«J
1.8
0.9
3.6
0.5
0.6
-0.5
ND
<0.5
0.6
ND
ND
0.9
0.7
ND
ND
-------
TABLE 3-6. SUMMARY OF FUEL OIL ANALYSES FROM
SITE 2, RESIDUAL-OIL-FIRED BOILER
Dates and Sample Numbers
Carbon, %
Hydrogen, %
Nitrogen, %
Sulfur, %
Ash, %
Oxygen (by difference), %
API Gravity at 60 °F
Gross Heat of Combustion, Btu/lb
Net Heat of Combustion, Btu/lb
Carbon, %
Hydrogen, %
Nitrogen, %
Sulfur, %
Ash, %
Oxygen (by difference), %
API Gravity at 60 °F
Gross Heat of Combustion, Btu/lb
Net Heat of Combustion, Btu/lb
3-15-79
1
85.78
12.26
0.27
0.97
0.021
0.70
21.6
21.7
19,000
17,900
3-16-79
2
85.82
12.16
0.28
0.93
0.027
0.78
21.6
20.9
19,050
17,950
3-19-79
3
85.86
12.14
0.28
0.94
0.027
0.75
21.6
18,950
17,830
3-20-79
4
85.76
12.03
0.24
0.99
0.028
0.95
19,000
17,890
4-12-79
5
86.21
12.08
0.24
0.85
0.026
0.59
18,960
17,850
4-17-79
6
86.24
12.10
0.24
0.88
0.025
0.52
21.9
19,020
17,920
Carbon, %
Hydrogen, %
Nitrogen, %
Sulfur, %
Ash, %
Oxygen (by difference) , %
API Gravity at 60°F
Gross Heat of Combustion, Btu/lb
Net Heat of Combustion, Btu/lb
4-18-79
7
86.00
12.06
0.27
0.96
0.024
0.69
21.2
19,000
17,900
4-18-79
8
85.97
11.97
0.27
0.96
0.024
0.81
20.7
IS, 980
17,890
4-19-79
9
85.85
11.97
0.28
1.02
0.024
0.86
20.9
19,040
17,950
32
KVB 6017-1216
-------
TABLE 3-7. SUMMARY OF BOILER EFFICIENCY CALCULATIONS FOR
SITE 2, RESIDUAL-OIL-FIRED BOILER
Test No.
Date
Test Load
103 Ib/hr
MW
% of Capacity
Stack 02/ I
Stack CO, ppm
Stack Temp. (K/°F)
Ambient Temp. (K/°F)
Uoiler Heat Losses
Dry Gas, %
Moisture in Fuel, %
Moisture from 11- , %
Combustibles, %
Radiation, %
Total Losses, »
Boiler Efficiency, %
1-1
3/15/79
55
16.1
61.11
8.9
I.O.O.S.
500/440
294/70
10.58
0.0
6.76
0.0
1.0
18.34
81.66
Average
Average
1-2
3/15/79
55
16.1
61.11
8.9
I.O.O.S.
500/440
294/70
10.58
0.0
6.76
0.0
1.0
18.34
81.66
2-1
3/16/79
55
16.1
61.11
7.5
510/458
294/70
10.42
0.0
6.69
0.0
1.0
18.11
81.89
Baseline Efficiency n «
Low NO Efficiency y =
2-2
3/19/79
56
16.4
62.22
7.8
508/455
294/70
8.79
0.0
6.57
0.0
1.0
16.35
83.65
81. 9%
82.6*
2-3
3/19/79
56
16.4
62.22
7.8
511/460
294/70
8.90
0.0
6.57
0.0
1.0
16.47
83.53
1-3
4/17/79
56
16.4
62.22
7.6
497/435
294/70
10.03
0.0
6.65
0.0
1.0
17.68
82.32
2-4
4/18/79
58
17.0
64.44
B.I
493/428
294/70
10.79
0.0
6.59
0.0
1.0
18.38
81.62
2-5
4/19/79
56
16.4
62.22
8.0
493/42B
294/70
9.89
0.0
6.57
0.0
1.0
17.46
82.54
2-6
4/19/V9
56
16.4
62.22
8.0
0.0
499/439
294/70
10.19
0.0
6.57
0.0
1.0
17.76
82.24
cn
o
CTi
-------
3.2.5 Data Reduction
The gaseous emissions data measured by the analyzers were recorded
on strip chart recorders as described earlier. An automatic data logger was
ordered but was not available for this 30-day test. The only alternative
was manual reduction of strip chart records and punched cards for computer
data input as was the case for Site 1. This procedure required a very large
manpower effort to produce the data required .for analysis.
Strip chart records were collected from the recorders along with
copies of the appropriate control room data logs. The recorder charts
were reviewed to detect any possible data gaps. In addition, the strip
chart records were verified by comparison with measurements recorded by a
technician on a two-hour basis.
A tabulation of 15-minute averages was compiled for the entire test
period. After the data were compiled, they were spot checked and edited
to detect obvious errors and anomalies. The data were then keypunched on
cards for input to the computer. Figure 3-3 shows an example of the list
of 15-minute averages. The entire list of 15-minute averages is presented
in Appendix F.
After data editing was completed, 24-hour averages were calculated
For an average to be valid, at least 75 percent of the 15-minute points in
that interval had to be valid. Figure 3-4 shows a summary of the 24-hour
averages for the 30-day test at Site 1.
A statistical summary was prepared to determine the following
parameters for the 24-hour averages: mean, standard deviation, maximum,
minimum, range, and average deviation. These parameters were calculated
assuming the data were normally distributed. The 24-hour averages were
tabulated in ascending order and divided into 10 groups. A frequency
histogram was then prepared. Table 3-8 presents the frequency distribution
of the 24 hour averages of NO emissions of all data. These data were then
plotted to determine the distribution. When the data were plotted on normal
probability paper (Figure 3-5) it was apparent that the data were not normally
34 KVB 6017-1216
-------
««*«»««»»******«*****«**«***
** 15 MIN. DATA
«* DRT STACK CA3 CONCENTRATION
**
**
*«
** DATE
ftftftftftftftft it to a
* 3/14/79
** 3/14/79
** 3/I4/79
** 3/14/79
** 3/14/79
* 3/14/79
** 3/14/79
3/14/79
«* 3/14/79
** 3/14/79
* 3/14/79
« 3/14/79
* 3/14/79
** 3/14/79
* 3/14/79
** 3/14/79
* 3/14/79
** 3/14/79
** 3/14/79
* 3/14/79
** 3/14/79
«* 3/14/79
* 3/14/79
«« 3/14/79
* 3/14/79
** 3/14/79
3/10/79
** 3/14/79
» 3/14/79
* 3/14/79
** 3/14/79
« 3/14/79
«* 3/14/79
* 3/14/79
«« 3/14/79
*» 3/14/79
*« 3/14/79
** 3/14/79
** 3/14/79
** 3/14/79
** 3/14/79
3/14/79
** 3/14/79
*« 3/14/79
* 3/14/79
»* 3/14/79
** 3/14/79
*« 3/14/79
TIME
ft ft ft ft ft ft
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
1830
184S
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
MWTH
11.4
ll.o
11.4
H.4
13.6
13,6
13.6
13.6
16.3
16.3
16.3
16.3
16.4
16.4
16.4
16.4
16.4
16.4
]6.4
16.4
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
OS
VOL*
MEAS
9.6
9.7
9.7
9.7
9.6
9.1
8.5
8.4
8.3
8.4
8.3
8.3
8.3
8.3
8.3
8.3
8.4
8.5
8.5
8.5
8.5
8.5
8.5
8.6
8.6
8.6
8.7
8.6
8.6
8.6
8.5
8.5
8.5
8.5
8.5
8.5
8.5
8.5
8.5
8.6
8.5
8.5
8.5
8.5
8.5
8.5
8.6
8.7
C02
VOLX
MEAS
7.9
7.9
7.9
7.9
8.3
8,7
8.9
8.9
8.9
8.9
8.9
8.9
8.9
8.9
8.9
8.9
8.9
8.9
8.9
8.9
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.9
8.9
8.9
8.9
.9
.9
.9
.9
.9
*
8.
8.
8.
8.
8.8
8.8
8.8
8.7
8.7
NO
PPMV
MEAS
ft ft ft ft ft ft 1
162.
161.
156.
153.
165.
173.
184.
186.
189.
191.
193.
196.
199.
200.
203.
203.
191.
191.
191.
190.
190.
189.
189,
188.
186.
185.
183.
182.
180.
179.
178.
177.
176.
173.
172.
172.
172.
173.
173.
171.
173.
180.
182.
185.
189.
191.
194.
197.
NO
PPMV
NO
NG/J
»*
**
**
**
*«
3X02 *
257. 1«2.
258.
209,
246,
262.
263.
267.
268.
269.
273.
275.
279.
282.
285.
289.
289.
270.
275.
270.
274.
270.
270.
270.
273.
272.
270.
268.
266.
262.
260.
258.
256.
253.
250.
248.
249.
250.
251.
251.
248.
250.
260.
263.
267.
270.
277.
282.
289.
102.
137,
136,
105,
105.
107,
t«8.
Ifl8,
151.
152.
154.
156,
157,
159.
159.
151.
151.
151.
151.
151.
151.
151.
150.
150.
109.
108.
107.
100.
103.
102.
101.
100.
138.
137.
137.
138.
138.
138.
137.
138.
103.
105.
107.
151.
153.
156.
159.
**
*
**
**
**
**
**
**
*
**
**
*
*«
**
**
**
*«
**
**
*
**
*
*
*«
**
**
*
**
*«
**
*
»»
*
»»
**
**
*»
**
»*
**
**
*
*«
**
**
*«
******««
Figure 3-3. Format of 15-Mirmte Emissions Data, Site 6017-2
35 XVB 6017-1216
-------
«**
24 HOUR OAT*
0»r 3T*C* G*3 CONCENTRATION
*
DATE 7
!
3/14/79
* 3/15/79
3/16/79
3/17/79
3/18/79
* 3/19/79
3/20/79
3/21/79
3/22/79
3/23/79
3/24/79
3/25/79
3/26/79
3/27/79
3/28/79
3/29/79
3/30/79
3/31/79
4/ 1/79
4/ 2/79
4/ 3/79
4/ 4/79
4/ 5/79
4/ 6/79
* 4/ 7/79
4/ 8/79
4/ 9/79
4/10/79
4/11/79
4/12/79
4/13/79
* 4/14/79
4/15/79
4/16/79
4/17/79
4/18/79
* 4/19/79
LOAD
>*«*<
15.2
16.0
15.4
IS. 3
18.1
16.5
16.7
16.6
16.5
16.5
16.4
16.3
|6.4
16.6
16.6
11.2
12.9
l3'*
t»I»
16.0
16.3
16.8
17.2
20.6
20.7
17.8
13.9
17.3
t*.2
18.5
18.9
l*.S
17.0
16.8
16.7
02
VOLX
><
.7
.0
.5
.1
.1
7.7
7.6
7.5
7.6
7.6
7.9
8.5
8.0
7.8
7.9
10.5
10.5
10.1
10.8
*«2
8.1
8.3
7.3
7.1
6.8
6.7
6.3
6.8
10.1
8.1
8.8
6.7
7.2
7.4
7.7
7.9
9.2
C02
vocx
MEA3
>*<<
8.7
lo|9
11.9
10.5
11.4
12.6
11.4
10. 1
10.1
9.8
9.6
9.9
10.4
10.4
8.4
7.9
8.3
!*
9.9
10.1
10.1
10.1
10.4
10.5
10.6
10.5
8.2
9.6
9,3
10.1
10.0
10.1
10.0
9.9
>***<
MO
MEA3
(I
181.
183.
163.
157.
1*6.
162.
152.
132.
121.
132!
135.
132.
111.
11*.
0.
125.
133.
121.
127.
123*
126.
123.
153.
163.
187,
181.
132.
165.
158.
181.
166.
173.
161.
137,
121.
i
HO
PPMV
jXOf
>.*«*<
266.
274.
236.
220.
273.
219.
204.
175.
163.
160.
182.
1*5.
183.
151.
164.
0.
216.
220.
214.
1*6.
163.
176.
165.
160.
1*4.
205.
22*.
230.
218.
231.
234.
229.
218.
230.
218.
1*0.
184.
NO
NG/J
>«*<
147.
151.
130.
121.
151.
121.
112.
*7.
*0.
88.
too.
107.
101.
83.
*0.
0.
121*.
tie.
toa.
*o.
*7.
ea!
107.
113.
126.
127.
120.
127.
12*.
126.
120.
127.
120.
105.
101.
>**<
*
»
»,
«
*
«
*«
.«
c<
*
«,
..
*
*
«
«
*
a
«
Figure 3-4. Summary of 24-hour Average Data
36
KVB 6017-1216
-------
TABLE 3-8. NO EMISSIONS FREQUENCY DATA
SITE 2
Cell
83- 89.80
89.81- 96.60
96.61-103.40
103.41-110.20
110.21-117.00
117.01-123.80
123.81-130.60
130.61-137.40
137.41-144.20
144.21-151.00
Frequency
3
4
5
4
2
8
7
0
0
3
Cum.
Frequency
3
7
12
16
18
26
33
33
33
36
Plot
Percent
8.1
18.9
32.4
43.2
48.7
70.3
89.2
89.2
89.2
97.3
g (geometric dispersion) = 1.17
x (geometric median) = 110 ng/J
37
KVB 6017-1216
-------
U)
00
I
M
K)
01
150
140
120
cr
c
§
100
80
Site 2
Residual Oil
Capacity: 26.4 MW (Thermal)
0.01
I
I
x = 110 ng/J
10 50
percent less than
90
99
Figure 3-5. Normal-probability plot of 24-hour averages of NO emissions from a
residual oil fired boiler.
-------
distributed. Further analysis indicated that the data were log-normally
distributed. The data and log sheets were reviewed to separate the emissions
data into two groups corresponding to low NO firing conditions (one burner
X
out of service) and normal operating conditions. Table 3-9 presents the
frequency distribution of the boiler NO emissions while operating in the
SCA condition. Table 3-10 shows the frequency distribution with the boiler
operating in the normal mode. A log-normal plot of NO emissions is presented
as Figure 3-6 for the residual oil fired boiler at Site 2 under low N0x
operating conditions. The graph shown in Figure 3-7 illustrates the
performance of the residual oil fired boiler with all burners in service
based on the 24-hour averages. The mean NO emission rate is 100 ng/J with
a geometric dispersion of 1.12 while operating with SCA. The NO emission
rate from the boiler while operating in the normal mode (all burners firing)
was determined to be 130 ng/J with a geometric dispersion of 1.11.
A daily plot of the NO emissions is shown in Figure 3-8. This plot
shows high levels in NO emissions when all burners are firing a large fraction
of the day or when the excess O level is high. Figure 3-9 presents a daily
plot of excess O_. High values of excess 0_ correspond to high NO emission
rates, even if a burner is out of service. The high excess 02 levels
generally correspond to week-ends where KVB personnel were not on hand
to advise the operational personnel on the excess air condition.
Staged combustion as a NO control technique resulted in a 23 percent
X
reduction from the baseline value of 130 ng/J. Under low NO operation (SCA),
X
99 percent of the values were less than 130 ng/J. Under normal operating
conditions, 99 percent of the values were less than 170 ng/J.
39 KVB 6017-1216
-------
TABLE 3-9. FREQUENCY DATA FOR SITE 2 BOILER WITH SCA
Burner
Status
2,3
Cell
81- 85
86- 90
91- 95
96-100
101-105
106-110
111-115
116-120
121-125
126-130
x = 100 ng/J
g.d. = 1.12
Frequency
1
5
1
3
3
3
2
2
2
2
n = 24
Cumulative
Frequency
1
6
7
10
13
16
18
20
22
24
Percent
Plot
4
24
23
40
52
64
72
80
88
96
TABLE 3-10. FREQUENCY DATA FOR SITE 2 BOILER UNDER NORMAL FIRING CONDITIONS
Burner
Status
1,2,3
Cell
118-120
121-213
125-126
129-129
130-132
133-135
136-138
139-141
142-144
145-147
148-150
151-153
154-156
x = 130 ng/J
g.d. = 1.11
Frequency
2
2
2
2
2
0
0
0
0
1
0
0
1
Cumulative
Frequency
2
4
6
8
10
10
10
10
10
11
11
11
12
Percent
Plot
15
31
46
62
77
77
77
77
77
85
85
85
92
40
KVB 6017-1216
-------
I
M
M
1000
900
800
700
600
500
400
300
200
100
90
80
70
60
50
40
30
20
10
TinIIIIIr
Site 2
Residual Oil
Capacity: 26.4 MW (Thermal)
I I I
1 I
I I
T 1
x = 100 ng/J
9 = 1.12
_LJ I I J I
I I I III L
I I
I I
I I
.01.05.1.2 .5 1
10 20 30 40 50 60 70 80
PERCENT LESS THAN
90 95 98 99 99.8 99.9 99.99
Figure 3-6. Log-Probability plot of 24-hour averages of NO Emissions from a Residual Oil
Fired Boiler under low NO conditions.
X
-------
*».
10
en
o
-j
I
1000
900
800
700
600
500
400
300
200
g1 100
O 90
55 80
70
60
50
40
30
20
10
_l I I I IT
1 I
i r
Site 2 - Residual Oil Fired Boiler
Capacity: 26.4 MW
All Burners Firing
x = 130 ng/J
g = 1.11
»i I I I I I I I I I 1 1 L_L
.01.05.1 .2 .5 1 2
5 10 20 30. 40 50 60 70 80
percent less than
90 95 98 99 99.8 99.9 99.99
-------
200
180
160
140
120
n
en
o
z
100
80
60
40
20
Site 2 - Residual Oil Fired Boiler
24-Hour NO Averages vs. Days
(60)
(40)
(15)
High O,
x = 113 ng/J
s = 17.9
^ All burners firing
O BOOS
( ) Percent time BOOS
Cl
i
CO
en
P-
I
n
-------
12
11
10
u
c
O
u
M
O
Site 2 - Residual Oil Fired Boiler
24 Hour Average O vs. Days
I
*r
r-
co
r-t
I
ro
co
CN
I
--N
I
i
a1
i
CN
r-
i
10
15
20
DAYS
25
30
35
Figure 3-9. Daily Plot of Excess O.
44
KVB 6017-1216
-------
Emission factors for the residual oil fired boiler were calculated
using the procedure set forth in 40CFR60, Subpart D. The NO emission factor
(dry basis) was calculated using the following equation:
D-C,F
d d 20.9 - % 02
Where E = Pollutant emission rate, ng/J (Ib/million Btu)
C = NO concentration, ng/scm (Ib/scf)
F = Stoichiometric conversion factor, 2.47 x 10
dscm/J (9,190 dscf/million Btu), for residual oil
0_ = Oxygen concentration, percent by volume, dry
d
The conversion of measured NO values (ppmv) to ng/scm is made by multiplying
by 1.912 x 10 . To convert from ppm to Ib/scf, multiply by 1.19 x 10
NO emissions were measured as NO and the NO emission rates
x x
reported herein are calculated based on the molecular weight of NO .
45 KVB 6017-1216
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SECTION 4.0
REFERENCES
1. Cato, G. A., et al., "Field Testing: Application of Combustion
Modifications to Control Pollutant Emissions from Industrial
Boilers - Phase I," EPA 650/2-74-078a, NTIS No. PB 238 920,
June 1975.
2. 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.
3. 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.
46 KVB 6017-1216
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APPENDIX A
EFFICIENCY MEASUREMENTS
47 KVB 6017-1216
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EFFICIENCY
Unit efficiencies for boilers are calculated and reported according
to the ASME Power Test Codes for Steam Generation Units, PTC 4.1-1965. These
codes present instructions for two acceptable methods of determining thermal
efficiency. One method is the direct measurement of input and output and
requires the accurate measurement of the quantity and high-heating value of
the fuel, heat credits, and the heat absorbed by the working fluids. The
second method involves the direct measurements of heat losses and is re-
ferred to as the heat loss method. This method requires the determination
of losses, heat credits, and ultimate analysis and high-heat value of the
fuel. Some of the major heat losses include losses due to heat in dry flue
gas, losses due to fuel moisture content, losses due to combustible material
in refuse and flue gas, and radiation losses. Heat credits are defined as
those amounts added to the process in forms other than the chemical heat
in the fuel "as fired." These include quantities such as sensible heat in
the fuel, heat in the combustion air, and heat from power conversion in a
pulverizer or fan. The relationships between input, output, credits, and
losses for a steam generator are illustrated in Figure A-l.
KVB's experience has shown the heat-loss efficiency determination
method to be the most reliable when working with industrial boilers. Ac-
curate fuel input measurements are rarely possible on industrial boilers due
to the lack of adequate instrumentation, thus making the input-output method
undesirable. The accuracy of the efficiency based on the heat loss method
is determined primarily by the accuracy of the flue gas temperature measure-
ment immediately following the last heat removal station, the stack gas
excess 0 level, the fuel analysis,, the ambient temperature, and proper
identification of the combustion device external surfaces (for radiation
losses). Determination of the radiation and other associated losses may
apoear to be a rather imposing calculation, but in practice it can be ac-
comclished by utilizing standard efficiency calculation procedures. Inac-
curacies in determining efficiency occasionally occur even with the heat
48 KVB 6017-1216
-------
HEAT IN FUEL (H() (CHEMICAL)
INPUT
1 IN r u I
ENVELOPE
f BOUNDARY
|
|
1
LOSSES (L)
===:
PA HEAT IN ENTERING AIR
BZ HEAT IN ATOMIZING STEAM
Bl SENSIBLE HEAT IN FUEL
BX PULVERIZER OR CRUSHER POWER
Bx BOILER CIRCULATING PUMP POWER
a V t- CREDITS (BJ
BX PRIMARY AIR FAN POWER C
BX REC1RCULATING GAS FAN POWER
B»A MEAT SUPPLIED BY MOISTURE
IN ENTERING AIR
B. HEAT IN COOLING WATER
f V ; HEAT IN OESUPERHEATER WATFR AND CIPCUI ATIMIJ PUMP INJECTION WATER
»- HEAT IN BLOWOOWN AHP r!»CUl ATING PUMP LEAK-OFF WATER
LUC UNBURNED CARBON IN REFUSE
L0 HE AT IN DRY GAS
L»l MOISTURE IN FUEL
LM MOISTURE FROM BURNING HYDROGEN
L-A MOISTURE IN AIR
LZ HEAT IN ATOMIZING STEAM
LCO CARBON MONOXIDE
LUH UNBURNED HYDROGEN
LUMC UNBURNED HYDROCARBONS
L3 RADIATION AND CONVECTION
L. RADIATION TO ASH PIT. SENSIBLE HEAT IN
' SLAG i LATENT HE AT OF FUSION OF SLAG
Lw 5FN5IBLE HEAT IN FLUE DUST
I-, MEAT IN PULVERIZER REJECTS
L . HEAT IN COOLING WATER
'-. SOOT BLOWING
OUTPUT = INPUT - LOSSES
OEF.N.T.ON: EFF.C.ENCY (PERCENT) = ^ (%) = ffijgai , 100
HEAT BALANCE: H, +8 = OUTPUT + L OR ^ (%) - [' ' flT^
Figure A-l. Heat balance of steam generator.
100
" '°°
49
KVB 6017-1216
-------
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.
50 KVB 6017-121t:.
-------
SUMMARY SHEET
FOR
TABLE A-l
A.SME TEST FORM
ABBREVIATED EFFICIENCY
TEST
PTC 4.1-a(196.:
OWNER OF PLANT
TEST CONDUCTED BY
30ILER MAKE & TYPE
TEST NO.
LOCATION
OBJECTIVE OF TEST
80ILER NO.
RATED CAPACITY
DATE
DURATION
STOKER TYPE & SIZE
PULVERIZER, TYPE & SIZE
FUEL UJED MINE
COUNTY
BURNER, TYPE 4
SIZE
STATE SIZE AS FIRED
PRESSURES & TEMPERATURES
FUEL DATA
1
2
3
4
5
6
7
S
9
10
11
12
13
U
15
16
17
18
!9
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
26
STEAM PRESSURE IN BOILER DRUM
STEAM PRESSURE AT S. H. OUTLET
STEAM PRESSURE AT R. M. 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.) (BOILER)
STEAM QUALlTYr. MOISTURE OR P. P.M.
AIR TEMP. AROUND BOILER (AMBIENT)
TEMP AIR FOR COMBUSTION
IThit it Reference Temperature) ?
TEMPERATURE OF FUEL
GAS TEMP. LEAVING (Boiler) (Eton.) (Air Htr.)
GAS TEMP. ENTERING AH (if condition. t« be
corrected to audtontee)
UNIT QUANTITIES
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 17)
HEAT ABS/LB R.H. STEAM (ITEM 19 -ITEM IB)
DRY REFUSE (ASH PIT + FLY ASH) PER LB
AS FIRED FUEL
8ft, PER LB IN REFUSE (WEIGHTED AVERAGE)
CARBON BURNED PER LB AS FIRED FUEL
DRY GAS PER LB AS FIRED FUEL BURNED
psia
psio
osia
pjio
F
F
F
F
F
F
F
F
F
Btu/lb
Btu/lb
3tu/lb
Btu/lb
Btu/lb
Btu-lb
Btu/lb
Ib/lb
Stu/lb
Ib/lb
Ib/tb
HOURLY QUANTITIES
ACTUAL WATER EVAPORATED
REHEAT STEAM FLOW
RATE OF FUEL FIRING (AS FIRED «t)
TOTAL HFAT INPUT (Item 28 X Item 41)
1000
HEAT OUTPUT IN BLOw-BOWN WATER
Hf AT Otem 26» l»em 20)»(l tern 27»l tern 21)»ltem 30
OUTPUT iocs
Ib/hr
Ib/hr
Ib/hr
kS/hr
kB/hr
kB/hr
FLUE GAS ANAL. (BOILER) (ECON) (AIR HTR) OUTLET
CO,
0,
CO
N, (BY DIFFERENCE)
EXCESS AIR
V. VOL
% VOL
% VOL
% VOL
-
COAL AS FIRED
PROX. ANALYSIS
37
38
39
40
MOISTURE
VOL MATTER
FIXED CARBON
ASH
TOTAL
41
42
Btu per Ib AS FIRED
ASH SOFT TEMP.'
ASTM METHOD
% wt
COAL OR OIL AS FIRED
ULTIMATE ANALYSIS
43
44
45
46
47
40
37
CARBON
HYDROGEN
OXYGEN
NITROGEN
SULPHUR
ASH
MOISTURE
TOTAL ,
COAL PULVERIZATION
48
49
50
64
GSINDABILITY
INDEX-
FINENESS %THRU
50 M-
FINENESS % THRU
200 M*
INPUT.OUTPUT
EFFICIENCY OF UNIT ;
51
52
53
44
4)
OIL
FLASH POINT f
Sp. Grovity Deg. API*
VISCOSITY AT SSL"
BURNER SSF
TOTAL HYDROGEN
% wf
Btu per Ib
GAS
54
55
56
57
53
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. «r
5 VOL
DENSITY 68 F
ATM. PRESS.
Btu PER CU FT
Btu PER L3
ITEM 31 * 100
ITEM 29
Btu/lb
HEAT LOSS EFFICIENCY A. F. FUEL
65
66
67
AS
69
70
77
72
HEAT LOSS DUE TO DRY GAS
HEAT LOSS DUE TO MOISTURE IN FUEL
HEAT LOSS DUE TO H,0 FROM COMB. OF H:
HEAT LOSS DUE TO COMBUST. IN REFUSE
HEAT LOSS DUE TO RADIATION
UNMEASURED LOSSES
TOTAL
EFFICIENCY = (100 - Item 71)
% of A.
FUEL
* Not Required for Efficiency Testing
T For Point of Measurement See Por. 7.2.8.1-PTC 4.I-J964
51
KVB 6017-1216
-------
CALCULATION SHEET
TABLE A-2
ASME TEST FORM
FOR ABBREVIATED EFFICIENCY TEST
PTC 4.1-b (1964)
Revised September JJ
OWNER OF PLANT
30
24
25
36
65
66
67
68
69
70
71
72
HEAT OUTPUT IN BOILER SLOW-DOWN
If impractical to weigh refuse, this
item can be estimated as follows
OTJY REFUSE PER LB OF AS FIRED FUE
ITEM 43
CARBON BURNED
FUEL 10°
TEST NO. BOILER NO. DATE
" ITEM 15 ITEM 17" kB/hr
WATER SLB OF WATER BLQ*-DQ*N PER HR x ....
1000
% ASH IN AS FIRED COAL HOTE. |(f f
100 - % COMB. IN REFUSE SAMPLE p,T REFUSE
r- .IN COMBUST
ITEM 22 ITEM 23 SHOULO BE
x SEPARATEL
[ 14.500 J COMPUTAT,
DRY GAS PER LB 11 CO, + 80a + 7(N, + CO)
BURNED 3(CO> + C0) / \ p
ITEM 32 ITEM 33 { ITEM 35 ITEM 34 j ITEM 24
11 x + 8 x * 7\ * /x
3 x
« co
EXCESS °>
.2682N. - (o, - C0_
2
LUE DUST & ASH
DIFFER MATERIALLY
IBLE CONTENT, THEY
ESTIMATED
Y. SEE SECTION 7,
ONS.
ITEM 47
/ITEM 32 ITEM 34 \ {_ 267 J
( + )
ITEM 33
- 100 * * -
' .2682 (ITEM 35) - (ITEM 33 - ITEM 34 )
2
HEAT LOSS EFFICIENCY
HEAT LOSS DUE LB DRY GAS
TO DRY CAS » PER LB AS xC
FIRED FUEL p
xr,..-w, = ITEM25xo.24(ITEM'3)-(1TEMn),
Unit
MOKTUR"^'^ = AS RRED^UEL X ^ (ENTHALPY OF VAPOR AT ' PSIA * T GAS LVC)
-(ENTHALPY OF LIQUID AT T AIR)] = UliUL x [(ENTHALPY OF VAPOR
100
AT 1 PSIA & T ITEM 13) -(ENTHALPY OF LIQUID AT T ITEM 11)] »
HEAT LOSS DUE TO H,0 FROM COMB. 0
. 0 » ITEM *f * [ENTHALPY Of tfj
'00 T ITEM 11)] = . . .
F H, = 9H, X [(ENTHALPY OF VAPOR AT 1 PSIA & T CAS
LVC) - (ENTHALPY OF LIQUID AT T AIR)]
kPOR AT 1 PSIA & T ITEM 13) - (ENTHALPY OF LIQUIO AT
HEAT LOSS DUE TO ITEM 22 ITEM 23
COMBUSTIBLE IN REFUSE * x *
HEA'T LOSS DUE TO TOTAL BTU RADIATION LOSS PER HR
RADIATION- LB AS FIRED
FUEL - ITEM 21
UNMEASURED LOSSES
TOTAL
EFFICIENCY * (100 - ITEM 71)
Btu/lb LOSS x
AS FIRED HHV
FUEL 100 =
lixioc,
41
^i x 100 =
41
-i_xlOO =
41
a x,oo,
41
69
K 100 -
41
70 x 100 -.
41
t Fot
If lot... OT
*tian af accass air saa Appandi* 9.2 PTC 4.1*1964
nat naaHirad. u«o ABMA Standard Radiation Lais Chart, Fia. 8, PTC 4.1-1964
lo*M* liitad in PTC 4.1 but nat tabulated abav* may by prooidad far by a«sianin« .
valaa fer Itaai 70.
52
utually
KVB 6017-1216
-------
FIGURE A-2
HP-67 KEYED CALCULATION SHEW
ASME ABBREVIATED EFFICIENCY CALCULATION - HEAT LOSS METHOD
Test No.
Date
Location
Unit No.
Fuel
(Turn Calculator Off «nd Then On. Load Program Card.)
A. FROM FUEL ANALYSIS:
Wt. % in as-fired fuel: C
\, Moisture
\. H
».- S
Al: (S7O 0)
High heating value of fuel as-fired
B. FROM FLUE GAS ANALYSIS:
Volume % in flue gas of: O
Bl:(STO 5)
A5:(STO 4)
*, CO,
A2:(STO 1) A3:(STO 2) A4 : (3TO 3)
Btu/lb
\. CO
B2:(STO 6) B3:(STO 7)
C. FROM REFUSE (FLY ASH AND ASH PIT) ANALYSIS:
Cl. Fraction of dry refuse in fuel
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)
0. MEASURED TEMPERATURES
01. Gas temp, leaving boiler, econ. or air heater
D2. Comb, air temp.
E. FROM STEAM TABLES:
El. Enthalpy: HjOtg) at tenp. Dl t 1 psia
E2. Enthalpy: H O{1) at conb. air temp.
(STO A)
(STO B)
F
Btu/lli
(STO C)
(STO D)
Btu/lb
-. FROM. ABJ1A STANDARD RADIATION LOSS CHART (UNLESS MEASURED) :
Fl. Heat loss due to radiation
(STO E)
C. FROM tr.IIT SPECIFICATIONS (if available, otherwise enter 0):
% of gross heat input
Gl. Unmeasured losses
(f P ^ S) (STO 0) (f P I S)
% of gross heat input
1. Excess Air
100 (2B1 - B3)
0>53M<100 - Bl - B2) - (2B1 - B3)
2. (Optional) Pounds dry gas per pound of fuel -
(A)
3.
4.
5.
6.
7.
8.
Bl « 4B2 + 700
3
-------
APPENDIX B
DATA RECORDING FORMATS
54 KVB 6017-1216
-------
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 (C02>, carbon
monoxide (CO), and oxygen (O.,) are measured and recorded. The concentration
of these species are measured and displayed continuously by analyzers and
strip chart recorders mounted in a console. The strip chart recordings are
retained for future reference. 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
3_1 Thirty-Day Field Test Data Sheets Record control room data
B-2 Gaseous Emissions Data Record Gaseous Emissions
Analyzer data
B_3 Nozzle Size, Qm and AH Calculations Calculate nozzle size,
flow rate, and AH for
Method 5 Test
B-4 Response Time for Continuous Continuous monitor certi-
Instruments fication
3.5 zero and Calibration Drift (24 hr) Continuous monitor certi-
fication
3-6 Zero and Calibration Drift (2 hr) Continuous monitor certi-
fication
B-7 Accuracy Determination (NOx) Continuous monitor certi-
fication
B-8 Calibration Error Determination Continuous monitor certi-
fication
55 KV3 6017-1216
-------
Figure No. Title
B-9 Analysis of Calibration Gas Mixture
B-10 Particulate Calculation Sheet
B-ll Stack Data
B-12 Particulate Emission Caculations
B-13 Velocity Traverse
B-14 Liquid or Solid Fuel Calculation
Purpose
Continuous monitor certi-
fication
Calculate weight of solid
particulate catch
Record volumes, tempera-
tures , pressures of Method
5 control unit.
Calculate particulate em-
mis ion factors
Record temperature and
velocity profile of stack
Calculate stoichiometric
properties of fuel
56
KVB 6017-1216
-------
Figure B-l.
KVB, Inc.
THIRTY DAY FIELD TEST DATA SHEET
Site
Fuel
Test No.
Date
Time
Load
Test Description
Windbox, in. HJD
Furnace, in. H^O
2
Overfire air, in. H_O
Boiler exit, in. H,0
Economizer exit, in. HJD
ID fan inlet, in. H^O
Steam flow, krnah
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 .
57
(continued)
Data Sheet 6017-26
12/12/78
KVB 6017-1216
-------
Figure B-l. (Continued)
THIRTY DAY FIELD TEST DATA SHEET
Page 2
Test No.
Smoke Indicator Chart
Rotary speed
Spill plate setting
Grate speed
Overfire 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:
58
Data Sheet 6017-26
12/12/78
KVB 6017-1216
-------
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. Oxvgen (%)
8. NOX (hot)
read/3% O_ (pern)
9. NO (hot)
read/3% 0., (ppm)
10. NO (hot)
read/3% O_ (ppm)
11. Carbon Dioxide
(%)
12. Carbon Monoxide
(pnm) uncor/cor
13. Opacity
14. Atmos. Temp.
(°F/°C)
15. Dew Point Temp.
(°F/°C)
16. Atnos. Pressure
(in. Hg)
17. Relative
Humidity (%)
59
Data Sheet
6015-23
9/29/78
KVB 6017-1216
-------
Figure B-3.
HP-67 Keyed Calculation Sheet
NOZZLE SIZE, Q and AH CALCULATIONS
Test No.
Unit Ho.
Crew: Engr.
Date
Fuel
Location
Saaolin? Method
Techs.
DATA
Constants
Pitot 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, %
Key
(STO 1)
(STO 2)
(STO 3)
(STO 4)
NOZZLE SIZE,
THRU B, CLEAR
0.. and % CO
Actual Conditions
Meter Tenperature. TBCF)
Barom. Press., PBar (in. Hg)
Static Press. Diff.. APS (iwg)
Nozzle Teap. . Tn (T)
Stack Vel. Press., Ap (iwg)
Caseous Stack Comoosition
* H20 (%)
% 02 dry (%)
% C02 dry (»)
Key
(STO 5)
(STO 6)
(STO 7)
(STO 8)
(STO 9)
ENTER
ENTER
(A) Ideal Nozzle Size, D inches
METER FLOW RATE AND ORIFICE PRESS. DIFF. CALCULATION
Actual Nozzle Size. * inches
(CJ Actual Meter Flow Rate, Sm(Actual) _ ACFM (on meter)
(RCL 7) Orifice Press. Diff., AH to obtain Q _ iwg
NOTEs To Deternine Qg, and AH for Other Actual Nozzle Size, Key in Dn(Xctualj, Press C for Q , then RCL
For one DH (Actual) with Changing Stack Velocity Pressure (Ap) and Nozzle Temperature (T )
(It is not necessary to restore data in registers 4-8 for these calculations) "
Ap (ENTER) Tn
4*0) - 7M
t*0*>
i !* irtk.tr* a * ma-tor of lur*clan« to ofectia £« (AH * AH 1
"'* k4=*- '"-801
1-1
:: (la. at <«
««0| - it* 0 ' n.
60 KVB 6017-1216
KVB 6015-25 (Rev. 1)
12/13/78
-------
Figure B-4.
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
RESPONSE TIME FOR CONTINUOUS INSTRUMENTS
Date of Test
Span Gas Concentration ppm
Analyzer Span Setting ppm
1 seconds
Upscale 2 seconds
3 seconds
Average upscale response _ seconds
1 seconds
Downscale 2 _ seconds
3 seconds
Average downscale response _ seconds.
System average response time (slower time) = _ seconds.
("average upscale minus average downscalel
|_ slower time J
% deviation from slower ("average upscale minus average downscale
system average response
61 7/1/77
Data Sheet 6017-35
40CFR60/App. B
KVB 6017-1216
-------
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)
j- [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
62 KVB 6017-1216
-------
I
M
M
H
CTl
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 T [Span] x 100 =
+ CI (Span) 1 f [Span! x 100 =
C
H
n>
to
CO
Data Sheet 6017-33
40CFR60/App. B
7/1/77
-------
MONITOR PERFORMANCE TEST DATA SHEET
ACCURACY DETERMINATION (NO )
x
Engineer^
Test
No.
1
2
3
4
5
6
7
8
9
Date
and
Time
Reference Method Samples
NO
X
Sample 1
(ppm)
NO
X
Sample 2
(ppm)
NO
X
Sample 3
(ppm)
NO Sample
Average
(ppm)
Mean reference method
test value (NO )
95% Confidence intervals = + ppm
Accurac
* Expla
. Mean of the differences + 95%
X
(N0x)
confidence interval
"**~" Mean reference method value * *""
lin and report method used to determine integrated averages
Analyzer 1-flour
Average (ppm)*
N0x
Difference
(ppm)
N°x
Mean of
the differences
% (NO )
e
8
CD
o
H
NJ
Data Sheet 6O17-32
40CfRfiO/App. H
-------
Figure B-8.
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
CALIBRATION ERROR DETERMINATION
Calibration Gas Mixture Data
Mid (50%) ppra High (90%) ppm
Calibration Gas Measurement System
Run # Concentration, ppm Reading, ppm Differences, ppm
10
11
12
13
14
15
Mid High
Mean difference
Confidence interval
Mean Difference2 + C.I. .
Calibration error = Average calibration Gas Concentration X 10°
Calibration gas concentration - measurement system reading
Absolute value
Data Sheet 6017-31
40CFR60/App. B
7/1/77
65 KVB 6017-1216
-------
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
66 40CFR60/App. B
7/1/77
KVB 6017-1216
-------
Figure B-10.
Test No.
Box No.
Test Description
PARTICULATE CALCULATION SHEET
Date
Location
Test Crew
Sample Probe Position
Dry Gas Meter Vol. (3
Final
Initial
Total
Beaker No.
Date
Weighed
Tare 1
Wt. 2
3
4
5
6
Avq
Bottle No.
Impinger
Content (Water)
Rinse (ml)
^ate 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
Cnitial
A Vol
Probe
(Water)
Intpinger
1 2
Cyclone
(Acetone)
Water Vc
3
Flask
(Dry)
>1 (ml)
S. Gel 1
Filter
No.
'otal
Blank
No.
Comments:
Data Sheet 6002-3
67
KVB 6017-1216
-------
Figure B-ll.
Date_
Load
Location
KVB. INC.
STACK DATA
Unit No.
Test No,
Engr.
Fuel
Sample Box No.
Kt/hr or MBtu/hr
Meter Box No.
Filter No.
Probe No.
Filter Heater Setting
Probe Heater Setting
Stack Moisture
Ambient Temperature
Nozzle Diameter
Atmospheric Pressure
Weather
OF
in.
in.Hg
I
diam.
I
Stack Gas Pressure, Ps iwg
Abs. Stack Press., AP=P +407= iwga
Stack Gas Sp. Gravity, 5s n.d.
Stack Area, As ft2
_Probe Length
Remarks
Final Meter:
Initial Meter:
Time
Total
Avg.
Vm
Meter
Volume
Beading
(CF)
Vacuum
Gage
Reading
(iwg)
*P
Pitot
Tube
Pressur
(iwg)
H
Orfice
Pressure
*, Diff
(°F)
Stack
Temp.
(°F)
°F
°F
+ 460
Impinger
Temperature
Out
(OF)
In
(°F)
Filter
Box
Temp.
(°P)
Meter
Temp .
(°F)
68
60-13
11/20/75
KVB 6017-1216
-------
Figure B-12.
3. Date
HP-67 KEYED CALCULATION SHEET*
PARTICULATE EMISSION CALCULATIONS
Location
Engr.
nit NO.
pj.tot Factor, Fs
Fuel
.83
Tot- Liquid Collected, V
Sampling Train and Method
Barometric Pressure, P
bar (STQ Q)
ml Total Particulate, M
in. Hg
-m gm
Velocity Head, AP_
1 (STO 1)
_iwg Stack Temp., Ts
TSTO 4)
n (STO 2)
°F Stack Area, As
ft
(STO 5)
Sasple Volume, Vm
Orifice Press.
Sanple Time, 9
(STO 6)
Orifice Press. Dif f. , H_
_ft Stack Press., Psg
iwg Excess 0 , XO % %
2 2 (STO 8)
(bTO
min Nozzle Dia., Dn
(STO 7)
_iwg,(Flue Gas Density/Air Density)@ Ts, Gs
n.d.
(STO B)
(STO C)
(STO A)
in. Meter Temp., T °F
(STO D)
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 oar
2. Water Vapor
Vw
std
0.0474 V
Ic
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C = 0.0154 Mn/Vm
.-6
'std
b. C = 2.205 x 10 w Mn/Vm
c. C = Eq. 4b x 16.018 x 10
'std
3
5. Abs. Stack Press. Ps = P. x 13.6 + Psg
oar
6. Stack Gas Speed Vs = 174 Fs /APTs ~ x
7. Stack Gas Flow a. Qsw
Rate @ 70°F
530
Eq. 6 x As x TT X
1.00
Gs
Ps
8. Material Flow
9. XD factor
10. Emission
U. % Isokinetic
Ts " 407
b. Qsd = Eq. 7a x (1. - Eq. 3)
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 . . + Vv
std
9 x Vs x Ps x Dn
SCF
SCF
N.D.
grains/DSCF
Ib/DSCF
grams /DSCM
in. w abs.
ft/min
WSCF/min
DSCF/min
N.D.
Ib/MMBtu
ng/ joule
*If calculating by hand:
1) Convert Ts and Tm to °R
2) Multiply EQ 1 by 530/Tm(°R) if «eter not temperature compensated.
3)
2.684 x 10'5 x F
69
Data Sheet 6002-4
Revised 9/27/78
KVB 6017-1216
-------
Figure B-13.
* nject:
bdte:
KVB, Inc.
VELOCITY TRAVERSE
Test Description:
Location:
Unit:
Test:
Fuel:
Stack Cross Section
Personnel :
Barometric Press, (in.
Absolute Static Press, in Stack (in. Hg):,
Pitot Tube Coefficient:
CP
ps**"
[vs".
1/2
j i
4-
Time
Tr avers
Port
e Point
Depth
Velocity
Head
(in. H20)
AP
Gas Temp.
(°F)
Gas Temp.
(°R)
TS
Molecular
Wt.
MS
Velocity
(ft/sec)
VS
02
Cone.
(% Dry) ;
!
1
. 1
*
^^
70
Data Sheet KVB 6002-13 K7B 6017-11
-------
Figure B-14.
KVB
Test No._
Fuel
Date
Fuel Sample [Jo.
Location
Unit No.
Fuel Sample Point
LIQUID OB SOLID FUEL, CALCULATIONS
(f)(CL REG), (f) (P
-------
APPENDIX C
CONTINUOUS MONITOR CERTIFICATION DATA SHEETS
72 KVB 6017-1216
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
CALIBRATION ERROR DETERMINATION
MAP O ft 1Q7Q
i*..-v* *-: ^ IO/3
Calibration Gas Mixture Data
Mid (50%) IZO ppm High (90%) Z ?*' ppm
r\* L^y // /IS* t ' / *?* '" *"^ "" / (^^ £ w^ f * ^ £" * &
I i
Calibration Gas Measurement System
Run f Concentration, ppm Reading, ppm
Differences, ppm
1 & O £> <=>
2/V / 2 C^ / /
4 yU 1 ? V "7 3 f o"
5 / / /ZC^ / / ^ X
6 ^y 2 ^** 2.-^.J> 4
~> s-r /T.s> / T- ^
8 0 ^ . f
9 M |^.(-
100 t/ % % 3,
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
CALIBRATION ERROR DETERMINATION
MAR 2 0 1979
Calibration Gas Mixture Data
s
Mid (50%) / 0X99*,-
High (90%) /"?.
Run f
Calibration Gas
Concentration/ ppm
Measurement System
Reading, pp» «>£
Differences,
a
4 A'
//
it.
1 7.
B O
10
/7.V
12 / /
/g>. a?
13
Mean difference
Confidence interval
Calibration error «
Mean Difference + C.I.
Mid
.£»£>
High
Calibration Gas Concentration
,^ <-s.
x 100 /«3 %
*"» ' ' -M* -
Calibration gas concentration - measurement system reading
Absolute value
~"Data Sheet 6017-31
40CFR60/App. B
7/1/77
74 KVB 6017-1216
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
CALIBRATION ERROR DETERMINATION
0 1979
Calibration Gas Mixture Data
Mid (50%) *y&D ppm High (90%)
rt* 4
Run #
Calibration Gas
Concentration, ppm
Measurement System
Reading, ppro
Differences, ppm
/'
O
o
~iC,>
o
2_o
V7J"
10
11
12
13
14
15
Mean difference
Confidence interval
Mean Difference + C.I.
Calibration error - Average calibration Gas Concentration
1Calibration gas concentration - measurement system reading
Absolute value
75
Data Sheet 6017-31
40CFR60/App. B
7/1/7-7
KVB 6017-1216
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
CALIBRATION ERROR DETERMINATION MAR 2 0 1979
Calibration Gas Mixture Data
Mid (50%) &£> .jpa High (90%) f- £
' .' 7,1 - -5
^>-' >
Calibration Gas Measurement System . yt
Run # Concentration, -ppar as Reading, -PB«- */ Differences, ppnr
1 7
Calibration error Mean Difference2 * C.I. V"/ % / V %
Average Calibration Gas Concentration * 1O° V
Calibration gas concentration - measurement system reading
Absolute value
Data Sheet 6017-31
40CFR60/App. B
7/1/77
76 KVB 6017-1216
-------
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (2 HOUR)
Engineer
Data Zero Span Calibration
Set Time Zero Drift Span Drift Drift
No. Begin End Date Reading (AZero) Reading (ASpan) (Span-Zero)
1 cJT/Vyi.' T~ / OO C> 3 -if' "7 f O - ' 2. 3 V ~~
2 I20n\
3 i 4-r>(.> "*
4 / bw '
5 n^o l
R ,^ ^
- 2. 2. 1 H - 1 V- /
- 3 - / 25o - 3 - 1
- 6 - 3 7-"to - |o -7
- f z 2/7 - ( -y- /
- f,y -/..r ^/? - i.c
?-_ A. ^p 1 j* ^1 ^ v^x "O ^> * 1
*5^7~~£i r F* / f* ^'*^ *^ ** / r^ "" / / ( 1 *" * t ^x ^/ ^^ "^*^
8 /Zr>* '
9 y ^/^.j
10 /^O
11 /«f,')r5
0 0 7-"? «^ <^ D
/ / i'^4 o - /
3 -2. "2 ^ r) -V - (^
\ S 7 Z'-'iT. 4 z. o
1 9 - ^-v *^
** i^7>y ** v y xij^ XA 2* j M "^ ^i cJ -^* "*") 7. cj i. L. f * - .
**^Xv^» -C r / IsC/ (J ^} f f * f ^~ ,/- ^ "
13
0 0 a^f \r 4 J«-{
14 /<^»r-> s ^.r ^..iT ^^3 -f s +\,<
15 /<^^^ NT 4. r / 6> a^T - '/ - LT
Zero Drift - [Mean Zero Drift*
Calibration Drift « [Mean Span
* Absolute Value.
/. ^.
Drift* 2-.T3 + CI (Span) /' '- ] * [Span] x 100= /.&f%.
01
o
I
to
H
01
\
3
z.
Data Sheet 6017-33
40CFR60/App. B
7/1/77
-------
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (2 HOUR)
Engineer_
Data
Set Time
Ho. Begin End Date
Zero
Reading
Zero
Drift
(Azero)
Span
Reading
Span
Drift
(Aspan)
Calibration
Drift
(Span-Zero)
1 J>W /*** 3'/S-74 /% - ' /?^
2 /gee j ./j-. 7q
3 ft00 J -XT-/*'
* ^fe» 3-/J~- 7*9
5 /#<2%? 3-/jT~ 7$
6 £000 3'Af'?0i
1 J/art #00 3-/6'7& _I
1* JJast 3-19- 79
14 /40& 3 ~t*?' 7 3-rt'79
/7 IO0O 3 -
-------
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (2 HOUR)
Engineer
-~J
IO
ffl
o
H
H
M
H
Data
Set Time Zero
No. Begin End Date Reading
Zero Span Calibration
Drift Span Drift Drift
(AZero) Reading (Aspan) /Span-Zero)
I Start /00o 3'&-74 0 - ?**
2 see* v
3 /*** :..
4 /£&& &
5 /S*0 3'fe'73 ^
_8 ,joa,
9 /*
10 /^te» v
11 /0tf7 -
13 /^^
/&&&
15 /60o
-tf -4 fcf /S"
- - Data Sheet 6017
£, &*?<£ ~& 40CFR60/App. B
CO
7/1/77
-------
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (2 HOUR)
Engineer
D*^a Zero Span Calibration
Set Time Zero Drift Span Drift Drift
No> Be*in End Dat« Reading (AZero) Reading (ASpan) (Span-Zero)
i sr*»r /e&c* j/,s- ^ A _ '? 21
2 12.00
4 tLe>o
5 /*<*o ?//(* f-Z.7
8 f7.ro
9 /«00
10 /6 <>o
11 1 Sou
?? 7 0
£>
15 /^^)0 '
<727 ^
*;. ^7 ^>
' ^. 2-7 O
Zero Drift - (Mean Zero Drift* * CI (Zero) ] * (Span] x 100 'xA^/4 .
Calibrt.tion Drift (Mean Span Drift* ,03*? + CI (Span) , OT/ 1 * (Span] x 100 = r>. 9 ? /*T
Absolute Value.
/' '
00
CO
to
H
^.27
- Z. i
Data Sheet 6017-33
40CFR60/App. B
7/1/77
-------
KVB
Engineer_
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (24-HOUR)
'^f
Date Zero Span Calibration
and Zero Drift Reading Drift
Time Reading (AZero) (After Zero Adjustment) (ASpan)
3
i/'t. ,'»30 £ J? C 34 2-_
ivcc. -y - 5" LA
Z-
Zero Drift » [Mean Zero Drift* ^ 1 + C.I. (Zero) / . ^ §_ ]
* [Instrument Span] x 100 = /. ^^ .
Calibration Drift - [Mean Span Drift* J, £ 6- + C.I. (Span) ,gS,
T [Instrument Span] x 100 = /i <0 ^ .
"*Ab3e.lute Value
Data Sheet 6017-34
40CFR60/APP- B
7/1/77
81 KVB 6017-1216
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (24-HOUR)
Date Zero s?an
and Zero Drift Reading
Time Reading (AZero) (After Zero Adjustment)
Calibration
Drift
(ASpan)
/ "9 £) &j ^^
i? T /Af *9J9 t j* ^J *"' ' * vf f^^
3 £$'74 1*00 O & /?'& ,
0
2 & rdt - / ~ 1 /£ P '* fy
t-n-M , e* 6 o M* &
s-ff'Jt) /*00 & O fftJ -J
3~/6i' ?*? i&0ff & Q 'tf'S y
, , . X5 /) /?.#
3 -(30 jef I00e? O U ' & _ _ ._ .
C?
J'//-7*9 /e*6 O O f7*3 &
Zero Drift * [Mean Zero Drift* .Oofr * C.I. (Zero) _?iS ]
T [Instrument Span] x 100 « -7^ P.. -£»""-'
Calibration Drift - [Mean Span Drift* , i<~7 + C.I. (Span) _,
T [Instrument Span] x 100 » ,/«,70__." "^^^f.
Absolute Value
_, X.
,/f^ 3
?~~
82
Data Sheet 6017-34
40CFR60/APP- B
7/1/77
KVB 6017-1216
-------
KVB
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (24-HOUR)
Engineer
Date Zero Span Calibration
and Zero Drift Reading Drift
Time Reading (AZero) (After Zero Adjustment) (ASpan)
/W-7* **, 0-900 -
3 -'£?*! " O O 90-iT 1 <£~
j./f jtf » g 0 ^00 &
3n-7* '
3 -ig 7<9 "
4, y^ ^7 /7
^ ^ 092 -8
j /
-------
KVB
MONITOR PERFORMANCE TEST DATA SHEET
ZERO AND CALIBRATION DRIFT (24-HOUR)
Engineer
Date
and
Time
Zero
Reading
Zero
Drift
(AZero)
Span Calibration
Reading Drift
(After Zero Adjustment) (ASpan)
9.2?
-.0-L
<7 6 o
- ,'i 7
- .07
o
/o 00
f.c?
Zero Drift = [Mean Zero Drift* + C.I. (Zero)
T [Instrument Span] x 100 - ^^^ .
Calibration Drift [Mean Span Drift* _,/// + C.I. (Span)
T [Instrument Span] x 100 » 3, *4 7 *
Absolute Value
34
Data Sheet 6017-34
40CFR60/App. B
7/1/77
KVB 6C17-1216
-------
KVB
Engineer_
MONITOR PERFORMANCE TEST DATA SHEET
RESPONSE TIME FOR CONTINUOUS INSTRUMENTS
Date of Test
MAR 3 0
Span Gas Concentration
Analyzer Span Setting
ppm
ppm
seconds
Upscale
3 -$~
seconds
seconds
Average upscale response £> >ST seconds
3 seconds
Dovnscale
2 Z"
3
seconds
. O seconds
Average downscale response
System average response time (slower time)
/ seconds.
seconds.
% deviation from slower
system average response
a [
|^
average upscale minus average downscale
slower time
|
J
1QQ%
35
Data Sheet 6017-35
40CFR60/App. B
7/1/77
KVB 6017-1216
-------
KVB
Engineer^
MONITOR PERFORMANCE TEST DATA SHEET
RESPONSE TIME FOR CONTINUOUS INSTRUMENTS
*<%* 4
Date of Test
i^ "
Span Gas Concentration / / cr . ppa-
Analyzer Span Setting
1
7- * seconds
Upscale 2 3- f seconds
3 4* ^ seconds
Average upscale response ^» 2~* seconds
1 3 9 seconds
Downscale 2 ^ «/ seconds
3 ^ Z- seconds
Average downscale response ?g seconds.
System average response time (slower time) ₯ Z. seconds.
% deviation from slower ^[average upscale minus average downscale| ^ 100%
system average response "j_ slower time j
Data Sheet 6017-35
40CFR60/App. B
7/1/77
86 KVB 6017-1216
-------
KVB
Engineer
MONITOR PERFORMANCE TEST DATA SHEET
RESPONSE TIME FOR CONTINUOUS INSTRUMENTS
MAR 2 0 1979
Date of Test
Span Gas Concentration *?&<& ppn
Analyzer Span Setting
-gg&
Upscale
/ J J
1 ff 7 seconds
2 ff J7 seconds
3 9,g seconds
Average upscale response
seconds
seconds
Dovmscale
2
3
seconds
seconds
Average downscale response
System average response time (slower time)
se conds.
seconds.
% deviation from slower
system average response
upscale minus average downscale
slower time
1
J
87
Data Sheet 6017-35
40CFR60/App. B
7/1/77
KVB 6017-1216
-------
KVB
Engineer_
MONITOR PERFORMANCE TEST DATA SHEET
RESPONSE TIME FOR CONTINUOUS INSTRUMENTS
Date of Test MAR 2 0 1979
Span Gas Concentration £ 3
</,
Analyzer Span Setting *?. 3"ZS ppm
seconds
Upscale 2 /g seconds
3 /^,
-------
MONITOR PERFORMANCE TEST DATA SHEET
ACCURACY DETERMINATION (NO )
X
Engineer
Test
NO.
1
2
3
4
5
6
7
8
9
Date
and
Time
3- >?' 71
/0:S3'7 IttOL
/ ppm
Accura
* Expl
, Mean of the differences + 95%
N0x
Sample 3
_. (ppm)
©J"K& 0t
c?0/
a>0<2
/3%*0,
V
8
0
7
1
Data Sheet 6017-32
40CFR60/App.
7/1/77
-------
APPENDIX D
CONTINUOUS MONITOR PERFORMANCE SPECIFICATIONS
90 KVB 6017-1216
-------
App.B
Title -40Protection of Environment
,2 PxxroEitutex
" sraciTi(!l?16MS tiro BHTCinc*Tjott rear no-
CZDUBXS ro« MONTTOU or SO« AND NOi
raoif STATIOKAST sooacxa '
I. Principle and Applicability.
1.1 Principle. The concentration of sulfur
dioxide- or oxldet of nitrogen pollutants la
stack emission* U measured by continu-
ously operating emission measurement sys-
tem. Concurrent with operation of the con-
tinuous monitoring system. the pollutant
concentrations are also measured with refer-
ence methods (Appendix A). An average of
the continuous monitoring tyitem data li
computed for each reference method testing
period and compared to determine the rela-
tive accuracy of the continuous monitoring
system. Other testa of the continuous mon-
itoring system are also performed to deter-
mine calibration error, drift, and response
characteristics of the system.
1.2 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 specification* contain test pro-
cedures. installation requirements, and data
computation procedures for evaluating the
acceptability of the continuous monitoring
systems.
2. Apparatus.
a.l Calibration O*s Mixtures. Mixtures of
known concentrations of pollutant gas in a
diluent gas shall be prepared. The pollutant
gas shall be sulfur dioxide or the appropriate
oxide(i) of nitrogen specified by paragraph
4 and within subparu. For sulfur dioxide gms
mixture*, the diluent gas may be air or nitro-
gen. For nitric oxide (NO) gas mixtures, the
diluent gas ah ill be oxygen-free «30 ppm)
nitrogen, and for nitrogen dioxide (NO,) gas
mixtures the diluent gas shall be air. Concen-
trations of approximately 50 percent aad 90
percent of span are required. The BO percent
gas mixture is used to set aad to cheek the
span and is referred to as the span gas,
22 Zero Oat. A gas certified by toe manu-
facturer to contain less than 1 ppm of the
pollutant gas or ambient 'air may be used.
2.3 Equipment for measurement of the pol-
lutant gas concentration using the reference
method specified la tie applicable standard.
2.4 Data Recorder. Analog chart recorder
or other suitable device with input voltage
range compatible with analyzer system out-
put. The resolution of the recorder's data
output shall be sufficient to allow completion
of the test procedures within this speetfl-
catlon.
3.S Continuous monitoring system for BO,
or NO. pollutants as applicable.
S. Definitions,
' 8 J Continuous Monitoring System. The
total equipment required for the determina-
tion of a pollutant gas concentration la a
source effluent. Continuous monitoring sys-
tem* consist of major subsystems as follows:
S.1.1 Sampling Interface. That portion of
an extractive continuous monitoring system
that performs on* or more of the following
operations: Acquisition, transportation, and
conditioning of a sample of the source efflu-
ent or that portion of an In-aitu continuous
monitoring system that protects the analyzer
from the effluent.
3.1.2 Analyzer. That portion of the con-
tinuous monitoring system which senses the
pollutant gas and generates a signal output
that is a function of the pollutant concen-
tration.
3.1.3 Data Recorder. That portion of the
continuous monitoring system that provides
a permanent record of the output signal in
terms of concentration units.
33 Span. The value of pollutant concen-
tration at which the continuous monitor-
ing system Is set to produce the maximum
data display output. The span shall be set
at the concentration specified in each appli-
cable subpart.
3J Accuracy (Relative). The degree of
correctness with which the continuous
monitoring system yields the value of gas
concentration of a sample relative to the
value given by a defined reference method.
This accuracy U 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
aad the known concentration of the test
gas mixture.
33 Zero Drift. The change la the continu-
ous monitoring system output over a stated
period of time of normal continuous opera-
tion when the pollutant concentration at
the time for the measurements is zero.
.3.8 Calibration Drift. The change in the
continuous monitoring system output over
a stated time period of normal continuous
operations when the pollutant concentra-
tion at the time of the measurements is the
same known upscale value.
3.7 Response Time. The tin* 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 dat» recorder.
3.8 Operational Period. A minimum period
of time over which a measurement system
is expected to operate within certain per-
formance specifications without unsched-
uled maintenance, repair, or adjustment.
3.9 Stratification. A condition Identified
hy a difference in excess of 10 percent be-
tween the average concentration in the duct
or stack and the concentration at any point
more """ 1.0 meter from the duct or stack
wall.
4. Installation Specifications. Pollutant
continuous monitoring systems (SO, aad
MO,) shall be Installed at a sampling loca-
tion where measurements can be made which
are directly representative (4.1). or which
can be corrected so as to be representative
(4.2) of the total emissions from the affected
91
KVB 6017-1216
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Chapter IEnvironmental Prelection Agency
App.B
facility. Conformsnce with thla requirement
snail be accomplished a* follows:
4 I Effluent g«ses may be assumed to be
nonstrstlfled II a sampling location elgbt or
more stack diameters (equivalent diameters)
downstream of any alp In-leakaee Is se-
lected. This assumption and data correction
procedures under paragraph 4.3.1 may not
be applied to sampling locations upstream
of an air prebeater la a steam generating
facility under Bubpart O of this part. For
campling locations where effluent gases are
either demonstrated (4.3) or may be as-
sumed to be nonstratlfled (elgbt diameters).
a point (extractive systems) or path (la-alta
systems) of average concentration may He
monitored.
42 for sampling locations -where effluent
gases cannot be assumed to be nonstratl-
fled (less than eight diameters) or hare been
shown under paragraph 4.3 to be stratified.
results obtained most be consistently repre*
tentative («. a point of average concentra-
tion may shift with toad changes) or the
data generated by sampling at a point (ex-
tractive systems) or across a path (In-sltu
systems) must be corrected (4.3.1 and 433)
so as to be representative of the total emtt-
slons from the affected facility. Conform-
ance with this requirement may be accom-
plished in either of the following ways:
4.2.1 Installation of a diluent continuous
monitoring system (O, or CO, as explicable)
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
ssme type (both extractive or both In-iitu).
the extractive system must use a multipoint
probe.
4.2.J Installation of extractive pollutant
monitoring systems using multipoint sam-
pling probes or In-sltu pollutant monitoring
systems that sample or Hew emissions wnlcn
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 sre consistently repre-
sentative for several typical facility process
operating conditions.
4.3 The owner or operator may perform a
traverse to characterize any stratification of
effluent gases that might exist In a stack or
duct. If no stratlOcatlon is present, sampling
procedures under paragraph 4.1 may be ap-
plied even though the eight diameter criteria
la not met.
4.4 When single point sampling probes for
extractive systems are Installed within the
stack or duct under paragraphs 4.1 and 4.2.1.
the sample may not be extracted at any point
less than 1.0 meter from the stack or duet
wall. Multipoint sampling probes Installed
under paragraph 4.2.2 may be located at any
points necessary to obtain consistently rep-
resentative samples.
6. Continuous Monitoring Bvstem PCT-
The continuous monitoring system shall
meet the performance specifications to Table
3-1 to be considered acceptable under this
method.
2-1.Performance «peri/leaMon»
Pmmarr
z. CaUbcadaa caar >.
S. Zen drift (ZM>
4. Zero drtft. W h> i
a. Calibration drift (2 b)«..
&. Calibration drtti (34 a)«
7. Responsv tf2ce...»M_..
s. OpmUaaal pvted.
<30 pet nftlM mean vain* of tb*RfensuemcU>od tot
t of (sen (SO pet, SO pet) oUIbradoo «af nlxtors
ipetiXspssi
Do.
Do.
iSpct-ofipan
of »bso!au mean value nlos M pet eo-uUenoct nurval of a serial of Uats.
8JJ Calibration Oas Analyse*. Triplicate
analyses of the gas mixture* shall be per-
formed within two weeks prior to use using
Reference Methods 8 for SO, sad 7 for NCK.
Analyze each calibration gas mixture (80%.
M%) and record the results on the example
Sheet shown la Figure 3-1. Zaeb sample test
result mot be within 30 percent of the aver-
aged result or the testa shall be repeated.
This step may be omitted for non-extractive
monitors where dynamic calibration gas mix-
tures are not used (9.1.3).
-jj Calibration gum Test Procedure.
Make a total of IS nonconsecutlve measure-
ments by alternately using zero gas and each
calibration gas mixture/concentration (e.g.
0%. 80%. 0%. 90%. 80%. 90%. 80%. 0%.
*te.).*ui ueunUauiiiB UWlUuuuuj u.M.Uur-
'"f fTTtfT"* *^1> t"^ 1"~* ~"T *****
a. Performance Specification Test
dun*. The following teat procedures shall be
used to determine coalormance with the
requirements of paragraph 6. For NO*-An-
alyzer- that oxidize nitric oxide (NO) to
nitrogen dioxide (NO,), the response time
test under paragraph &3 of this method shall
be performed using nitric oxide (NO) spaa
gas. other tests for HO. continuous monitor-
ing systems under paragraphs 8.1 and 8.3 end
all tests for sulfur dioxide system* shall.be
performed using the pollutant span gas cpe-
clfled by each lubpart.
8.1 Calibration Error Test Procedure. Bet
up end calibrau the complete continuous
monitoring system according to the manu-
facturer's written Instructions. This may be
accomplished either ta the laboratory or la
-'«* rr*
92
KVB 6017-1216
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APP.B
Title 40Protection of Environment
cell* whose concentrations are certified by
the manufacturer to be functionally equiva-
lent to these gas concentrations. Convert the
continuous monitoring system output read-
ings to ppm and record the result* on the
example sheet shown In Figure 2-2.
8JJ Field Text for Accuracy (Relative),
Zero Drift. and Calibration Drift. Install and
operate the continuous monitoring system In
accordance with the manufacturer's written
Instructions and drawings as follows:
6.3.1 Conditioning Period. Offset the zero
setting at least 10 percent of the spaa so
that negative zero drift can be quantified.
Operate the system for aa Initial IBS-hour
conditioning period In normal operating
6.2.3 Operational Test Period. Operate the
continuous monitoring system for aa addi-
tional 168-hour period retaining the cero
offset. The system shall monitor the source
effluent at all time* except when being
ceroed, calibrated, or backpurged.
6J3.2.1 FJemsst^B!.JLCSJlB3.JS*l*SlS»J^
For continuous monitoring systems employ*
ing extractive sampling, the probe tip for the
continuous monitoring system and the probe-
tip for the Reference Method sampling train
should be placed at adjacent location* la the
duct. For NOj continuous monitoring sys-
tems, make 37 NOr concentration measure-
ments, divided into nine sets, using the ap-
plicable reference method. Ho more than one
set of tests, consisting of three individual
measurement*, shall b» performed la lay
oae hour. All individual measurements of
each set shall be performed concurrently.
or within a three-minute latervml aad the
results averaged. For SO, continuous moni-
toring systems, make nine BO, coneenSMion
measurements using the applicable reference
method. Mo more *>'«'> 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 la Figure
3-3.
4333 Field Test for Zero Drift and Cali-
bration Drift. For extractive systems, deter-
mln* the values given by zero aad spaa gas
pollutant concentrations at two-hour Inter-
vals until U sets of data are obtained. Par
praduciag_a_s»ro-oondltton-
swtem chert nf thf analvi
ad-ail- electron
4aternal uiiflurs
bf-l
ng-Us
initujy^ inftiTifUng 4fr^
>nrt rtatacttn.' mhly-ar
Belli aad computing the aero polntfrom-the
nrisrils uisaauremeaU. g Uiis- Utter -tach-
nlqua la nsert, a grsph(s) must be retain*!
by-lb* -owner -or-operator-Tor each-measure^
meat system that shows the relatlenatilp b«-
tweea the-gp»eale-measTgein«nts~aad tne
TO polnt-_Xh« span-of-th» system shan be
checked AT Mtef « r^m^yim, nn rrll imr
tiflfirt Ty the, manufaoturer-to-be -fancttoB-
alli-equi valent-«o-60 percent of span coneen-
-ttatloa. tlecord the cero and spaa uieesin*
meats (or the computed zero drift) on the
example data sheet abown In Figure 3-4.
The two-hour periods over which measure-
ments are conducted need nai be consecutive
but may not overlap. All measurements re-
quired under "ii. paragraph may be eon-
ducted concurrent with testa under para-
graph 8.2.2.1.
6.2.2.3 Adjustments. Zero and eallbratlgn
corrections and adjustments 4>> .llawgd only
at 24-hour intervals or at such shorter In-
tervals as the 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 163-hour
operational test period, record on the ex-
ample sheet shown In Figure 25 the values
given by zero and span gas pollutant con-
centrations before and after adjustment at
24-hour Intervals.
6 J Field Test for Response Time,
6 J.I 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.
6.3.2 Response Time Test 'Procedure. In-
troduce cero gas Into the continuous moni-
toring system sampling Interface or as close
to the sampling Interface as possible. When
the system output reading has stabilized.
switch quickly to a known concentration of
pollutant gas. Record the time from concen-
tration switching to 85 percent of ""»' 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.
this teat leouenT* +*~. fgi times
^
Record the results of each test on the
example sheet shown la Figure 3-6.
7. Calculations, Data Analysis and Report-
ing.
7J Procedure for determination of mean
value* and confidence Intervals.
T.I.I The mean value at a data set i*
calculated according to equation 3-1.
* «- Equation 2-1
where:
«.=abaoltite value of the measurements,
l=sum of the individual values,
x=mean value, aad
n= number of data points.
74 J The 88 percent confidence interval
(two-sided) Is calculated according to equa-
tion 3-3:
Equation 2-2
93
K7B 6017-1216
-------
Chapter 1Environmental Protection Agency
App.B
here:
EX i=sum of all data points,
tjn=t,-o/2, and
C.I.«=-95 percent confidence interval
estimate of the average mean
value.
Values for'.975
centratlon measured under 8.13 (Figure 3-3).
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 rum of the absolute
value of the mean difference and the 95 per-
cent confidence Interval) as a percentage of
each respective calibration gas concentra-
tion. Dee example sheet sbown In Figure 3-3.
7.2.3 Zero Drill (2-hour). Using the zero
concentration values measured each two
hours during the Held 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 the zero drift
as the sum of the absolute mean value and
the confidence Interval as a percentage of
span. Use example sheet sbown In.Figure
71>* value* In this table are already cor-
rected for n-1 degrees of freedom. Use a
equal to the number of samples as data
point*.
7.2 Data Analysis and Reporting.
7.2.1 Accuracy (Relative). For each of the
nine reference method test point*, determine
the average pollutant concentration reported
by the continuous monitoring system. These
average concentration* shall be determined
from the continuous monitoring system data
recorded under 7.2.2 by Integrating or aver-
aging the pollutant concentration* over tu***
of the tune Intervals concurrent with each
reference method testing period. Before pro-
ceeding to the nezt step, determine the oasis
(wet or dry) of the continuous monitoring
system data and reference method test data
concentration*. If the base* are not con-
sistent, apply a moisture correction to either
reference method concentrations or the con-
tinuous monitoring system concentrations
a* 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 **** difference for twft test
run by subtracting the respective reference
method test Ti?TVTM***tiffn* (us* average of
each set of three measurements for NO.)
tram the continuous monitoring system late-
grated or averaged concentrations. Using
these data, compute the mean difference and
the K percent confidence Interval of the dif-
ferences (equations 3-1 and 3-3). Accuracy
to reported a* the sum of the absolute value)
of the mean difference and the 99 percent
confidence interval of the differences ax-
pressed as a percentage of the mean refer-
ence method value. Use the f*ffipl^ sheet
atoown In Figure 3-4.
/ 7A2 Calibration rrror. Dsmg the data
from paragraph 6J. subtract the measured
pollutant concentration determined under
paragraph 6.1 J (Figure 3-1) from the value
shown by the continuous monitoring system
Cor each of the five readings at each eon-
7.2.4 Zero Drift (24-hour). Using the zero
concentration values measured every 34
hours during the field test, calculate the dif-
ferences between the zero point after zero
adjustment and the zero value 24 hours later
Just prior to zero adjustment. Calculate the
PP»«T^ value of th*«^ point* f"** the confi-
dence Interval using equations 2-1 and 2-3.
Report the zero drift (the sum of the abso-
lute mean and confidence Interval) a* a per-
centage of spaa. Use example tbect sbown in
Figure 3-6.
13Jt Calibration Drift (3-hour). Using
the calibration values obtained at two-hour
Interval* during the field test, calculate the
difference* between consecutive two-hour
readings expressed as ppm. These values
should be corrected for the corresponding
zero drift during that two-hour period. Cal-
culate the mean and confidence Interval of
these corrected difference values using equa-
tions 3-1 and 2-2. Do not use the 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 ebeet shown In
la Figure 3-4.
7.2.8 Calibration Drift (34-hour). Using
the calibration values measured every 34
hours during the field test, calculate the dif-
ference* between the calibration concentra-
tion reading after sen and calibration ad-
justment, aad the calibration concentration
reading 34 hours later after zero adjustment
but before calibration adjustment. Calculate
the mean value of these differences aad the
~*n*tt-n~. interval using equation* 3-1 aad
3-2. Report the calibration drift (the sum of
the absolute mean aad confidence interval)
a* a percentage of spaa. Use the example
beet anown la Figure 2-5.
7.3.7 Response Time. Udng the charts
from paragraph SJ. calculate the time Inter-
val from concentration switching to 99 per-
cent to the final stable value for all upscale
aad downscal* tests. Report the mean of the.
three upscale test times sad the mesa of the
three downscale test times. The two aver-
age times should not differ by more than 19
percent of the alower time. Report the dower
94
KVB 6017-1216
-------
App.B
jjl|e 40Protection of Environment
u the system response time. Use the ex-
ampla sheet shown In Figure 3-fl.
7.2.8 Operational Test Period. During the
168-hour performance and operational test
period, the continuous monitoring system
ihall not require any corrective maintenance,
repair, replacement, or adjustment other than
that clearly specified as required in the op-
eration »nd maintenance manuals as routine
Ad expected during a one-week period. If
the continuous monitoring system operates
within the specified performance parameters
and does not require corrective maintenance,
repair replacement or adjustment other than
u specified above during the 168-hour test
period the operational period will be success-
fully concluded. Failure of the continuous
monitoring system to meet this requirement
thai] call for a repetition at the 168-hour test
period. Portions or the test which were satis-
factorily completed need not b« repeated.
Failure to meet any performance specifica-
tions shall call for a repetition of the one-
week performance test period and that por-
tion of the testing which Is related to the
fa'Jed specification. All maintenance and ad-
justments required shall be recorded. Out-
put readings shall be recorded before, and
after all adjustment!.
S. References.
8.1 "Monitoring ImtaTunentaUon for u»e
Measurement of Sulfur Dioxide in Stationary
Source Emissions," Environmental Protection
Agency. Research Triangle Park, H.C, Feb-
ruary
g.2 "Instrumentation for the Determine-
Won of Nitrogen Oxides Content of Station-
ary Source Emissions," Environmental Pro*
tectlon Agency. Research Triangle Parx. M.C.
Volume 1. APTD-0847, October 1971; Vol-
ume 2. APTD-0942, January 1972.
8.3 "Experimental Statistics." Department
of Commerce, Handbook 01. 1963, pp. 3-31.
paragraphs J-3.1.4.
8.4 -Performance Specifications for Sta-
tionary-Source Monitoring Systems for Oasei
and Visible Emissions," Environmental Pro-
tection Agency, Research Triangle Park, N.C,
EPA-450/2-74-013, January 1974.
j«l1»r->:ii»i C*t ?!Utyf»
b'trvHU f»tl«« UUt
I (««»! ClHe^-etl*^ <
-------
Chapltr I EnvirP^»mentaI*Prol««Hon Agency
App.B
Calibration Gas Mixture Oau (Fnn Figure 2-1)
«d (505) p« High (90S)
f ! Calibration fas
Run* t Concentration.ppm
Measurement Systen
Reading, pen
Differences, oca
IS
Kean difference
Confidence -interval
Calibration error
Eean Difference8 * C.I.
MM High
Average Calibration Gas Concentration
x 100
Calibration gas concentration - neasurement systea reading
Absolute value
Figure 2-2. Calibration Error Determination
96
KVB 6017-1216
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App. B
Title 40Protection of Environment
'«t
w.
1
»
mtf
nd
TIM
.
.!
U»?« 1
(w»)
« i
7
tait
tit
151
ca
'fal
rtftPtnct" i
MllM (SOj
.oaf Uriel 1
Ua4
ItUnrtU
>V«n of
5^?^
iwf« 1
(Pt-l
^f.»
(IW)
Jwf< 1
(pp«)
J
«J, Suvlt
>ier..i
(w»l
Aiulntr t-Hour
*>ltln ind rtport ctttetf uu< U itUnlrt Inti^rtud t»()
"I ".
1
MM of
uit tlffirnui
m
«(sor
y
I (Wx)
figure 2-1. tceurta BcumliutiM
9>U
S«t
TIM
BlU
Zcra
ttn
Drift Sun
tetdlnf
Brt ft
Zero)
irraorift «[**« itro Drift*
bllbrittM Drift * [««» Spn Drift*
»«lut.
97
KVB 6017-1216
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Chapter IEnvironmental Protection Agency
App.B
Date Zero Span Calibration
and Zero Drift Reading Drift
Time Reading (AZero) (After zero adjustment) (&£pan)
Zero Drift « [Mean Zero Drift* + C.I. (Zero) J
« [Instrument Span] x TOO .
CiUbratlon Drift [Mean Span Drift* * C.I. (Span) _
« [Instrument Span] x 100
Absolute value
Figure 2-5. Zero and Calibration Drift (24-hour]
98
KVB 6017-1216
-------
App. B
40Protection of Environment
Date of Test
Span Cas Concentration
Analyzer Span Setting
Upscale
Average
Downscale
Average
PCS
ppa
1 seconds
2 seconds
3 seconds
upscale response seconds
1 seconds
2 seconds
3 seconds
downscale response seconds
System average response time (slower tine) » seconds.
Xdevlatlon from slower faverace unseal e minus averiqe downscslej . ,«,, .
system average response
slower time \ ~~
^s» ^~
Figure 2-6. Response Time
3 Prrformsnce
specifications and specification teat prooe
dare* for monlton of CO, and O, from sta-
tlonary sources.
1. Principle and Applicability.
1.1 Principle. Effluent gaies are contlnu-
011*17 sampled and are analyzed for carbon
dioxide or oxygen by a continuous monitor-
ing system. Testi of the system are performed
during % witntTniiTTi operating period to deter-
mine zero drift, calibration drift, and re-
sponse time characteristic*.
1.2 Applicability. Thl* performance speci-
fication 1* applicable to evaluation of con-
tinuous monitoring systems for measurement
of carbon dioxide or oxygen. Theae specifica-
tions contain test procedures. Installation re-
quirement*, and data computation proce-
dures for evaluating the acceptability of the
continuous monltortng aystema subject to
approval by tfie Administrator. Sampling
may include either extractive or non-extrae-
UTS> (in-aitu) procedune. .
a. Apparatus.
Xl Continuous Uonltortng System for
Carbon Dioxide or Oxygen.
X3 Calibration Oaa Mixtures. Mixture of
known concentrations of carbon dioxide or
oxygen la nitrogen or air. Uldrange and BO
percent of span carbon dioxide or oxygen
concentrations are required. The 90 percent
of spaa gas mixture Is to be used to set and
check the analyzer spaa and U referred to
as spaa gas. Tor oxygen analyzers, if tb*
span Is higher than 31 percent Or ambient
air may be -used la place of the BO percent of
span calibration gas mixture. Triplicate
analyses of the gas mixture (except ambient
air) shall be performed within two weeks
prior to use using Reference Method S of
this part.
2 J Zero Qaa. A gas containing leaa 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's data
output *«" be sufficient to allow completion
of the test procedures within this specifica-
tion.
a. Definitions.
U Continuous Monitoring System. The
total equipment required for the determina-
tion of carbon dioxide or oxygen In a given
source effluent. The system consists of three
major subsystem*;:
*aj 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 sample of the
source effluent or protection of the analyzer
from the hostile aspect* of the sample or
source environment.
99
KVB 6017-1216
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Chapter 1Environmental Protection Agency
App. B
S.1.2 Analyzer. Tnat portion of the oon-
tlnuoui monitoring < ystem which senses the
pollutant gas sad generate* a signal output
that 1> a function of the pollutant coneen-
tntlan.
3.1 J Data Recorder. That portion of the
continuous monitoring system that provide*
a permanent record of the output signal in
term* at concentration unit*.
33 Span. The value of oxygen or carbon di-
oxide concentration at which the contlnuou*
monitoring system 1* set that produce* the
maximum data display output. For the pur-
pose* of this method, the span shall bo a*t
no less than 1J to 3-5 times the normal car-
bon dioxide or normal oxygen concentration
In the stack gu of the affected facility.
3.3 Mldrange. The value of oxygen or car-
bon dioxide concentration that is representa-
tive of the normal condition* IB the stack
gas of the affected facility at typical operat-
ing rates.
3.4 Zero Drift. The Changs in the contin-
uous monitoring system output over stated
period of time of normal continuous opera-
tion when the carbon dioxide or oxygen con-
centration at the Urn* for the measurements
Is zero.
j_j calibration Drift, Th* change la th»
continuous monitoring system output over a
stated tune period of normal continuous op-
eration when the carbon dioxide or oxygen
continuous monitoring system is
the concentration of span gas.
SjB f^p^f+Vr1^ Test Period. A
period of time over which the continuous
monitoring system to expected to operate
within certain performance specifications
without M*»«**i*^t^|^frd maintenance* repair or
adjustment.
3.7 Response time. The time Interval from
a step change in concentration at the input
to the continuous' monHerring system to *^+
time at which 96 percent of the correspond-
ing anal value is displayed on the continuous
monitoring system date, recorder.
4. Installation Specification.
Oxygen or cartM
dioxide
warn
Itortng systems snail be installed at a loca-
tion where mcastiremente. are directly Tepre*
sentatlve of the total effluent from the
affected faculty or representative of the earns
effluent sampled by a SO, or NO, continuous
monitoring system. This requirement ahaU
be compiled with by use of applicable re-
quirements: In Performance gr*rt«f~tnm 3 of
this appendix as follows:
aJ installation of Oxyftn or Carbon X*-
odde Continuous Monitoring Systems Hot
Used to Convert Pollutant Data. A *«rr""t;
ban be selected in accordance with
the procedures under paragraphs tau or
4A3, or Performance Specification 3 of thtt
Oarbon D1-
4.3 TnetanatloB of Oxygen 1
oxide Continuum Moalualm
to Convert Pollutant Contlnuou* Monitoring
System Data to Units of Applicable Stand-
ards. The tJUuent continuous monitoring sys-
tem (oxygen or carbon dioxide) shall be In-
stalled at a sampling location where measure-
ments that can be made are representative of
the effluent gases sampled by the pollutant
continuous monitoring tystem(s). Conform-
anca with **M« requirement may be accom-
plished in any of the following ways:
4.2.1 The sampling location for the diluent
system shall be near the aampllng location for
Uje pollutant continuous monitoring system
such that the same approximate point (s)
(extractive systems) or path (in-situ sys-
tem*) in the cross section is sampled or
viewed.
4.2.2 The diluent and pollutant continuous
*nTKTi1***r*"g systems may be Installed at dif-
ferent locations if the effluent gases at both
sampling locations are nonstratlfied as deter-
mined under paragraphs 4.1 or 4.8. Perform-
ance Specification 3 of this appendix and
there is no In-leakage occurring between the
two aampllng locations. If the effluent gases
are stratified at either location, the proce-
dures under paragraph 4.2.2, Performance
Specification 3 of this appendix ahall be used
for loxtjmiDf copttimovf rfiT?nl*47Tfr|gr fnteixDii
at that location.
S. Continuous Monitoring System Perform-
ance Specifications.
The continuous monitoring system shall
meet the performance specifications In Table
S-1 to be considered acceptable under **««
method.
A. Performance Specification Test Proce-
dures.
The following test procedures shall be need
to determine conformance with the require-
ment* of paragraph 4. Due to the wide varia-
tion existing in analyzer designs and princi-
ples of operation, these procedures an not
applicable to all analyzers. Where this occurs.
alternative procedures, subject to the ap-
proval of the Administrator, mar be em*
ployed. Any such alternative procedures must
fulfill the same purposes (verify response.
drift, and accuracy) as the following proce-
dures, and must dearly demonstrate con-
formance with specifications In Table 8-1.
41 Calibration Check. Establish a calibra-
tion curve for the continuous monitoring
system using sera, midrange. and span con-
centration gas mixtures. Verify that the) re-
sultant curve of analyzer reading compared
with the calibration gas value is '""-'TtTm
with the expected response carve as described
by the analyzer manufacturer. If the ex-
pected response carve Is not produced, addi-
tional calibration gas measurements shall
be made, or additional steps undertaken to
verify the accuracy of the response curve of
the analyzer.
«J Field Test for Zero Drift sad Cali-
bration Drift, tnetall and operate the oon-
ttmioiis monitoring system in
100
KVB 6017-1216
-------
App. B
Title 40Protection of Environment
with the manufacturer's written instructions
and drawings as follows:
TASIC S-I.Performance rpecifcatlaiu
Pamnder
Sftdftatla*
1. Zare drift O b) '
i Zero drift (24 h) ' -
1. Calibration drill (2 b) >. .
4. Calibration drift (24 b) '.
4. Oparadoiul period ...
a. RasDODH dnw. .
<0.4 pet Oi or CO*.
«*"" at absolute ouan nlus plus U pet
eoafidenea latcrral o( a wiiei of lasts.
62.1 Conditioning Period.'Offset the zero
setting at least 10 percent of span so that
negative zero drift may be quantified. Oper-
ate the continuous monitoring system for
an Initial 168-hour conditioning period la a
normal operational manner.
022. Operational Test Period. Operate the
continuous monitoring system for an addi-
tional 168-hour period maintaining the zero
offset. The system shall monitor the source
effluent at all times except whan being
zeroed, calibrated, or backpurged.
923 Field Test for Zero Drift aad Calibra-
tion Drift. Determine the values given by
zero aad mldrange gas concentrations at two-
hour intervals until IS sets of data are ob-
tained. For non-extractive continuous moni-
toring systems, determine the zero value
given by a mechanically produced zero con-
dition or by computing the zero value from
upscale measurements using calibrated gas
cells certified by the manufacturer. The mid-
range cheeks shall be performed by using
certified calibration gas cells functionally
equivalent to less than 60 percent of span.
Record these readings on the example sheet
shown In Figure 3-1. These two-hour periods
need not be consecutive but may not overlap.
In-stta CO, or O, analyzers which cannot be
fitted with a calibration gas cell may be cali-
brated by alternative procedures acceptable
to the Administrator. Zero and calibration
corrections and adjustments are allowed
only at 2i-bour Intervals or at such shorter
intervals as the manufacturer's written in-
structions specify. Automatic corrections
made by tt» continuous monitoring system
without operator Intervention or Initiation
are allowable at any time. During the en-
tire 168-hour test period, record the values
given by zero and span gas concentrations
before and after adjustment at 34-hour In-
tervals la the example sheet shown In Figure
8.3 Field Test for Response Time,
6.3.1 Scope of Test.
This test ahHl! CM accomplished using the
continuous monitoring system as Installed.
including sample transport lines if used.
Flow rates, line diameters, pumping rates.
piusuies (do not allow the pressurized cali-
bration gas to change the normal operating
pressure la the sample Une>, etc, shall be
at the nominal values for normal operation
as specified in toe manufacturer's written
Instructions. If the analyzer is used to sample
more than one source (stack), tnls teat shall
be repeated for each sampling point.
6.3.2 Response Time Test Procedure.
Introduce zero gas Into the continuous
monitoring system sampling interface or as
close to the sampling Interface as possible.
When the system output reading has stabi-
lized. switch quickly to a known concentra-
tion of gas at SO percent of span. Record Uie
time from concentration switching to 95
percent of final stable response. After the
system response has stabilized at the upper
level, switch quickly to a zero gas. Record
the time from concentration switching to 95
percent of final stable response. Alterna-
tively. for nonextractive continuous monitor-
ing systems, the highest available calibration
gas concentration shall be switched into and
out of the sample path and response times
recorded. Perform this test sequence three
(3) times. For each test, record the results
on the data sheet shown In Figure 3-3.
7. Calculations. Data Analysts, and Report-
Ing.
7.1 Procedure for determination of mean
values and confidence intervals.
7.1.1 The mean value of a data set Is cal-
culated according to equation 3-1.
Equation 3-1
where:
x.= absolute value of the measurements,
t = tum of the Individual values.
i = mean value, and
a=number of data points.
7.3.1 The 95 percent confidence interval
(two-sided) Is calculated according to eoua-
Uao.3-2: ^^
'n-1
Equation 3-2
where:
ZXssnm of all data points.
«JB75=t,-«/a.and
CJ^=B5 percent confidence Interval es-
timates of the average mean value.
*J?S
101
KVB 5017-1216
-------
Chapter IEnvironmental Protection Agency
App. B
Tbe values In this table in already corrected
(or a-1 degreea of freedom. Use n equal to
the number of samples as data point*.
7-2 Data Analysis aod Reporting.
7.2.1 Zero Drift (2-hour). Using the zero
concentration values measured each two
Sours during the field test, calculate tbe Oil
ference* between tne conaecutlTC two-hour
readings expressed In ppm. Calculate the
mean difference and tne confidence Intern!
using equations 3-1 and 3-2. accord the sum
at the absolute mean value and tne confi-
dence interval on tile data sheet shown In
Figure 3-1.
7.2-2 Zero Drift (24-hour). Using the zero
concentration values measured every 34
hours during the field test, calculate the dif-
ferences between the zero point after aero
adjustment and the sero value 24 hours
later Just prior to zero adjustment. Calculate
the mean value .of these points and the con-
fidence interval using equations S-l and 3-2.
Record the zero drift (the sum of the ab-
solute mean and confidence interval) on ta*
data sheet shown la Figure 3-2.
7.3J Calibration Drift (3 -hour). Using the
calibration value* 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 far the corresponding
sero drift during that two-hour period. Cal-
culate the mean and confidence Interval of
these corrected difference values using equa-
tions 3-1 and 3-3. Do not use the differences
between non -consecutive readings. Becord
the sum of the absolute mean and confi-
dence Interval upon the data sheet shown
In Figure 3-1.
7.2.4 Calibration Drift (94-hour). Using tbe
calibration values measured every 34 boon
during the field test, calculate tbe differ-
ences between the calibration concentration
reading after zero and calibration adjust-
ment and the calibration concentration read-
Ing 24 noun later after zero adjustment but
before calibration adjustment. Calculate the
mean value of these differences aad the con-
fidence interval using equations 3-1 aad «-3-
Becord the sum of tbe absolute aeaa aad
confidence Interval on the data sheet shown
in Figure 8-2.
7.2.6 Operational Test Period. During the
188-hour performance and operational test
period, the continuous monitoring system
shall not receive any corrective maintenance.
repair, replacement, or adjustment other
H-«" that clearly specified sa required la tbe
manufacturer's written operation and main-
tenance manuals as routine aad expected
during a one-week period. If the continuous
monitoring system operates within the speci-
fied performance parameters and does not re-
quire corrective maintenance, repair, replace-
ment or adjustment other than as specified
above during the 188-hour test period, tbe
operational period will be successfully con-
cluded. Failure of tbe continuous monitoring
system to meet this requirement shall call
for a repetition of the 188 hour test period.
Portions of tbe test which were satisfactorily
completed need not be repeated. Failure to
meet any performance specifications shall
«*" for a repetition of tbe one-week perform-
aac* test period aad that portion of the test-
lag which is related to tike failed spectflea-
^lorj Ait m«i^t^T?**^r^ aad adjustments re-
quired shall be recorded. Output readings
shall be recorded before .and after all ad-
justments.
7.3.8 Besprmee Tim*. Using the date, devel-
oped under paragraph 8J. calculate the tun*
interval from concentration switching to 98
percent to the final stable value for all up-
scale aad dowascale testa. Report ta* mean of
the three upscale test times aad the mean of
the three downscale teat times. Tbe two av-
erage times should not differ by more than
16 percent of the slower time. Report the
slower time a* the system response am*. Re-
cord the results on Figure 9-3.
8. References,
8.1 "Performance Specifications for Sta-
tionary Source Monitoring Systems for Oases
and Visible Emissions." Environment*! Pro-
tection Agency. Research Tnangl* Park. H.C.
2PA-68Q/2-74-013. January 1874.
8-3 "Sxpertmental Statistics," Department
of Commerce. National Bureau of Standards
«!»*>>»»» 01. J98J. pp. 8-41. paragraph*
s-SO.4.
102
KVB 6017-1216
-------
App. B
Title 40Protection -of Environment
*t
la.
T1«
Ujfo 1*4
tot*
Zero
felting
Drm
(tZtro)
Sptn
hiding
Drift
(lioin)
Ctmntlw
Drift
Cillbritlm Drift (Ktui Spin 8rm4
CI ligin
1. tiro IIMI C4l«nt
-------
Chapter IEnvironmental Protection Agency
App. B
Zero Span Calibration
ind Zero Drift Reading ,Dr1ft,
ri« Reading (aZero) (After zero adjustment) USpan)
Zero Drift - [Mean Zero Drift*
Calibration Drift [Mean Span Drift*
C.I. (Zero)
C.I. (Span)
' Absolute value
Figure 3-2. Zero and Calibration Drift (24-hour)
104
K7B 6017-1216
-------
App-C
Title -40Protection of Environment
Datt of Test
Span Gas Concentration
Analyzer Span Setting
1.
Upscale 2.
3.
ppm
. PP"
seconds
seconds
seconds
Average upscale response
seconds
Downs die
1.
2.
3.
, seconds
_seconds
seconds
Average downscale response
seconds
System average response time (slcwer'tfme) seconds
Ecv^xi/ from slower m average upscale minus average dewnscale
system average response slower fine
x 10K
Figure 3-3. Response
[40 FH 4625B, Oct. 6. 197S; 40 FR 59204, 63205. Dec. 22, 1975, u amended at 42 FR 5937,
_£». 31.1977]
Amoras CDcTZBHtHATioK or ZMUSOH R&n _ _ _
5-SS«'t^ S fl)
U Tbe toUowint method ihall be ard to detennla*
wbetber a pbr"caf or operational chance to an roMnt
tadUty naulted In an ineraue la tbe cattsioo retf to the
aUnrepbere. Tbe nuthod used Is the Stadeafi I tot, where:
oonunonir ojed to mate fttfcreoeet from eauUl amplei a-Emission i»U for the fth ran.
comber of re&a
U Calculate tbe wmple mlane*, B>. far each «rt of
data aaac Xqaatlaa 2.
U Zeeta minion test «b*0 oaoaUt of « mm (axoally
time) whleb product * tmladoo nut. Tbm two net* of
aiflloniml«intmaaUen,lbt(aclUtT*ballbe
opented u U a manuul eailnloa ten were betaf per*
fanned. Valid data mint the arendnc time which would
be reqojrad U a manual emlBloa UH wen batBc eoa-
docted ataall be DMd.
S. Pnatmn.
U Bobmlpo a and b deoote pneaaan and
aJianp rnn« tlulf
U Calcolaw the ertthaietlc mean eau»*on»«ta,E, for
n-l
n-1
(2)
a.4 Calcaiau tbe pooled tttlmata, &. BOns Zqaa-
5«^( * * I
pett. L n,+«i 2 J
aaRof data (alnc Xqoatian I.
(3)
U CatcalaU the Urt aaUrte, t. aslnc *
-------
APPENDIX E
SUMMARY OF PREVIOUS DATA FROM SITE 2
106 KVB 6017-1216
-------
Location No. 18, Test No. 9
Boiler No. 2 at Location 18 is a Babcock and Wilcox integral furnace
watertube boiler with a rated capacity of 90,000 Ibs/hr steam flow and was
installed in 1935. The current top load capability is 79,000 Ibs/hr steam
flow and is limited by the fans. The furnace wall consists of watertubes
approximately 3 inches in diameter spaced 10.25 inches on centers. The
wall exposure between the tubes consists of refractory; the furnace was
rebricked in 1972. The boiler operates at a nominal steam pressure of
320 psig and steam temperature of 428°F (saturation).
Three B&W steam-atomized burners are spaced, in a triangular pattern,
with the top burner spaced directly above the center position of the lower
two burners. The vertical spacing (height of the triangle) is 36 inches, and
the horizontal spacing (base of the triangle) is 37 inches. The oil guns
use a BSW Y-jet steam atomizer with the steam pressure at the burner nominally
35 psi greater than the oil pressure. No. 6 fuel oil was used for this test.
The temperature of the oil at the burner varied from 185°F at the lower loads
to 208°F at top load. The oil pressure at the burner at top load was 85 psig.
A tubular type preheater is used to preheat the combustion air; however, no
air temperature data were available during this test.
The furnace volume and area loading, i.e., ft /MBtu/hr and ft /MBtu/hr,
and burner loading are all about average for boilers of this capacity.
The NO emissions and excess O, levels as a function of boiler steam
x 2
flow are presented in Figure E-l. Although the 0_ levels are high over the
entire load range investigated, there is not the sharp increase in 0 at lower
loads which has typically caused the emissions from other boilers to increase
at lower loads. This practice of holding the excess oxygen relatively constant
over the load range is unique to location 18 boilers and is followed consistently
at most facilities of the same company.
Maximum NO levels were found to occur at baseline to too load operating
x
conditions. The effect of excess O_ on NO emissions is presented in Figure E-2
and shows a relatively strong effect, especially for the high operating excess
107 K7B 6017-1216
-------
o
00
10 ._ 250
2
%
_ 200
NOx
@3%
Dry
- 150
(ppm
100
_ 50
T
T 1 1 r
Location No. 18
T
Unit Maximum Capacity 90K Ib/hour
Test No. 9, Fuel: Oil
10
20
Burner No. 1 Out of Service
(106% Theoretical Air to Active Brns.)
I 1
i I ' I I L
Burner
Pattern
Baseline
30
40
50
60
70
80
90
LOAD (K»/hr)
en
O
H
~j
I
i-<
to
H
CTl
Figure E-l. Effect of Load
-------
3UL»
400
1
-51 300
CNI
O
Of
<3>
X
J± fl 200
8 8"
100
«
1 1 1 1 1 1 1
Test Load: 72K Ib/hour Location No. 18
Unit Maximum Capacity: 90K Ib/hour
Test No. 8, Fuel: Oil
s~\^^~~
^^^*3J
s~*\ S^J
^^s^^
$)
/^
A 1 1 1 1 1 1 1
04 5 6 7 8 9 10 11
<] EXCESS O, (% VOL. )
^ Figure E-2. Effect of Excess Oxygen
I
cri
-------
0, levels. Since the furnace pressure is slightly negative, air may be
leaking into the flue passes through the boiler casing into the backpasses
and flue duct, such that the O levels in the furnace may be substantially
lower than those measured downstream at the sampling port.
The burner pattern previously described offered the opportunity of
experimenting with off-stoichiometric combustion by removing the center
burner (No. 1). This did not upset the symmetry of the furnace because of
the triangular arrangement of the burners. Figure E-l presents the NO and
X
O data for this test. By terminating the fuel flow to the No. 1 burner and
leaving the air registers 100 percent open, the excess air to the active
burners was reduced to two-thirds of its original value with all burners in
service, because the remaining one-third of the air was injected through
the out-of-service burner port. This test was conducted at 60,000 Ibs/hr
steam flow and an excess O_ level of 8.2 percent. Assuming the excess 0.
levels measured in the flue duct are representative of the air flow through
the burners, the percent theoretical air at the burner was reduced from
162 percent to 106 percent. The NO emissions were reduced from 240 ppm
to 175 ppm or a reduction of 27 percent.
Sulfur oxide concentrations for the baseline operating condition were
found to be 485 ppm of total SO with 465 ppm of SO . The ratio of SO,/SO
X fc J JV
for this test is 4 percent and the range of data obtained for this SO
concentration is from 2 percent to 5 percent. Particulate emissions of
0.134 lbs/10 Btu were measured for the baseline operating condition which
is about average for steam-atomized No. 6 fuel oil tests.
110 KVB 6017-1216
-------
APPENDIX F
TABULATION OF 15-MINDTE DATA
111 KVB 6017-1216
-------
»«««****«******«*»**««****«*********«*****»*****«*+****
**
**
**
**
**
* DATE
********«
* 3/14/79
** 3/15/79
** 3/16/79
** 3/17/79
*« 3/18/79
** 3/19/79
** 3/20/79
* 3/21/79
* 3/22/79
* 3/23/79
** 3/2«/79
** 3/25/79
* 3/26/79
* 3/27/79
** 3/28/79
* 3/29/79
* 3/30/79
3/31/79
* 4/ 1/79
** «/ 2/79
«/ 3/79
* 4/ 4/79
«/ 5/79
« 4/ 6/79
«« 4/ 7/79
*« «/ 8/79
** «/ 9/79
** 4/10/79
* «/ll/79
« «/12/79
*« 4/13/79
** 4/14/79
** «/15/79
* 4/16/79
** 4/17/79
4/18/79
* 4/19/79
20 HOUR DATA
DRY STACK GA3 CONCENTRATION
LOAD
TIME M*TH
!**** ***«
15,2
16.0
15.4
15.3
18,1
16.5
16,7
16.6
16.5
16.5
16.4
16.3
16.4
16.6
16.6
11.2
12.9
U.9
13.6
15.7
l*.l
16.0
16.3
16.8
17.2
20.6
20.7
17.8
13.9
17.3
1?.2
18.5
18.9
19.5
17.0
16.8
16.7
02
VOLX
MEAS
[*«*«
8.7
9.0
8.5
8.1
8.1
7.7
7.6
7.5
7.6
7.6
7.9
8.5
8.0
7.8
7.9
10.5
10.5
10.1
10.8
9,2
8.1
8.3
7.3
7.1
6.8
6.7
6.3
6.8
10.1
8.1
8.8
6.7
7.2
7.4
7.7
7.9
9.2
C02
VOLX
MEAS
***»*«
8,7
9.2
10.9
11.9
10.5
11.4
12.6
11.4
10.1
10.1
9.8
9.6
9.9
10.0
10.4
8.4
7.9
8.3
7.7
«.9
9.9
10.1
10.1
10.1
10.4
10.5
10,6
10.5
8.2
9.6
9.3
10.1
10.0
10.1
10.0
9.9
9.7
NO
PPMV
MEAS
****<
181,
193.
163.
157.
196,
162.
152.
132.
121.
119.
132.
135.
132.
111.
119.
0.
125.
133.
121.
127.
117.
123.
126.
123.
153,
163,
187.
181.
132.
165.
158,
181.
166.
173.
161.
137.
121.
NO
PPMV
jXOf
r******«
266.
2T4,
236.
220.
273.
219.
204.
175.
163.
160.
182.
195.
183.
151.
164.
0.
216.
220.
214.
196.
1<>3.
176.
165.
160.
194,
205.
229.
230.
218.
231.
234.
229.
218.
230.
218.
190.
184.
NO
NG/J
>***»«
147.
151.
130.
121.
151.
121.
112.
97.
90.
88.
100.
107.
101.
83.
90.
0.
119.
121.
118.
108.
90.
97.
91.
88,
107.
113.
126.
127.
120.
127.
129.
126,
120.
127,
120.
105.
101.
*
*
*
**
**
**
**
*
*»
**
**
**
*
«
**
**
**
**
*
*
*
*
*
*
*
*
*
«»
*
*
**
**
**
**
**
**
*
**
**
**
***«******«*********«**********************
112
KVB 6017-1216
-------
«***»»«*««****»«*****«******«*«»***»***********«*«»**»
* 15 *IN, OAT* «
* DRY STACK GAS CONCENTRATION
* **
* 02 C02 NO NO NO **
** LOAD VOLX VOLX PP"V PPMV NG/J **
** DATE TIME HWTH MEAS MEA3 MEAS 3*0? **
***«««******»*«»«**«*****«*«»*««****»«****»»»***
** OX Q/79 0 .0 .0 .0 0. 0. 0. *
** OX 0/79 0 ,0 .0 .0 0, 0. 0. **
** O/ 0/79 0 .0 .0 .0 0. 0. 0. *
* O/ 0/79 0 .0 .0 .0 0. 0. 0, *
** O/ 0/79 0 .0 .0 .0 0. 0. 0. *
» O/ 0/79 0 .0 .0 .0 0. 0. 0. **
** O/ 0/79 0 .0 .0 .0 0. 0. 0. **
** O/ 0/79 0 ,0 .0 .0 0. 0, 0. *
** O/ 0/79 0 .0 .0 .0 0. 0. 0. **
«* O/ 0/79 0 .0 .0 .0 0. 0. 0. **
*« O/ 0/79 0 .0 .0 .0 0, 0. 0. **
** O/ 0/79 0 .0 .0 ,0 0. 0. 0. «
* OX 0X79 0 .0 .0 .0 0. 0, 0. ««
** OX 0X79 0 .0 .0 ,0 0. 0. 0. »*
* OX 0X79 0 .0 .0 .0 0, 0. 0, *«
** OX 0X79 0 .0 .0 .0 0. 0. 0, *»
* OX 0X79 0 .0 .0 ,0 0. 0. 0. «*
* OX 0X79 0 .0 .9 .0 0. 0, 0. **
** OX 0X79 0 .0 .0 .0 0. 0, 0. »
* OX 0X79 0 .0 .0 .0 0. 0. 0. **
** OX 0X79 0 .0 .0 .0 0. 0. 0. **
** OX 0X79 0.0 .0 .0 0. 0. 0. **
* OX 0X79 0 ,0 .0 .0 0. 0. 0, **
*« OX 0X79 0 .0 .0 .0 0. 0. 0. *
** OX 0X79 0 .0 .0 ,0 0. 0. 0. **
* OX 0X79 0 .0 .0 .0 0. 0. 0. **
** OX 0/79 0 .0 .0 .0 0. 0. 0. *
*« OX 0X79 0 .0 .0 .0 0. 0. 0. *
** OX 0X79 0 .0 .0 .0 0, 0. 0. **
«* OX 0X79 0 ,0 .0 .0 0. 0. 0. »*
** OX 0X79 0 .0 .0 .0 0. 0. 0. *«
*« OX 0X79 0 .0 .0 .0 0. 0. 0. *«
** OX 0X79 0 .0 .0 .0 0. 0. 0. «
** OX 0X79 0 .0 .0 .0 0. 0. 0. **
** OX 0X79 0 .0 .0 .0 0. 0. 0. **
** OX 0X79 0 .0 .0 .0 0. 0. 0,
** OX 0X79 0 .0 .0 .0 0. 0. 0, *
* OX 0X79 0 .0 .0 .0 0. 0. 0. **
*« OX 0/79 0 .0 .0 .0 0. 0. 0. *
** O/ 0/79 0 .0 .0 .0 0. 0. 0. *
** OX 0X79 0 .0 .0 .0 0. 0. 0. **
** OX 0X79 0.0 .0 .0 0. 0. 0. *«
** OX 0X79 0 .0 .0 .0 0. 0. 0. «
* 3Xl«X79 1100 11.1 9.9 7.8 156. 255. 1«0. *
** 3/H/79 HIS 11.6 9.8 7.8 161. 259. 103.
** 3/l«/79 1130 11.6 9.7 7.8 164. 262. 1«5.
* 3/l«X79 1105 11.6 9.7 7.8 163. 2<>0. 103. *
» 3X1«X79 1200 11.6 9.6 7.9 163. 258. 102. «
A*************************************************************
113 KVB 6017-1216
-------
a****************************
*« 15 MIN
«* OBY STACK GAS
**
**
**
** DATE
TIME
LOAD
NWTH
02
VOLZ
HEAS
**************
. DATA
CONCENTRATION
COS
VOL*
HEAS
NO
PPMV
HEA3
*****************
»*
*
NO
PPMV
3X02
N(J
NG/J
**
*
**
**
a**************************************************************
»* 3/14/79
** 3/U/79
*» 3/14/79
** 3/14/79
* 3/14/79
3/14/79
** 3/14/79
** 3/14/79
** 3/14/79
** 3/ia/79
3/14/79
« 3/14/79
** 3/14/79
* 3/14/79
* 3/14/79
** 3/14/79
** 3/14/79
** 3/14/79
** 3/14/79
* 3/14/79
* 3/14/79
*« 3/14/79
* 3/14/79
** 3/14/79
»« 3/14/79
** 3/14/79
* 3/14/79
« 3/14/79
*« 3/14/79
«* 3/14/79
** 3/14/79
*« 3/14/79
** 3/14/79
* 3/14/79
*« 3/14/79
» 3/14/79
** 3/14/79
*« 3/14/79
« 3/14/79
* 3/14/79
** 3/14/79
** 3/14/79
** 3/14/79
** 3/14/79
* 3/14/79
3/14/79
* 3/14/79
** 3/14/79
1215
1230
1245
1300
1315
1330
1345
1400
141S
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
11.4
11.4
11.4
11.4
13.6
13.6
13.6
13.6
16.3
16.3
16.3
16.3
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
9.6
9.7
9.7
9.7
9.6
9.1
8.5
8.4
8.3
6.4
8.3
8.3
8.3
8.3
8.3
8.3
8.4
8.5
8.5
8.5
8.5
8.5
8.5
8.6
8.6
8.6
8.7
8.6
8.6
8.6
8.5
8.5
8.5
8.5
8.5
8.5
8.5
8.5
8.5
8.6
8.5
8.5
8.5
8.5
8.5
8.5
8.6
8.7
7.9
7.9
7.9
7.9
8.3
8.7
8.9
8.9
8.9
8.9
.9
.9
.9
.9
.9
.9
.9
.9
.9
,9
.8
.8
.9
8.
8.
8.
8.
8.
8.
8.
8.
8.
8.
8.
8.9
8.9
8.9
8.8
8,8
.8
.8
.8
.8
.8
.8
.7
8.7
>62.
161.
156.
153.
165.
173.
184.
186.
189.
191.
193.
196.
199.
200.
203.
203.
191.
191.
191.
190.
190.
189.
189.
188.
186.
185.
183.
182.
180.
179.
178.
177.
176.
173.
172.
172.
172.
173.
173.
171.
173.
180.
182.
185.
189.
191.
194.
197.
257.
258.
249.
246.
262.
263.
267.
268.
269.
273.
275.
279.
282.
285.
289.
289.
274.
275.
274.
274.
274.
274.
274.
273.
272.
270.
268.
266.
262.
260.
258.
256.
253.
250.
248.
249.
250.
251.
251.
248.
250.
260.
263.
267.
274.
277.
282.
289.
»«2.
t<>2.
137.
136.
145.
1«5.
t«7.
148.
148.
151.
152.
154.
156.
157.
159.
159.
151.
151.
151.
151.
151.
151.
151.
150.
150.
149.
148.
147.
144.
143.
142.
141.
140.
138.
137.
137.
138.
138.
138.
137.
138.
143.
145.
147.
151.
153.
156.
159.
**
**
**
**
**
**
*
**
*
*
«*
**
**
»*
**
«*
**
**
*
**
**
**
*
**
**
**
*
**
**
*
*«
**
**
**
**
*
**
*
**
**
**
**
*
**
**
**
a*************************************************************
114
KVB 6017-1216
-------
»««*«**»«****»**»»»«»*»**«***»****»**«»*******<
**
**
**
**
**
« 0*TE
15 KIN. D»TA
OBY STACK GAS CONCFNTHATION
TIME
LOAD
MKTH
02
VOLX
MEAS
C02
VOLX
HCAS
NO
PPMV
M£AS
NO
PPMV
3X0"
*»«»***«**»«*»««*******«***********»»»***«
»* 3/15/79
** 5/15/79
** 3/15/79
3/15/79
** 3/15/79
* 3/15/79
«* 3/15/79
** 3/15/79
** 3/15/79
* 3/15/79
** 3/15/79
* 3/15/79
* 3/15/79
** 3/15/79
* 3/15/79
** 3/15/79
** 3/15/79
** 3/15/79
» 3/15/79
** 3/15/79
** 3/15/79
** 3/15/79
** 3/15/79
** 3/15/79
** 3/15/79
* 3/15/79
* 3/15/79
3/15/79
3/15/79
* 3/15/79
* 3/15/79
** 3/15/79
* 3/15/79
* 3/15/79
** 3/15/79
** 3/15/79
** 3/15/79
** 3/15/79
** 3/15/79
* 3/15/79
** 3/15/79
** 3/15/79
** 3/15/79
** 3/15/79
** 3/15/79
* 3/15/79
* 3/15/79
** 3/15/79
15
30
05
100
115
130
105
200
215
230
205
300
315
330
305
000
415
030
oo5
500
515
530
545
600
615
630
645
700
715
730
745
aoo
815
830
805
900
915
930
90S
1000
1015
1030
1045
1100
1115
1130
1145
1200
16.1
16.1
16.1
16.1
16.0
16.0
16.0
16.0
15.8
15.8
15.8
15.8
16.1
16.1
16.1
16.1
16.0
16.0
16.0
16,0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.1
16.1
16.1
16.1
16.0
16.0
16.0
1*.0
16.0
16.0
16.0
16.0
8.8
8.8
8.8
8.8
8.8
8.9
9.0
8.9
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
8.9
9.0
8.9
8.9
9.0
9.1
9.1
9.2
9.1
9.1
9.0
9.0
9.0
9.0
8.8
8.8
8.8
a. a
8.8
8.7
8.7
8.7
8.7
8.8
8.8
8.7
8.7
8,8
8.7
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
a. a
8. a
8.8
8,9
8.9
8.9
8.9
8.9
8.8
8.8
8. a
8.8
.0
9.0
9.4
9.0
9.4
9.4
9.4
9.0
*01.
203.
205.
207.
207.
204.
202.
200.
200.
205.
206.
205.
205.
205.
205,
205.
205.
205.
204.
204.
203.
202.
202.
201.
200.
199.
199.
199.
199,
198.
199.
200.
200.
201.
201.
1.
199.
201.
180.
176.
179.
181.
175.
173.
170.
176.
176.
177.
298.
300.
303.
306.
306.
304.
303.
305.
306.
309.
310.
309.
309.
308.
308.
309.
308.
308.
307.
307.
305.
304.
303.
301.
300.
299.
300.
300.
299.
297.
300.
300.
301.
301.
300.
-1.
296.
300.
270.
268.
272.
277.
267.
262.
264.
260.
265.
267.
NO
NG/J
«*
*
**
**
*
**
i**********
164.
165,
167.
169.
169.
168.
167,
168.
169.
170.
171.
170.
170.
170.
170.
170.
170.
170,
169,
169,
168.
168.
167.
166,
165.
165.
165.
165,
165.
164,
165.
166,
166.
166.
166,
1.
163.
165,
109,
108.
150.
152.
147.
140.
145.
106.
106.
107.
**
**
**
*
**
**
*«
**
**
**
**
**
**
**
»«
«*
»*
**
**
**
*
**
*
**
»
*
**
**
**
**
**
*
*
**
**
**
*
*
*
**
**
**
**
**
**
*
A*************************************************************
115
KVB 6017-1216
-------
**«*«*********************ft*****«****«*****«»*****«******»
« j5 "IN. OAT* *
** OR* STACK GAS CONCENTRATION **
»* **
* 02 C02 NO NO NO «*
ft* LOAD VOLX VOLX P"«V PPMV NG/J «
** DATE TIME MMTH MEAS HEAS HEAS 5*02 *
a**************************************************************
* 3/15/7*
** 3/15/79
** 3/15/79
** 3/15/79
* 3/15/79
3/15/79
3/15/79
* 3/15/79
* 3/15/79
* 3/15/79
** 3/15/79
3/15/79
** 3/15/79
3/15/79
* 3/15/79
** 3/15/79
3/15/79
* 3/15/79
** 3/15/79
* 3/15/79
** 3/15/79
** 3/15/79
* 3/15/79
** 3/15/79
ft* 3/15/79
** 3/15/79
* 3/15/79
* 3/15/79
ft* 3/15/79
ft* 3/15/79
ft* 3/15/79
3/15/79
« 3/15/79
«« 3/15/79
ft* 3/15/79
* 3/15/79
* 3/15/79
ft* 3/15/79
** 3/15/79
* 3/15/79
ft* 3/15/79
* 3/15/79
** 3/15/79
* 3/15/79
** 3/15/79
** 3/15/79
* 3/15/79
* 3/15/79
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
laaS
1500
1515
1530
1545
1600
1*15
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
16.0
16.0
16.0
16.0
16.1
16. 1
16.1
16.1
16.4
16.4
16.4
16.4
16.0
16.0
16.0
16.0
16.1
16.1
16.1
16.1 (
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
15.8
15.8
15.8
15.8
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
1*«0
16.0
16.0
16.0
.0 0
.0
.0
.0
.0
.0
.0
.0
.8
.7
.7
.7
.0
.0
.0
.0
.0
.0
.9
1.9
.9
0
.0
.0
.0
.0
.0
.1
.0
.0
.0
.0
.0
.0
.0
.1
'
.4
.a
.4
.4
.4
.4
.4
.4
.5
.7
.8
.7
.6
.4
.4
.4
.4
.4
.5
.5
.5
.5
.4
.4
.4
.«
.«
.5
.4
.4
.5
.5
.5
.5
.5
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.5
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.6
.6
.6
.6
.6
.6
.6
.6
.5
.6
178.
180.
182.
182.
182.
182.
182.
181.
182.
179.
176.
172.
167.
166.
169.
167.
166.
167.
167.
167.
167.
166.
165.
165.
166.
166.
165.
164.
165.
165.
165.
165.
165.
165.
166.
163.
162.
163.
164.
164.
163.
163.
163.
163.
163.
163.
163.
1*3.
267.
269.
272.
274.
274.
273.
274.
273.
269.
263.
258.
253.
252.
250.
254.
251.
249.
250.
249.
2«8.
248.
250.
249.
249.
249.
249.
249.
249.
249.
249.
249.
249.
248.
249.
249.
248.
242.
244.
243.
244.
242.
244.
242.
243.
242.
242.
242.
241.
1«7.
148.
150,
151.
151.
151.
151.
151.
148.
145.
142.
139.
139.
138,
140.
138.
138.
138.
137.
137.
137.
138.
137.
137.
137.
137.
137.
137.
137.
138.
137.
137.
137.
137.
137.
137.
134.
134.
134.
134,
133.
134.
134.
134.
133.
134.
134.
133.
*
**
**
*
**
**
**
**
*«
**
**
**
**
**
**
**
**
*«
**
*
**
**
**
**
**
*
**
*
**
**
*
**
*
*
*
**
**
**
*
**
**
**
**
**
ft**************************************************************
116
KVB 6017-1216
-------
** 15 "IN. DAT*
* DHY STACK GAS CONCENTRATION
ft*
*
*
»* DATE
TIME
LOAD
MWTH
02
VOLX
MEAS
C02
VOLX
MEAS
NO
PPMV
MEAS
**
**
NO
PPMV
3X0*
NO
NG/J
*
**
**
**
ft**************************************************************
** 3/16/79
* 3/16/79
** 3/16/79
»* 3/16/79
« 3/16/79
»* 3/16/79
*» 3/16/79
3/16/79
*« 3/16/79
*« 3/16/79
* 3/16/79
* 3/16/79
*« 3/16/79
»* 3/16/79
** 3/16/79
** 3/16/79
** 3/16/79
** 3/16/79
** 3/16/79
* 3/16/79
« 3/16/79
** 3/16/79
* 3/16/79
« 3/16/79
** 3/16/79
** 3/16/79
»* 3/16/79
« 3/16/79
** 3/16/79
ft* 3/16/79
** 3/16/79
** 3/16/79
«* 3/16/79
** 3/16/79
* 3/16/79
»* 3/16/79
ft* 3/16/79
** 3/16/79
** 3/16/79
ft* 3/16/79
* 3/16/79
ft* 3/16/79
* 3/16/79
** 3/16/79
** 3/16/79
** 3/16/79
« 3/16/79
* 3/16/79
15
30
45
100
115
130
105
200
215
230
215
300
315
330
3«5
400
«15
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
14.6
1<*.6
1«.6
14.6
14,6
14.6
14.6
14.6
1«,6
1«.6
14.6
14.6
14.6
14,6
1".6
14.6
14, a
14.4
14.4
14.4
15.8
15.8
15.8
15.8
15.8
15.8
15.8
15.8
15.7
15.7
15.7
15.7
15.7
15.7
15.7
15.7
16.0
16.0
16.0
16.0
16.1
16.1
16.1
16.1 .
16.0
16.0
16.0
16.0
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.9
.8
.7
.8
.3
.8
8.8
8.8
8.8
8.9
8.8
8.8
9.1
9.0
9.2
9.2
9.2
9.1
9.2
9.1
9.0
8.9
8.9
8.8
8.8
8.8
8.8
-1.0
9.1
9.0
9.0
9.2
1.0
8.2
8.2
9.7
9,7
9.7
9.6
9.6
9,7
9.7
9.6
9.6
9.6
9.6
9.6
9.7
9.6
9.7
9.8
9.7
9.0
9.7
9.7
9.7
9.7
9.7
9.7
9.7
9.5
9.5
9.4
'.3
9.3
9.4
9.3
9.3
9.4
9.5
9.5
9.6
9.6
9.7
9.7
9.7
9.7
9.7
9.7
9.6
.0
12.0
12.0
163.
164.
164.
162.
162.
162.
163.
162.
162.
162.
162.
162.
163,
162.
163.
164.
163.
157.
161.
161.
163.
160*
159.
159.
159.
157.
157.
155.
155.
155.
157.
156,
158.
161.
162.
166,
168.
171.
172.
174.
-1.
182.
183.
183.
1.
-1,
161.
161.
242.
242.
242.
240.
240.
239.
240.
240.
239.
240.
240.
240.
241.
241.
241.
241.
241.
243.
237.
239.
240.
238.
236.
236.
236.
238.
237.
239.
238.
238.
238.
239.
240.
243.
2«2.
246.
249,
253.
253.
257.
-1.
275.
275.
276.
-1.
1.
229.
228.
133.
133.
133.
132.
132.
132.
132.
132.
132.
132.
132.
133.
133.
133.
133.
133.
133.
134.
131.
132.
132.
131.
130.
130.
130.
131.
131.
132.
131.
131.
131,
132.
132.
134.
133.
136.
137,
139.
140.
1«2.
-1.
152.
152.
152.
-1.
-1.
126.
126.
ft*********************************************************
*
**
«*
**
**
**
**
«
*
**
**
**
*
*«
**
**
««
**
**
**
**
ft*
ft*
**
**
ft*
ft*
**
**
**
**
**
**
*«
**
ft*
ft*
**
**
**
**
**
**
**
*
**
**
*«
****
117
KVB 6017-1216
-------
«*«***««««****.*«*«*««**«********«***
**
*
ft*
ft*
ft*
* DATE
***AA^^HHHk*H'
« 3/16/79
* 3/16/79
** 3/16/79
* 3/16/79
3/16/79
** 3/16/79
** 3/16/79
* 3/16/79
ft* 3/16/79
* 3/16/79
* 3/16/79
ft* 3/16/79
* 3/16/79
* 3/16/79
ft* 3/16/79
"* 3/16/79
* 3/16/79
** 3/16/79
** 3/16/79
* 3/16/79
ft* 3/16/79
ft* 3/16/79
* 3/16/79
3/16/79
* 3/16/79
3/16/79
** 3/16/79
3/16/79
« 3/16/79
** 3/16/79
3/16/79
** 3/16/79
* 3/16/79
ft* 3/16/79
* 3/16/79
* 3/16/79
* 3/16/79
ft* 3/16/79
** 3/16/79
ft* 3/16/79
ft* 3/16/79
* 3/16/79
* 3/16/79
* 3/16/79
ft* 3/16/79
* 3/16/79
« 3/16/79
* 3/16/79
15 MIN
DRY STACK GAS
02
LOAD VOLZ
TIME
[****
1215
1230
12«5
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
15*5
1600
1615
1630
1645
1700
1715
1730
1745
1800
1015
1030
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
MWTH MEAS
ft**ftfta«**ft*ftftft
17.3 8.3
17.3 8.3
17.3 8.4
17.3 7.0
18.5 6.4
18.5 6.5
18.5 8.
18.5 7.
16.0 7.
16.0 7.
16.0 7.
16.0 7.
16.1 8.0
16.1 8.0
16.1 7.9
16.1 7.9
15.5 7.8
15.5 8.4
IS. 5
15.5
14.8
14.8
14.8
14.8
14.8
14.8
14.8
14.8
14.6
14.6
14.6
14.6
14.8
1«.8
14.8
14.8
14.8
14.8
14.8
14.8
l«.8
14.8
14.8
14.8
14.8
14.8
14.8
.5
.4
.5
.5
.5
.5
.5
.5
.4
.4
.3
.9
.1
.2
.2
.2
.2
.2
.2
.2
.2
.3
.3
.3
.3
.3
.3
.3
.3
14.8 8.3
. DATA
CONCENTRATION
C02 NO
VOtX PPMV
MEAS
6ft ****<
12.0
11.9
12.0
13.3
13.5
13.5
12.3
12.2
12.2
12.2
12.2
12.2
12.2
12,2
12.2
12.4
12.4
0
11.8
11.8
11.7
11.8
11.7
11.7
11.7
11.7
11.7
11.7
11.7
10.2
11.8
11."
11.8
11.8
H.'
11."
11.9
11.'
11.8
11.8
11.8
11.9
11.9
11.8
11.8
11.8
11.8
11.8
MEAS
A A *** *1
162.
162.
167.
212.
21«.
21«.
157.
156.
157.
159.
160.
160.
161.
158.
157.
158.
197.
156.
149.
149.
151.
150.
150.
150.
1««.
146.
146.
148.
150.
156.
151.
153.
154.
156.
159.
162.
163.
163.
164.
165.
166.
167.
167.
167.
165.
165.
165.
166.
NQ
PPMV
3*0*
1t to 1t il ft ft 4
230.
230.
23".
274.
266.
267.
221.
216.
217.
219.
220.
221.
223.
220,
217.
217.
269.
223.
21S.
214.
217.
216.
215.
216.
214.
210.
209.
212.
214.
255.
212.
216.
218.
221.
226.
229.
230.
231.
232.
235.
237.
238.
237.
237.
234.
234.
234.
236.
NO
NG/J
ft ft ft ft ft ft i
127.
127.
132.
151.
147.
147.
122.
119.
120.
121.
122.
122.
123.
121.
11'.
120.
149.
123.
119.
118.
120.
11'.
119.
11'.
H».
116.
115.
117.
118.
141.
117.
11'.
120.
122.
124.
126.
127.
127.
128.
129.
130.
131.
131.
131.
129.
129.
129.
130.
*
**
**
*«
*
ft ft ft
*
**
ft*
**
*
*
*
*
*
*
*
*
*
*
ft*
*
*
*
*
*
*«
*
ft*
*
*
*
*
**'
*
*
«
*
**
*
*
*
**
*
*
ft**************************************************************
118
KVB 6017-1216
-------
>*»*»**»»*«*
*« 15 MIN, 0*T» *
* D»t STACK GAS CONCENTRATION «*
** **
* 02 C02 NO NQ NO
ft* LOAD VOLX VOLX PP«V PPHV NG/J **
** DATE TIME MWTH MEAS MEAS MEAS 3x0? *
ft**************************************************************
** 3/17/79
* 3/J7/79
* 3/17/79
* 3/17/79
* 3/17/79
* 3/17/79
** 3/17/79
* 3/17/79
* 3/17/79
* 3/17/79
** 3/17/79
*» 3/17/79
** 3/17/79
»* 3/17/79
3/17/79
* 3/17/79
** 3/17/79
** 3/17/79
* 3/17/79
** 3/17/79
« 3/17/79
»* 3/17/79
** 3/17/79
* 3/17/79
* 3/17/79
«* 3/17/79
** 3/17/79
« 3/17/79
* 3/17/79
« 3/17/79
** 3/17/79
«* 3/17/79
«* 3/17/79
** 3/17/79
3/17/79
«* 3/17/79
** 3/17/79
** 3/17/79
*« 3/17/79
« 3/17/79
3/17/79
« 3/17/79
* 3/17/79
3/17/79
* 3/17/79
* 3/17/79
« 3/17/79
« 3/17/79
15
30
as
100
115
130
145
200
215
230
2«5
300
315
330
3a5
400
415
430
445
500
515
530
5«5
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
14.5
1«.5
1«.5
1«.5
17.6
17.6
17.6
17.6
17.7
17.7
17.7
17.7
17.7
17.7
17.7
17.7
1'.6
1'.6
1'.6
l',6
1*. «
1*.«
!*.«
l*tfl
1°.5
1«.5
1«.5
1«.5
!«.<»
14.6
I".*
14.6
!«.<>
14.6
!«.*
!«.*
1«.5
14.5
1«.5
1«.5
!«.«
!«.*
!«.*
!«.*
14.8
14.8
14.8
14.8
8.3
8.4
8.3
8.4
8.4
8.4
8.3
8.4
8.4
8.4
8.4
8.4
8.4
8.4
8.4
8.4
8.4
8.4
'.1
8.8
8.5
8.4
8.4
8.5
8.5
8.5
8.4
8.5
8.5
8.4
8.4
8.4
8.4
8.4
8.
8.
8.
8.
8.
8.
9.
-1.0
8.2
8.1
8.0
8.0
8.0
8.0
It. 8
11.8
11.8
11.8
11.8
11.8
11.8
11.8
11.'
H."
u.«
11.8
11.8
U.8
11.8
11.8
11.8
11.8
H.2
11.3
11.8
H.8
11.8
11.8
11.8
11.8
U.8
11.8
U. »
11.9
H.'
U.'
U.8
U.8
U.8
H.'
U.'
U.'
12.0
11.'
11.'
U.'
11.'
U.'
U.'
U.'
U.'
12.0
165.
164.
164.
164,
163.
162.
163.
164.
164.
166,
165.
164.
164.
163.
162.
162.
162.
162.
!«>«.
162.
15'.
157.
158,
15'.
160.
15'.
158.
158.
157.
158,
157.
160.
1*3.
166.
168.
172.
178.
183.
I'O.
1'5.
1*1.
!«<.
1.
150.
150.
150.
150.
149.
235.
234.
234.
234.
233.
232.
232.
234.
235.
237.
237.
234.
235.
233.
232.
231.
232.
232.
248.
240.
229.
224.
227.
229.
230.
229.
227.
228.
226.
227.
226.
229.
235.
239.
241.
248.
255.
262.
273.
288,
244.
124.
1.
210.
209.
209.
209.
207.
130.
12'.
129.
129.
129.
128.
128.
129.
129.
131.
131.
129.
130.
12'.
128.
128.
128.
128.
137.
132.
126.
124.
125.
126.
127.
126.
125.
125.
125.
125.
124.
127.
129.
132.
133.
136.
1«1.
144,
151.
159.
135.
68.
-1.
116.
115.
US.
115.
114.
»*
*
*
*
**
**
**
**
**
**
**
**
**
*
*»
**
**
**
**
**
**
*
ft*
*
«
ft*
*
**
*
ft*
ft*
**
**
**
*
**
**
**
ft*
ft*
**
*
**
*
119
K7B 6017-1216
-------
I***********
* 15 KIN. DAT* **
*« DRY STACK GA3 CONCENTRATION «*
*« *«
** 02 C02 NO NO NO *
** LOAD VOL* VOLX PPMV PP*V N6/J
* DATE TIME MMTH MEAS HEAS HEAS jXOf **
A******************************************************
** 3/17/79
* 3/17/79
* 3/17/79
** 3/17/79
* 3/17/79
** 3/17/79
* 3/17/79
** 3/17/79
** 3/17/79
3/17/79
* 3/17/79
** 3/17/79
*« 3/t7/79
** 3/17/79
* 3/17/79
** 3/17/79
** 3/17/79
3/17/79
* 3/17/79
3/17/79
** 3/17/79
* 3/17/79
* 3/17/79
** 3/17/79
* 3/17/79
* 3/17/79
* 3/17/79
** 3/17/79
* 3/17/79
* 3/17/79
3/17/79
** 3/17/79
* 3/17/79
«« 3/17/79
** 3/17/79
** 3/17/79
3/17/79
** 3/17/79
* 3/17/79
» 3/17/79
** 3/17/79
* 3/17/79
* 3/17/79
* 3/17/79
* 3/17/79
** 3/17/79
* 3/17/79
3/17/79
1315
1230
1245
1300
1315
1330
1345
laoo
1415
laso
1445
1500
1515
1530
1545
1600
1*15
1630
1645
1700
1715
1730
1745
1800
1815
1630
1845
19QO
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
14.6
14.6
14.6
14.6
14.6
14.6
14.6
14.6
14.6
14.6
1«.6
14.6
1«.8
14.8
14.8
14.8
l«,8
14.8
14.8
14.8
14.8
14. fl
14.8
14.8
14.6
14.6
}4.6
14.6
14.5
i«,5
1«,5
1«.5
1«.5
14,5
1«,5
l«,5
14.4
1«.4
14.4
14.4
14.4
14.4
14.4
14.4
14. a
14.4
l«.«
14.4
7.9
7.9
7.9
7.9
7.9
7.8
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.7
7.7
8.6
7.8
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.8
7.8
7.7
11.9
12.0
12.0
12.0
11.9
11.9
12.0
12.1
12.1
12.1
12.1
12.0
12.0
12.0
12.1
12.1
12.0
12.1
12.1
12.1
12.1
12.1
12.1
12.1
12.0
12.0
12.0
11.'
11. «
10.8
11.8
11.8
11.7
11.7
11.7
11.7
11.7
11.7
11.7
11.7
M.7
11.7
11.7
ll.fr
11.*
11.*
11.7
11.7
149.
151.
152.
151.
151.
152.
153.
154.
154.
155.
157.
157.
156.
157.
158.
158.
158.
158.
157.
157.
155.
154.
154.
155.
157.
157.
155.
154.
151.
147.
151.
151.
151.
150.
150.
149.
1«7.
l«5.
145.
146.
1«7.
1«7.
1«7.
1«6.
144.
1«5.
146.
148.
207.
208.
209.
209.
208.
208.
209.
209.
209.
212.
213.
214.
212.
213.
212.
213.
213.
213.
212.
211.
208.
208.
207.
209.
211.
211.
209.
208.
205.
215.
207.
208.
209.
206.
206.
205.
203.
200.
199.
200.
201.
202.
202.
202.
199.
198.
200.
200.
114.
115.
115.
115.
115.
115.
115.
115.
115.
117.
118.
118.
117.
117.
117.
118.
117.
117.
117.
116.
115.
114.
114.
115.
116.
117.
115.
115.
113.
118.
114.
115.
115.
114,
114.
113.
112.
110.
110.
110.
HI.
111.
111.
112.
110.
109.
110.
110.
«*
**
**
**
**
**
**
**
*
*
*
**
*
*«
*
*
**
**
**
*
«
«*
*
**
*
**
**
**
**
**
**
*
*
**
**
««
**
**
»«
**
*
**
**
**
**
*«*«*************«**«****************************
120
KVB 6017-1216
-------
****************************
**
ft*
ft*
**
ft*
DATE
***ft**** ***4
** 3/18/79
** 3/16/79
* 3/18/79
* 3/18/79
** 3/18/79
* 3/18/79
** 3/18/79
ft* 3/18/79
» 3/18/79
* 3/18/79
ft* 3/18/79
ft* 3/18/79
ft* 3/16/79
* 3/16/79
3/18/79
ft* 3/18/79
** 3/18/79
ft* 3/18/79
** 3/16/79
3/18/79
* 3/18/79
** 3/18/79
** 3/16/79
** 3/18/79
** 3/18/79
* 3/18/79
ft* 3/18/79
** 3/18/79
** 3/18/79
** 3/18/79
* 3/18/79
»* 3/18/79
** 3/18/79
** 3/18/79
* 3/16/79
** 3/18/79
** 3/18/79
** 3/18/79
* 3/18/79
** 3/18/79
** 3/16/79
** 3/18/79
** 3/18/79
* 3/18/79
** 3/18/79
* 3/18/79
* 3/18/79
** 3/18/79
*******i
jS "IN. DAT*
DRY STACK GAS CONCENTRATION
TIME
ft£ ****
15
30
45
too
115
130
105
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
645
900
915
930
9«S
1000
1015
1030
1045
1100
1115
1130
1145
1200
»*****
LOAD
MHTM
k ft * * * 1
17.3
17.3
17.3
17.3
1'.3
i«.3
1"».3
l«.3
10,6
19.6
10.6
19.6
19.6
19.6
19.6
19.6
19.6
19.6
19.6
1*.6
19.6
I*t6
1*.6
19.6
20.1
20.1
20.1
20.1
20.1
20.1
20.1
20.1
20.2
20.2
20.2
20.2
20.2
20.2
20.2
20.2
20.4
20.4
20.4
20.4
20.4
20.4
20.4
20.4
«****
02
VOLX
MEAS
£ £>£ * ** 1
7.6
7.6
7.6
7.6
6.9
6.7
6.7
6.7
6.7
6.7
6.8
6.8
6.8
6.7
6.7
6.7
6.6
7.1
7.1
6.9
6.9
6.9
7.1
7.2
7.1
7.2
7.1
7.2
7.2
7.2
7.2
7.1
7.1
7.1
7.
7.
7.
7.
7.
7.
7.
7.
7.2
7.3
7.3
7.3
7,1
7.0
*******
C02
VOLX
MEAS
* * * * * *1
11.8
11.8
11.8
11.8
12.5
12.7
12.6
12.6
12.6
12.6
12.6
12.
12.
12.
12.
12.
12.
12.
12.
12.
12.
12.
12.1
12.2
12.2
12.2
12.2
12.2
12.2
12.2
12.2
12.2
12.3
12.3
12.3
12.4
12.4
12.3
12.3
12.3
12.4
10.1
10.1
10.1
10.1
10.0
10.1
10.1
»****
NO
PPMV
MEA3
151.
154.
155.
156,
199.
291.
202.
202.
202.
202.
201.
201.
201.
201.
201.
1<»9.
201.
208.
227.
232.
233.
237.
237.
236.
235.
233.
231.
232.
233.
235.
238.
239.
237.
237,
238.
239.
240.
243.
246.
248.
1.
205.
209.
207.
206.
208.
211.
216.
ft******
NO
PPMV
3«f
f ft? H ft? 1k A ft 1
204,
207.
209.
210.
253,
254.
255.
255.
255.
255.
255.
255.
255.
253.
253.
251.
252.
271.
294.
297.
298.
303.
307.
309.
306.
304.
301.
302.
305.
306.
311.
311.
306.
307.
308.
310.
310.
314.
320.
322.
-1.
2*6.
273,
273.
275.
274,
275,
277.
*******
NO
NG/J
rft1 ftft * **!
112.
U«.
115.
116.
140.
1«0,
141,
lflt.
141.
141.
140,
140.
140.
140.
too.
138.
139.
149.
162,
164.
164.
167.
169.
170.
169.
167.
166.
167.
166.
170.
172.
171,
170.
169.
170.
171.
171.
173.
176.
177.
"1.
147.
151.
151.
151.
151.
152.
153.
*******
**
*
*
**
«
*
ft* *
**
**
*
*«
*
*«
**
ft*
**
**
ft*
**
**
*
*
*
ft*
ft*
ft*
**
**
**
**
*
**
*«
**
*
**
**
*
ft*
**
**
*
**
*
**
**
**
ft*
**
**
**
**
**
**
*
***
121
KVB 6017-1216
-------
A****************************'
***********
**
**
*«
**
** DATE
t5 MIN. DATA
OPY STACK GAS CONCENTRATION
02 C02 NO
LOAD VOLX VOLX PPMV
TIME MWTM MEAS MEAS MEAS
NO
PPMV
3*0*
NO
NG/J
*
*
**
**
**
A**************************************************************
« 3/18/79
«« 3/18/79
** 3/18/79
3/18/79
* 3/18/79
** 3/18/79
** 3/18/79
* 3/18/79
«* 3/18/79
** 3/18/79
«* 3/18/79
** 3/18/79
* 3/18/79
»* 3/18/79
*« 3/16/79
* 3/18/79
** 3/18/79
*« 3/18/79
** 3/18/79
*« 3/18/79
** 3/18/79
*« 3/18/79
** 3/18/79
3/18/79
*« 3/18/79
* 3/18/79
** 3/18/79
** 3/18/79
** 3/18/79
* 3/18/79
** 3/18/79
* 3/l*/79
** 3/18/79
** 3/18/79
* 3/18/77
** 3/18/79
»* 3/18/79
** 3/18/79
** 3/18/79
** 3/18/79
** 3/18/79
*« 3/18/79
** 3/18/79
** 3/18/79
** 3/18/79
* 3/18/79
** 3/18/79
* 3/18/79
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
19.9
19.9
19.9
19,9
16.4
16.4
16.4
16.4
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16,3
16.1
16.1
16.1
16,1
16.1
16.1
16,1
16.1
16.1
16.1
16.1
16.1
16.1
16,1
16.1
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
6.9 10.2
6.9 10.2
7.1 10.2
8.3
9.1
9.1
9.1
9.1
9.1
9.1
9.1
9.2
9.2
9.2
9.1
9.1
9.2
9.2
9.2
9.2
9.1
9.2
9.2
9.1
9.1
9.1
9.1
9.2
9.5
9.3
.6
.0
.0
.0
.0
.9
.9
.0
.0
.0
.0
.0
.0
.1
.1
.1
.2
.1
.1
.1
.1
.1
.1
.1
.1
.7
.9
9.3 8.9
9.3 8.9
9.3 8.
9.3 8.
9.3 8.
9.3 8.
9.3 8.
9.2
9.2 .9
9.3 .9
9.2 .9
9.2 .9
9.2 .9
9.2 8.9
9.2 8.9
9.2 8.9
9.2 8.8
9.2 8,9
215.
216.
218.
207.
198.
200.
202.
203.
204..
205.
205.
205.
204.
204.
204.
202.
203.
201.
193.
187.
184.
182.
181.
181.
178.
177.
176.
173.
166.
167.
166.
165.
164.
159,
157.
154.
151.
149.
148.
147.
144.
142.
139.
138.
138.
137.
133.
I3tt.
276.
276,
282.
295.
301.
303.
308.
309.
310.
313.
313.
314.
312.
312.
310.
307.
310.
307.
297.
286.
280.
279.
278.
275.
271.
268.
268.
265.
262.
257.
256.
255.
254.
246.
242.
238.
233.
230.
228.
226.
221.
218.
214,
212.
211.
210.
203.
205.
152.
152.
155.
163.
166.
167.
170.
170.
171.
172.
172.
173.
172.
172.
171.
169.
171.
169.
164.
158.
154.
154.
153.
152.
150.
140.
148.
146.
145.
142.
141.
141.
14Q.
135.
133.
131.
128.
127.
126.
125.
122.
120.
118.
117.
116,
116.
112.
113.
**
**
**
*
**
**
**
**
*«
**
**
**
*
**
*«
*
**
**
**
*«
**
**
*
**
*
**
**
**
*
**
**
*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
*
**
***************************************************************
122
KVB 6017-1216
-------
***************************************************************
** l5 MIN, DAT* **
** D«Y STACK GAS CONCENTRATION **
** **
** 02 C02 NO NO NO **
* LOAD VOtX VOLX PP*V PPMV NG/J *«
** DATE TIME MWTH ME»3 MEAS MEA3 3*02 **
A****************-**********************************************
** 3/19/79
** 3/19/79
»* 3/19/79
** 3/19/79
* 3/19/79
* 3/19/79
** 3/19/79
** 3/19/79
** 3/19/79
** 3/19/79
* 3/19/79
* 3/19/79
** 3/19/79
3/19/79
«« 3/19/79
*« 3/19/79
*» 3/19/79
«* 3/19/79
«* 3/19/79
** 3/19/79
* 3/19/79
« 3/19/79
** 3/19/79
* 3/19/79
« 3/19/79
* 3/19/79
« 3/19/79
*« 3/19/79
** 3/19/79
** 3/19/79
** 3/19/79
** 3/19/79
** 3/19/79
«* 3/19/79
** 3/19/79
*« 3/19/79
** 3/19/79
* 3/19/79
* 3/19/79
«« 3/19/79
»* 3/19/79
* 3/19/79
« 3/19/79
* 3/19/79
* 3/19/79
** 3/19/79
** 3/19/79
** 3/19/79
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
15.4
15.4
15.4
15.4
16.1
16.1
16^1
16.1
16.1
16,1
16,1
16,1
16.1
16.1
16.1
18.3
18,3
18.3
18.3
18.3
18.3
18.3
18.3
18,5
18.5
18.5
18,5
18,3
18.3
18.3
18.3
17.6
17.6
17.6
17.6
16.3
16,3
16.3
16.3
16.0
16.4
16.4
16.4
16,3
16.3
9.2
8.2
7.5
7.5
7.6
7.3
7.2
7.2
7.2
7.2
7.2
7.2
7.4
7.2
7.2
7.2
7.4
7.2
7.8
7.6
7.7
7.7
7.7
7.6
7.6
7.6
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.8
8.3
7.7
7.8
7.8
7.7
7.7
7.7
7.6
7.7
7.7
7.7
7.6
7.6
7.8
8.9
10,1
10.3
10.3
10,3
10.5
10.5
10.6
10.6
10.6
10.6
10,6
10.5
10.5
10,5
10,5
10.4
10,4
9,9
10.2
10,1
10.1
10.1
10,2
10.1
10.1
10,1
10*1
10.1
10.1
10.0
10.0
10.0
10.0
9,6
10.0
10.0
10,0
10.1
10.1
12.3
12.5
12.4
12.4
12.4
12.4
12.4
12.4
134.
138,
146,
146.
146,
145.
145,
144.
144,
1*5,
145.
145,
145.
145.
146.
145.
144,
159,
153,
149,
148,
147,
147,
148.
148,
147.
148,
77.
153.
153.
154.
155.
154.
154.
155.
"1.
-1.
-I.
162,
162.
163.
164.
163,
162.
164.
165.
166)
205.
1*5,
1*5.
1*6.
1*6.
1*1.
1*0.
188.
188.
1*0.
189.
1*0.
1*2.
1*0.
1*1.
190.
1*1 .
209.
209.
202.
201.
200.
200.
200.
200.
1*9.
201.
104.
208.
208.
209.
211.
210.
211.
221.
1.
1.
1.
220.
221.
221.
221.
221.
221.
222.
222.
222.
227.
113.
107.
108.
108.
108.
105.
105.
104.
104.
105.
104.
105.
106.
105.
105.
105.
105.
115.
115.
111.
111.
110.
110.
110.
110.
109.
111.
57.
115.
115.
115.
116.
116.
116.
122.
1.
1.
1.
121.
122.
122.
122.
122.
122.
122.
122,
123.
125.
**
**
**
**
**
**
**
**
*
»»
**
**
**
**
«»
**
**
**
**
**
**
*«
*»
*»
*
**
**
»*
**
**
**
**
**
*»
**
**
**
**
*
**
*«
**
**
**
*
**
**
**
****************************************************************
123 KVB 6017-1216
-------
*
**
**
**
**
** DATE
15 "IN
OBY STACK GAS
TIME
LOAD
MMTH
02
von
MEAS
. DATA
CONCENTRATION
COS
VOLX
MEAS
NO
PPMV
MEAS
NO
PPMV
3X02
NO
NG/J
**
**
**
**
**
**
a**************************************************************
** 3/19/79
** 3/19/79
** 3/19/79
** 3/19/79
** 3/19/79
* 3/19/79
* 3/19/79
3/19/79
* 3/19/79
* 3/19/79
* 3/19/79
** 3/19/79
* 3/19/79
« 3/19/79
** 3/19/79
* 3/19/79
* 3/19/79
** 3/19/79
** 3/19/79
* 3/19/79
* 3/19/79
** 3/19/79
»* 3/19/79
3/19/79
* 3/19/79
** 3/19/79
* 3/19/79
** 3/19/79
** 3/19/79
** 3/19/79
»* 3/19/79
** 3/19/79
** 3/19/79
** 3/19/79
** 3/19/79
** 3/19/79
* 3/19/79
* 3/19/79
** 3/19/79
- 3/19/79
«* 3/19/79
3/19/79
** 3/19/79
« 3/19/79
** 3/19/79
« 3/19/79
* 3/19/79
** 3/19/79
1215
1230
1205
1300
1315
1330
13*5
1000
1015
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
16.1
16.1
16.1
16.1
16.3
16.3
16.3
1*.3
1*.3
16.3
16.3
16.3
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16,4
16.4
16.3
16.3
16.3
16.3
15.8
15.8
15,8
15.8
15.4
15.4
15.4
15.4
15.4
15.4
15.4
15,4
15.4
15.4
15.4
15.4
15.4
15.4
15.4
15.4
7.6
7.6
7.6
7.6
7.6
7.5
7.4
7.7
7.6
7.5
7.4
7.4
7.3
7.3
7.2
7.3
7.3
7.3
7.3
7.0
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.7
9.1
8.6
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
12.4
12.4
12.3
12.3
12.3
12.4
12.4
12.4
12. «
12.4
12.5
12.5
12.5
12.5
12.5
12.6
12.6
12.6
12.6
12.6
12.6
12.6
12.6
12.5
12.5
12.5
12.5
12.5
12.5
12.5
11.3
11.1
11.7
11.7
11.7
11.7
11.7
11.7
11.7
11.7
11.7
11.7
11.7
11.7
11.7
U.7
11.7
11.7
167.
169.
169.
167.
169,
170,
172.
170.
171,
172,
173,
174.
176.
179.
182.
185.
187.
191.
196.
196.
196.
191.
189.
185,
1.
169.
167.
166.
166.
167.
164,
167.
167.
167.
166.
167.
167.
167.
167.
165.
166.
166.
166.
165.
164.
165.
164.
163.
225.
227.
228.
225.
228.
227.
228.
231.
230.
231.
230.
231.
232.
235.
237.
243.
247.
252.
258.
261.
264.
257.
250.
209.
1.
227.
220.
223.
224.
227.
2«9.
2*4.
238.
238.
237.
237.
238.
238.
237.
235.
235.
235.
236.
236.
233.
234.
233.
232.
124.
125.
126.
124.
126.
125.
126.
127.
127. .
127.
127.
128.
128.
130.
131.
134,
136.
139,
102.
104.
106,
142.
140,
137.
-1.
125,
124.
123.
120.
125.
137.
134.
131.
131.
131.
131.
131.
131.
131.
129.
130.
130.
130.
130.
129.
129.
128.
128.
*
*
**
**
*
**
**
*
**
*
*
*
**
*
**
**
**
*
**
**
*
**
*
**
*
**
*
*«
**
**
**
**
**
**
**
»*
**
**
**
*
**
*
*
**
**
*
**
**
ft*************************************************************
124
KVB 6017-1216
-------
*,,************«**«««**«*******
l5 MIN. DATA **
*« DRY STACK GAS CONCENTRATION »
**
* 02 co2 NO NO NO *
» LOAD VOL* VOLX PPMV PPMV NG/J «*
* DATE TIME MNTH *EA3 NEAS MEA3 3*0f **
****»*****************«**********«**<>«***
* 3/20/79
3/20/79
3/20/79
3/20/79
»* 3/20/79
»* 3/20/79
* 3/20/79
* 3/20/79
* 3/20/79
3/20/79
** 3/20/79
* 3/20/79
»* 3/20/79
* 3/20/79
3/20/79
** 3/20/79
** 3/20/79
** 3/20/79
** 3/20/79
** 3/20/79
** 3/20/79
** 3/20/79
»* 3/20/79
** 3/20/79
3/20/79
* 3/20/79
** 3/20/79
** 3/20/79
** 3/20/79
** 3/20/79
3/20/79
*« 3/20/79
* 3/20/79
** 3/20/79
** 3/20/79
«* 3/20/79
** 3/20/79
** 3/20/79
** 3/20/79
** 3/20/79
** 3/20/79
** 3/20/79
** 3/20/79
** 3/20/79
* 3/20/79
** 3/20/79
** 3/20/79
** 3/20/79
15
30
as
too
115
130
ia5
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
16.6
16.6
1^.6
16.6
16.6
16.6
16.6
16.6
16. a
16.4
16.4
16.4
17.0
17.0
17.0
17.0
16,6
16.6
16.6
16.6
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
!*.»
16.4
16.4
16.4
I*. 4
!".«
16.4
16.4
16.4
16.4
16.4
16.4
1*.4
16.4
16.4
16.4
16.4
16.4
8.3
8.3
8.3
8.3
8.3
7.7
7.7
7.7
7.7
7.7
7.6
7.6
7.6
7.7
7.7
7.6
7.6
7.6
7.5
7.8
7.9
8.3
7.4
7.4
7.4
7.4
7.4
7.4
7.4
7.4
7.4
7.4
7.4
7.4
7.4
7.4
7.3
7.3
9.2
8.1
8.0
8.0
8.4
8.3
8.2
8.1
7.9
7.7
11.7
11.7
11.7
11.7
11.7
12.3
12.3
12.3
12.3
12.3
12.3
12.3
12.3
12.3
12.3
12.3
12.3
12.3
12.5
12.5
12.3
11.8
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
11.0
11.7
11.8
.0
.0
12.0
12.1
12.1
12.3
12.6
162.
160.
159.
159.
161.
158.
158.
159.
158.
157.
157.
157.
157.
156.
156.
155.
154.
155.
161.
203.
218.
148.
141.
142.
142.
143.
142.
142.
143.
142.
144.
1«S.
145.
145.
1«7.
147.
147.
147.
125.
138.
141.
141.
143.
144.
147.
149.
149.
152.
230.
228.
226.
226.
228.
215.
214.
215.
214.
213.
212.
212.
212.
211.
211.
210.
208.
209.
215.
278.
301.
210.
187. .
189.
189.
190.
189.
189.
1*0.
189.
1*2.
1*3.
1*2.
1*3.
1*4.
1*«.
1*4.
1*4.
1*2.
1*4.
1*5.
1*6.
205.
205.
208.
209.
206.
206.
127.
126.
125.
125.
126.
11*.
118.
118.
118.
118.
117.
117.
117.
117.
117.
116.
115.
115.
11*.
153.
166.
116.
103.
104.
104.
105.
104.
104.
105.
104.
106.
106.
106.
106.
107.
107.
107.
107.
106.
107.
107.
108.
113.
113.
114.
115.
114.
114.
*
**
*
**
**
*
**
**
«
**
»«
ft*
**
**
**
*
*
*
**
*
**
ft*
**
**
**
**
ft*
**
**
ft*
**
ft*
ft*
*
**
*
**
*
**
«
ft*
**
*
*
*
a************************************************************
125 KVB 6017-1216
-------
a*************************************************************
ft
ft
ft
ft
DATE
15 "IN
DRY STACK GAS
TIME
LOAD
MMTH
02
VOLX
MEAS
1. DATA
CONCENTRATION
C02
VOLX
MEAS
NO
PPMV
MEAS
NO
PPMV
3X0*
NO
NG/J
**
**
**
**
*
**
a**********************************************
* 3/20/79
* 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
3/20/79
*« 3/20/79
* 3/20/79
* 3/20/79
3/20/79
* 3/20/79
3/20/79
3/20/79
* 3/20/79
* 3/20/79
*« 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
« 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
* 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
ft 3/20/79
******»*
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1600
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
****«
16.7
16.7
16.7
16.7
16.7
16l7
16.7
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.8
16.8
16.8
16.8
16.2
18 2
1*.2
18.2
16.8
16.8
16.8
16.8
16.8
16.8
16.8
16.8
16.8
16.8
16.8
16.8
16.7
16.7
16.7
16.7
i«****«
7.5
7.3
7.1
7.1
7.2
7.2
7.2
7.1
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.1
7.1
7.1
7.1
7.3
7.3
7.4
7.4
7.4
7.1
7.6
7.8
7.6
7.6
7.7
7.7
7.7
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.5
7,6
7.6
7.7
7,6
7.6
7.7
7.6
7.7
****
12.8
12.9
13.1
13.0
13.0
12.9
13.0
12.9
12.9
12.9
12.9
12.9
12.9
12.9
12,9
12.9
13.0
13.0
13.0
12.9
12.9
12.9
12.9
12.9
13.4
12.9
12.5
12.7
12.7
12.7
12.7
12.7
12.7
12.8
12.8
12.7
12.7
12.8
12.8
12.9
12.8
12.7
12.7
12.7
12.8
12.8
12.8
12.8
*******
154.
156.
162.
163.
166.
168.
159.
152.
151.
150.
149,
149.
148.
149,
149.
152.
153.
154,
156.
154.
151.
150.
146.
148.
171.
198,
180.
146.
145.
144.
144.
143.
l"'
1431
143.
144.
144.
146.
146.
143.
140.
140.
140.
141.
140.
139.
139.
****
206.
206.
211.
212.
217.
219.
207.
198.
198,
196.
195.
195.
194,
194.
195.
198.
198.
201.
203.
203.
199.
198.
197.
197.
222.
268.
246.
197.
197.
196.
195,
194,
1*3,
193,
1*2,
1*3.
1*4,
194.
1*6.
195.
192.
190.
189.
190.
191.
190.
188.
188.
*******
113.
113.
116.
117.
120.
121.
114,
109.
109.
108.
106.
108.
107.
107.
107,
109,
109,
111.
112.
112.
110.
109.
106.
108.
123.
148.
136.
109.
108.
108.
108.
107.
107.
106.
106.
106.
107.
107.
108.
107.
106.
105.
104.
105.
105.
105.
104.
104.
*******
**
**
*
**
**
**
**
**
**
**
**
**
**
**
*
**
**
*
**
**
**
**
**
*
**
*
**
**
**
**
**
**
**
**
**
**
**
**
**
*
**
*
*
**
*
*
**
**
**
126
KVB 6017-1216
-------
A**************************************************************
**
**
**
**
**
** DATE
15 HIM. DATA
DRY STACK GAS CONCENTRATION
TIME
LOAD
M*TH
02
VOLX
*EAS
C02
VOLt
MEAS
NO
PPMV
MEAS
NO
PPMV
3102
NO
NG/J
**
**
**
**
*
**
A***********************************************************
** 3/21/7'
* 3/21/79
* 3/21/79
« 3/21/79
** 3/21/79
* 3/21/79
*« 3/21/79
** 3/21/79
* 3/21/79
»* 3/21/79
»* 3/21/79
** 3/21/79
»* 3/21/79
* 3/21/79
* 3/21/79
* 3/21/79
* 3/21/79
* 3/21/79
* 3/21/79
* 3/21/79
* 3/21/79
** 3/21/79
** 3/21/79
* 3/21/79
«« 3/21/79
** 3/21/79
* 3/21/79
** 3/21/79
3/21/79
** 3/21/79
** 3/21/79
«* 3/21/79
** 3/21/79
** 3/21/79
*« 3/21/79
** 3/21/79
** 3/21/79
** 3/21/79
* 3/21/79
»* 3/21/79
* 3/21/79
* 3/21/79
«* 3/21/79
*« 3/Z1/79
** 3/21/79
** 3/21/79
** 3/21/79
* 3/21/79
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
- eoo
815
630
845
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16,6
16.6
16.6
1*.*
16.6
16.6
16.6
16.6
16.4
16.4
16,4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16,4
16.4
16.»
16.4
16.4
16.4
16.4
16.4
16.6
16,6
16.6
16.6
16.6
16.6
16,6
16.6
7.7
7.6
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
8.5
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.6
7.7
7.7
7.7
7.6
7.7
7.6
7.
7,
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.4
7.3
7.3
7.2
7.2
7.2
12.8
12.8
12.8
12.8
12.8
12.8
12.7
12.7
12.7
12.7
12.7
12.7
12.7
12.0
12.7
12.7
12.7
12.8
12.8
12.8
12.8
12.8
12.8
12.8
12.8
12.8
12.8
12.8
12.8
12.8
12.8
12.8
12.8
12.8
12.8
12.8
12.7
12.7
12.6
12.6
12.6
12.5
12.6
10.2
10.3
10.3
10.3
10.3
139.
140.
102.
102.
102.
1«2.
102.
111.
101.
HI.
101.
101.
1«2.
13".
100.
139.
137.
136.
135.
135.
13*.
135.
134.
135.
137.
137.
135.
136.
137.
137.
139.
139.
139.
138.
139.
149,
151.
151.
152.
153.
t«8.
1«6.
149.
127.
128.
127.
123.
122.
iae.
190.
192.
192.
193.
193.
193.
192.
I'M.
1*1.
1*2.
1*2.
1*3.
201.
1*0.
190.
186,
1««.
183.
183.
182.
183.
182.
183.
185.
185.
183.
184.
185.
186.
188,
187.
187.
186.
1*7.
200.
203.
202.
204.
205.
201.
1*6.
199.
167.
168.
166.
161.
160.
104.
105.
106.
106.
106.
106.
106.
106.
105.
105.
106,
106.
106.
111.
105.
105.
103.
102.
101,
101,
100.
101.
100.
101.
102.
102.
101.
101.
102.
102.
104,
103.
103.
103.
103.
110.
U2.
HI.
113.
113.
HI.
108.
no.
*2.
*3.
*2.
89.
88.
«*
**
**
*
**
**
**
*
**
*»
**
**
**
»*
**
**
**
**
**
**
**
»*
**
**
**
»*
**
**
**
**
»*
*
**
**
*
**
**
*
**
**
*
**
**
**
*«
**
**
**
A************************************************************
127
KVB 6017-1216
-------
ft*************************************************************
ft*
**
**
*
** DATE
ft*£A AA***ft* A
»* 3/21/79
«* 3/21/79
** 3/21/79
** 3/21/79
*« 3/21/79
«» 3/21/79
« 3/21/79
** 3/21/79
** 3/21/79
** 3/21/79
3/21/79
* 3/21/79
« 3/21/79
«« 3/21/79
3/21/79
* 3/21/79
»« 3/21/79
*« 3/21/79
* 3/21/79
** 3/21/79
** 3/21/79
** 3/21/79
*« 3/21/79
* 3/21/79
** 3/21/79
** 3/21/79
** 3/21/79
** 3/21/79
** 3/21/79
»* 3/21/79
* 3/21/79
** 3/21/79
*« 3/21/79
** 3/21/79
* 3/21/79
** 3/21/79
** 3/21/79
*» 3/21/79
« 3/21/79
** 3/21/79
« 3/21/79
** 3/21/79
*» 3/21/79
** 3/21/79
** 3/21/79
*« 3/21/79
* 3/21/79
** 3/21/79
i5 MIN
Dflt 3T»CK SA3
TIME
******]
1215
1230
1205
1300
1315
1330
1305
1400
i4is
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
17«5
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
MHTH
>**<***
16.7
16.7
16.7
16.7
16,7
16.7
16.7
16.7
16.7
1*.7
1*.7
1*.7
16.8
16.8
16.8
16.8
16.8
16.8
16.8
16.8
16.8
16.8
16,8
16.8
16, 8
16.8
16.8
16,8
16.6
16,6
16,6
16.6
16.6
16.6
16,6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16,6
16.6
16.6
16.6
02
VOL I
ME»3
1t1l t H
-------
>*»*«*****«******«*
** 15 *IN. DATA *
* DRY STACK GAS CONCENTRATION
»* *
*
**
** DATE
TIME
LOAD
MWTH
02
VOLX
MEAS
C02
VOLX
MEAS
NO
PPHV
MEAS
NO
PPMV
jXOf
NO
NG/J
**
**
**
A**************************************************************
** 3/22/79
** 3/22/79
** 3/22/79
* 3/22/79
* 3/22/79
** 3/22/79
** 3/22/79
* 3/22/79
* 3/22/79
** 3/22/79
* 3/22/79
«* 3/22/79
* 3/22/79
* 3/22/79
«* 3/22/79
* 3/22/79
** 3/22/79
** 3/22/79
* 3/22/79
** 3/22/79
** 3/22/79
** 3/22/79
* 3/22/79
* 3/22/79
** 3/22/79
** 3/22/79
** 3/22/79
*« 3/22/79
** 3/22/79
** 3/22/79
* 3/22/79
«* 3/22/79
** 3/22/79
«* 3/22/79
** 3/22/79
** 3/22/79
* 3/22/79
* 3/22/79
** 3/22/79
»* 3/22/79
« 3/22/79
** 3/22/79
** 3/22/79
** 3/22/79
** 3/22/79
* 3/22/79
« 3/22/79
» 3/22/79
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
8tS
830
845
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
16.6
16.6
16.6
16.6
16.6
16,6
16.6
16,6
16.6
16.6
16,6
16.6
16.6
16.6
16.6
16.6
16.7
16.7
16.7
16.7
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.6
16.6
16.6
16.6
16.4
16.4
16.4
16.4
16^4
16. a
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
8.4
7.9
7.7
7.6
7.6
7.7
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.7
7.7
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
10.2
10.2
10.2
10.3
10.3
10.3
10.3
10.3
10.3
10.3
10.3
10.3
10.3
10.2
10.2
10.2
9.7
10.0
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.3
10.2
10.2
10.2
10.1
10.1
10.1
10.1
10.1
10.1
10.2
10.1
10.0
10.0
10.1
10.1
10.1
117.
118.
118.
117.
116.
US.
114.
113.
1 1".
114.
US.
115.
116.
117.
118.
117.
111.
113.
114.
114.
113.
113.
112.
111.
114.
115.
115.
115.
116.
115.
116.
117.
117.
116.
116.
127.
128.
129.
129.
129..
129.
129.
125.
126.
127.
127.
128.
129.
157.
160.
160.
158.
156.
155.
153.
152.
153.
154.
155.
155.
157.
158.
159.
159.
160.
156.
155.
154.
153.
153.
151.
151.
154.
155.
155.
156.
156.
155.
156.
157.
158.
157.
157.
172.
173.
174.
174.
174.
174.
173.
166.
169.
171.
171.
174.
173.
87.
88.
88.
87.
86|
84.
84.
84.
85.
85.
86.
86.
87.
88.
88.
88.
86.
85.
85.
84.
84.
83.
83.
85.
86.
86.
86.
86.
86.
86,
87.
87.
87.
87.
95.
95.
96.
96.
96.
96.
95.
93.
93.
94.
94.
«6|
«*
*
**
**
**
**
**
**
»*
**
*«
*«
**
**
»*
*
**
*
**
**
**
**
**
**
**
**
»*
**
**
**
**
**
**
*
**
**
*
**
«*
**
**
**
**
**
»«
*»
**
*
***************************************************************
129 KVB 6017-1216
-------
I**********
* is WIN. DATA *«
DRY STACK GAS CONCENTRATION *
«« *
** 02 C02 NO NO NO *
LOAD VOLX YOLX PPMV PPMV NG/J *
** DATE TIME HHTK M£AS HEAS HEAS 3X02 **
********»*****»***********»*******««««««**«««
** 3/22/79
»* 3/22/79
* 3/22/79
* 3/22/79
** 3/22/79
3/22/79
** 3/22/79
* 3/22/79
* 3/22/79
« 3/22/79
* 3/22/79
3/22/79
3/22/79
** 3/22/79
* 3/22/79
* 3/22/79
*« 3/22/79
* 3/22/79
** 3/22/79
* 3/22/79
» 3/22/79
* 3/22/79
*« 3/22/79
** 3/22/79
** 3/22/79
** 3/22/79
«* 3/22/79
** 3/22/79
** 3/22/79
*« 3/22/79
** 3/22/79
** 3/22/79
* 3/22/79
«* 3/22/79
** 3/22/79
3/22/79
* 3/22/79
3/22/79
** 3/22/79
* 3/22/79
** 3/22/79
»* 3/22/79
* 3/22/79
** 3/22/79
«* 3/22/79
» 3/22/79
** 3/22/79
» 3/22/79
1215
1230
1245
1300
131S
1330
1345
1*00
14tS
1430
1445
tsoo
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
16,
16.
16,
16,
16.
16.
16.
1*.
I*.
1*.
1*.
1*.
1*.
1*.
1*.
1*.
1*.
1*.
1*.
1*.
1*.
1*.
1*.
1*.
1*.
1*.
1*1
1*.
I*;
!'.
i?:
i7.
i*.
i*.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
1**
16.
16.
7.6
7.6
7.6
7.6
7.6
7.6
7.5
7.5
7.5
7.5
7.
7.
7.
7.
7.
7.
7.
7.
T.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
8.2
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
10. (
10. (
10. e
10.
10.
10.
10.
10.
10.
10.
10.
10.
to.
10.
10.
10.
10.
10. i
10. i
10. i
10.;
10.
10.1
10.1
10.1
10. ;
io.j
10.;
10.;
O
10.
10.
»o.
10.
10.
10.
10.
10.
10.
10.
10.
10.
10.
10.
10.
10.
10.
10.
1 12*.
> 129.
1 124.
125.
127.
127.
127,
127.
128.
128.
' 125.
122.
122.
122.
122.
122.
122.
J 123.
! 124.
> 124.
! 124.
126.
L 128.
1 129.
I 130,
! 129.
! 128.
> 128.
» 126.
> 130.
1 123.
121.
121,
120.
121.
121.
120.
119.
120.
119.
119.
119.
119.
II"*.
119.
116.
116.
116.
173.
173.
167.
168.
170.
170.
170.
169.
171.
171.
167.
163.
1*2.
1*2.
162.
162.
1*3.
1*4.
1*5.
1*5.
166.
168.
170.
172.
174.
»73.
171.
171.
168.
1«.
1*7.
1*«.
163.
163.
164.
163.
163.
162.
162.
162.
162.
162.
162.
162.
!6t.
158.
157.
158.
"6,
96.
92.
"3.
94.
90.
94.
93.
94.
94.
'2.
90.
90.
89.
89.
89.
90.
90.
91.
91.
91.
93.
94.
95.
96.
95.
94.
94.
93.
101.
92.
91.
90.
90.
90.
90.
90.
89.
89.
89.
90.
89.
90.
89.
89.
87.
86.
87.
**
*«
«
**
**
«*
«»
**
**
**
**
«
**
**
**
**
**
**
**
**
**
**
**
*«
**
*«
**
**
**
»*
»
*
**
**
**
**
**
**
**
«
*
**
*
*
*
*
ft*
ft**********************************ft*********************»***
130
KVB 6017-1216
-------
a***********************************************************
** j5 "IN. DATA **
DRY STACK GAS CONCENTRATION
*
*
*
»* DATE
************
** 3/23/79
«* 3/23/79
«* 3/23/79
** 3/23/79
»* 3/23/79
* 3/23/79
»* 3/23/79
** 3/23/79
« 3/23/79
3/23/79
* 3/23/79
»* 3/23/79
*« 3/23/79
** 3/23/79
** 3/23/79
* 3/23/79
« 3/23/79
** 3/23/79
* 3/23/79
** 3/23/79
* 3/23/79
** 3/23/79
** 3/23/79
** 3/23/79
*« 3/23/79
*« 3/23/79
* 3/23/79
»* 3/23/79
** 3/23/79
«* 3/23/79
** 3/23/79
«* 3/23/79
* 3/23/79
** 3/23/79
* 3/23/79
«« 3/23/79
* 3/23/79
* 3/23/79
* 3/23/79
** 3/23/79
* 3/23/79
3/23/79
* 3/23/79
** 3/23/79
** 3/23/79
** 3/23/79
»« 3/23/79
»* 3/23/79
TIME
******]
15
30
45
too
us
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
945
1000
1015
1030
1045
1100
HIS
1130
1145
1200
LOAD
MWTH
*******
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16,4
16.4
16.4
16.4
16,4
16.4
16.4
16.4
16.3
16.3
16,3
16.3
16.4
16.4
l'6.4
16,4
16,4
16,4
16,4
16.4
16.4
16.4
16.4
16.4
16.3
16.3
16.3
16.3
16.3
16^3
16.3
16.3
16.3
16.3
16.3
16.1
16.1
16.1
16.1
02
VOLZ
MEAS
*******
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
8.8
7.7
7.6
7.6
7.6
7.6
7.6
7.6
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7,7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.6
7,6
7.6
7.4
7.4
7.2
7.1
7.2
C02
VOLX
MEAS
*******
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
to.i
10.1
10.1
9.3
10.1
10.2
10.2
10.2
10.2
10.2
10.2
10.1
10. 1
10.1
10.1
10.1
10. 1
10.1
10.1
10.1
10.1
10.1
10,1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.2
10.1
10.2
10,3
10.3
NO
PPMV
MEAS
*******
us.
116.
US.
US.
us.
us.
115.
US.
115.
US.
114,
114.
113.
112.
111.
111.
101.
107.
107.
107,
106.
106.
106.
106.
108.
109.
108.
109.
109.
109.
109.
109.
uo.
112,
112,
111.
112,
112,
us.
115.
116.
114,
us.
126.
128.
129.
131.
134.
NO
PPMV
jxo<:
***++**
W W " W W*
156.
157.
156.
156.
156.
156.
156.
157.
157.
157.
155.
155.
154.
152.
151.
150.
149.
145.
145.
144.
143.
143.
143.
143.
147.
J47,
147,
148.
148,
147.
148.
148.
150.
152.
152.
151.
152,
152,
156.
155.
156.
154.
155.
168.
169.
169.
171.
175.
NO
NG/J
*******
86.
87.
86.
86.
86.
86,
86.
86.
86.
86.
86.
85.
85,
84.
83.
83.
82.
80.
80.
79.
79.
79.
79.
79.
81.
81.
81.
81.
81.
81.
82.
82,
83.
84.
84,
83.
84.
84,
86.
86.
86.
85.
86.
"2.
93,
"3.
94.
97.
**
**
**
**
***
**
«*
**
**
**
**
**
**
**
«*
**
**
*»
*»
**
**
*
**
**
**
**
**
**
**
**
**
*«
*
**
«»
**
**
**
**
**
**
**
**
«*
**
**
**
**
**
**
**
*«
**
131
KVB 6017-1216
-------
ft*************************************************************
** is HIM. °*T* **
*« DRY STACK GAS CONCENTRATION
* **
** 02 COS NO NO NO *«
* LOAD VOLX VOUX PPMV PPMV N6/J *
» DATE TIME M*TH HEAS HEAS MEAS 3102 **
A*************************************************************
** 3/23/79
* 5/23/79
** 3/23/79
** 3/23/79
3/23/79
3/23/79
* 3/23/79
»* 3/23/79
** 3/23/79
** 3/23/79
»* 3/23/79
** 3/23/79
** 3/23/79
* 3/23/79
3/23/79
* 3/23/79
* 3/23/79
* 3/23/79
** 3/23/79
** 3/23/79
** 3/23/79
** 3/23/79
** 3/23/79
* 3/23/79
** 3/23/79
*« 3/23/79
« 3/23/79
« 3/23/79
** 3/23/79
3/23/79
* 3/23/79
** 3/23/79
** 3/23/79
«* 3/23/79
* 3/23/79
** 3/23/79
3/23/79
* 3/23/79
* 3/23/79
* 3/23/79
* 3/23/79
** 3/23/79
*« 3/23/79
3/23/79
** 3/23/79
* 3/23/79
* 3/23/79
»* 3/23/79
12|5
1230
120S
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1930
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
.2200
2215
2230
2245
2300
2315
2330
2345
2400
16.7
16.7
16.7
16.7
16.8
16,8
16.8
16.8
1*.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.6
16.6
16,6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16,6
1*.*
1*.7
16.7
16.7
16,7
16.6
16.6
16.6
16,6
16,6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
7.2
7.«
7.3
7.3
7.J
7.i
7.J
7.J
7.i
T.i
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.'
a.,
7.<
8.
8.
a.
7.
7.
8.
7.
7.
7.
7.
7.
7.
7.
8.
7.
8.
7.
10.3
10.2
I 10.2
1 10.2
! 10.3
! 10.2
! 10.3
10.3
! 10.3
! 10.3
10.3
10.4
10.3
10.3
10.3
10.4
10.3
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.1
10.2
10.2
10.2
r 9,9
! 9.6
» 9.7
) 9.7
> 9,7
» 9.7
9.7
9.7
9.7
9.7
9.7
9.7
9.7
9.7
9.7
9.7
9 9.7
9 9,7
0 9,7
9 9,7
135.
134.
124.
124.
125.
129.
130.
129.
128.
127.
126.
125.
124,
123.
124.
122.
123.
122.
122.
121.
121.
120.
120.
119.
118.
118.
117.
118.
11*.
124.
124.
124.
126.
125.
124.
122.
121.
122.
123.
123.
123.
124.
123.
123.
126.
126.
126.
126.
177.
176.
163.
163.
164.
169,
170.
168,
168,
166.
164.
163.
162.
160.
161.
159.
162.
162.
162.
159.
160.
158.
159.
157.
156.
156.
154.
156,
158.
174.
172.
172.
170.
173.
171.
169.
168.
169.
170.
170.
170.
171.
170.
169.
174.
174.
174.
173.
97.
97.
90.
90.
90.
93.
94,
'3.
"2.
91.
90.
90.
89.
88.
99.
88.
89.
89.
89.
88.
88.
87.
87.
87.
86.
86.
85,
86.
87.
96.
95.
95.
96.
95.
94.
93.
93.
93.
94.
94.
94.
94.
94.
93.
96.
96.
96.
96.
**
*
*
*
«
*
*
«
*
**
**
**
**
*
*«
**
*
**
*
»*
**
»*
»*
»*
*
»
*»
**
**
**
*
*
**
**
**
**
**
**
**
**
*«
it*
*
**
**
**
A*************************************************************
132
KVB 6017-1216
-------
**
*«
*
ft*
*
** DATE
15 MIN. DAT*
DRY 9T»CK GAS CONCENTRATION
TIME
LOAD
HHTH
02
VOLX
MEAS
C02
VOLX
MEA3
NO
PPHV
HEAS
NO
PPMV
3XO"
NO
NG/J
ft
*
**
*«
**
*
*******«*»»«»«««***<»************«**
* 3/24/79
** 3/24/79
* 3/24/79
« 3/24/79
** 3/24/79
** 3/24/79
* 3/2«/79
** 3/24/79
ft* 3/24/79
ft* 3/24/79
ft* 3/24/79
*« 3/24/79
ft* 3/24/79
ft* 3/24/79
ft* 3/24/79
ft* 3/24/79
ft* 3/24/79
« 3/24/79
ft* 3/24/79
ft* 3/24/79
ft* 3/24/79
** 3/24/79
»* 3/24/79
* 3/24/79
* 3/24/79 '
* 3/24/79
ft* 3/24/79
** 3/24/79
ft* 3/24/79
ft* 3/24/79
ft* 3/24/79
ft* 3/24/79
ft* 3/24/79
ft* 3/24/79
ft* 3/24/79
ft* 3/24/79
* 3/24/79
** 3/24/79
*« 3/24/79
ft* 3/24/79
ft* 3/24/79
ft* 3/24/79
« 3/24/79
ft* 3/24/79
3/24/79
ft* 3/24/79
ft* 3/24/79
* 3/24/79
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
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16,4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.3
16.3
16.3
16.3
7.9
7.9
7.9
7.9
7.9
7.9
7.8
7.9
7.9
7.9
7.9
7.8
7.9
7.9
7.9
7.9
8.5
7.9
7.7
7.7
7.6
7.7
7.6
7.7
7.6
7.7
7.7
7.7
7.7
7.7
7.6
7.6
7.6
7.6
7.7
7.7
7.6
7.6
7.7
7.7
7.8
7.8
7.8
7.8
7.8
7.8
7.8
7.8
9.7
9.7
9.7
9.7
9.7
9.7
9.7
9.9
9.7
'.7
'.7
'.7
9.7
9.7
9.7
9.7
9.1
9.6
9,8
9.9
9.9
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-.8
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t
9.
9.
9.
9.
9.
9.9
9.9
9.9
10.0
9.9
9.9
10.0
9.8
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.7
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.7
.7
.7
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9.7
9.7
125.
124,
125.
125.
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124.
124.
124.
125,
125.
126.
127.
129.
129.
128,
128.
129.
127.
128.
128.
127.
126.
126.
126.
127,
127,
126.
126.
126.
127,
128.
128,
128,
127.
125,
121.
116.
116.
120.
123.
124.
125.
125.
125.
125.
127.
126.
125.
173.
172.
173.
172.
170.
170.
170,
170.
171.
171.
174.
174.
178.
178.
177.
177.
187.
175.
173.
173.
172.
171.
171.
171.
171.
172.
171.
171.
172.
172.
173.
173.
173.
171.
169.
163.
156.
157.
163.
167.
169.
171.
171.
171.
172.
174.
173.
171.
95.
95.
95.
95.
94.
9«,
94.
94.
94.
95.
96.
96.
98.
98.
97.
98.
103.
97.
95.
95.
95.
94.
94..
94.
94.
95.
94.
94.
95.
95.
95.
95.
95.
94.
93.
90.
86.
87.
90.
92.
93,
94.
94.
94.
95.
96.
95.
95.
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*
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*
*
133
KVB 6017-1216
-------
ft**************************************************************
»* (5 «IN. DATA *
** DRY STACK GAS CONCENTRATION **
**
*«
* 02 C02 NO NO NU **
»* LOAD VOLX VOLX PPMV PPMV N6/J *
* DATE TIME HMTH MEAS HEAS MEAS jZOf *«
ft***********************************************************
*
*»
*«
**
ft*
««
*
**
*
**
**
**
*
**
**
**
**
*
ft*
ft*
**
»*
*
*
ft*
ft*
ft*
*
*
ft*
**
0*
ft*
*
««
*
ft*
ft*
*
*
**
*
**
ft*
«*
ft*
ft*
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
3/24/79
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1SOO
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1900
1815
1830
1845
19QO
1915
1930
19«5
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
16.3
16.3
16.3
16.3 1
16.
16. 1
10.
1*. 1
1*. 1
1*. 1
16. 1
16. 1
16. 1
1*.
16. 1
16.1 1
16.1 1
16.1 1
16.1 1
16.1 1
16.3 1
16.3 1
16.3
16.3 1
16.3
16.3 1
16.3
16.3
18.2
1«.2 «
18*2
1«.2
16.4
16.
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1*.
1*.
1*.
1*.
1*.
16.
16.
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16.
16.4
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r 127.
1 127.
r 126.
r 127,
r 133.
» 132.
9 131.
130.
132.
132.
132.
13«.
135.
135.
135.
135.
136.
136.
138.
138.
138.
137.
136.
137.
135.
135.
134.
132.
) 158.
t 181.
t 181.
I 182.
r 147.
136.
136.
136.
135.
135.
137.
137.
r i37.
r i39.
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b 141.
r i«2.
r 140.
!> 141.
» 141,
17«.
174.
172.
17«.
182.
181.
180.
178.
180.
180.
180.
182.
185.
185.
185.
184.
186.
187.
189.
189.
189.
187.
187.
188.
186.
186.
186.
183.
217.
263.
263.
265.
207.
193.
1*2.
1*2.
1*2.
192.
194.
1*4.
1*5.
1*7.
197.
200.
201,
198.
1*9.
200.
"6.
96.
95.
96.
101.
too.
99.
98,
99.
99.
99.
101.
102.
102.
102.
102.
103.
103.
104.
104.
104.
103.
103.
104.
103.
103.
102.
tot.
119.
145.
145.
146.
114.
106.
106.
106.
106.
106.
107.
107.
107.
109.
109.
110.
111.
109.
110.
110.
**
**
**
**
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**
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134
X7B 6017-1216
-------
*************«******»************«********»*****»***
** j5 "IN. DATA **
** DRY 3TACK GAS CONCENTRATION **
* **
* 02 C02 NO NO NO *
** LOAD VOLX VOLI PPMV PPMV NG/J *
* DATE TIME MHTH MEA3 MEA3 MEA3 Jl0
-------
ft*********************** ft ********* *************** ft ft* ft ****** *ft*ft
*
*
**
ft*
** DATE
ft***********
** 3/25/79
** 3/25/79
* 3/25/79
* 3/25/79
« 3/25/79
** 3/25/79
* 3/25/79
* 3/25/79
** 3/25/79
3/25/79
* 3/25/79
3/25/79
* 3/25/79
3/25/79
« 3/25/79
* 3/25/79
*« 3/25/79
* 3/25/79
*« 3/25/79
3/25/79
*« 3/25/79
*« 3/25/79
* 3/25/79
*« 3/25/79
* 3/25/79
* 3/25/79
** 3/25/79
* 3/25/79
*« 3/25/79
*« 3/25/79
*« 3/25/79
* 3/25/79
ft* 3/25/79
«* 3/25/79
** 3/25/79
*« 3/25/79
** 3/25/79
** 3/25/79
* 3/25/79
** 3/25/79
« 3/25/79
** 3/25/79
* 3/25/79
** 3/25/79
* 3/25/79
** 3/25/79
* 3/25/79
* 3/25/79
15 MIN. DATA
ORt STACK GAS CONCENTRATION
TIME
02 C02
LOAD VOtX VOL*
HNTH MEAS MEAS
NO
PPMV
MEAS
NO
PPMV
3*0?
NO
NG/J
*«
*
**
**
**
*
A************************************************
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
16.1
16.1
16,1
16.1
16.1
16.1
16.1
16,1
16,3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
1*!3
16.1
16,1
16.1
16,1
16.4
16.4
16.4
16.4
16.4
16.4
16,4
16,4
16.4
16.4
16,4
16,4
16.4
16.4
16.4
16.4
7 9.5
7 9.5
7
7
7
7
5
3
4
.4
.4
.4
.4
.4
.4
.3
.4
.4
.4
.4
.4
.5
.5
.5
.5
.5
_
e
. ~
5
.2
2
i
^
2
.5
.5
.5
.5
.5
.5
.4
.4
,4
.4
.4
.5
.5
.5
.5
.5
.5
.5
.5
.5
.5
.5
.5
.5
.5
.5
.5
14
.7
.8
.8
.8
.8
.2 9.8
.2 9.8
.2 .8
.2 .8
.2 .7
.2 .7
.2 .7
.2 .7
.2 .7
.1 .7
.1 9.7
.1 9,7
134.
134.
134,
133.
133.
133.
135.
138,
136.
136.
135.
136.
137.
138.
138.
139.
}40.
139.
137.
137.
137.
138.
138.
138.
138.
136.
136,
136.
135.
134.
132.
132.
130.
131.
131.
130.
130.
131.
132.
133.
132.
130.
130.
130.
132.
133.
135.
135.
197.
197.
197.
195.
195.
195.
196.
196.
196,
196.
194.
196,
197.
198,
197.
198.
199.
199.
197,
197.
196.
199.
198.
198.
198.
196.
1*5.
195.
194,
194,
192.
186.
184.
183.
185.
184.
183.
184.
186.
187.
187.
183.
183.
184.
186.
187.
189.
189.
106.
109,
109,
107.
107.
107.
108.
108.
108.
108.
107.
108.
108.
109,
109,
109.
110.
110.
109,
108.
108,
110.
109,
109,
109,
108.
108,
108,
107.
107.
106,
103.
101.
101.
102.
101.
101.
102.
103.
103.
103.
101.
101.
101.
103.
103.
104,
104.
**
*
*
**
**
*
**
**
*
**
**
**
*
**
*
**
*
**
**
ft*
**
**
**
**
**
**
**
ft*
**
**
«*
**
*
*
*
**
*
**
*
**
**
**
**
*
**
**«******«********«************«*******
136
KVB 6017-1216
-------
ft********************************* **************************£
*
**
«*
*
*
15 HIM, DATA
DRY STACK GAS CONCENTRATION
DATE
TIME
02 C02
LOAD VOL I VOLX
MHTH MEA3 MEA3
NO
PPMV
MEA3
NO
PPMV
3*02
NO
NG/J
»*
**
»*
**
**
**
****************** A********************************* * **********
**
**
**
**
**
**
«
**
**
**
*
*
*«
*
*
**
**
*
«*
*«
*
**
**
*
**
**
**
**
*
**
**
**
**
»*
»*
*
**
**
**
**
*
**
**,
**
**
**
*»1
5/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
3/26/79
»********i
15
30
45
100
115
130
las
200
215
230
245
300
315
330
345
400
015
030
aas
500
515
530
5«5
600
615
630
645
700
715
730
745
800
815
830
845
900
"15
930
9«5
1000
1015
1030
1045
1100
1115
1130
1145
1200
»«**»*
16. a 8.1 9.7
16.4 8.1 Q.7
16.4 8.1 9.7
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
1*.
16.
16.
16.
I*.
16.
16.
16.
16.
16.
I*.
1*.
I*.
1*.
1*.
1*.
1*.
1*.
1*.
1*.
1*.
8.1 9.7
8.1 9.7
8.1 9.7
8.1 9.6
8.1
8.1
8.1
8.1
8.1
8.1
8.1
8.1
8.1
9.1
8.7
8.7
8.7
8.5
8.5
8.5
8.5
8.4
8.3
«.3
8.3
8.3
8.3
8.3
8.2
8.3
8.3
8.3
8.3
16.3 8.3
16.3 .2
16.3 .0
16.3 .1
16.1 .6
16.1 .5
16.1 .2
16.1 .1
16.3 8.0
16.3 8.0
16.3 8.Q
16.3 8.1
.6
.7
.7
.7
.7
.7
.7
.7
.7
.8
,3
.3
.3
.«
.5
.5
.5
.5
.7
.7
.7
.7
.7
.7
.7
.7
.7
.7
.7
.7
.7
.7
.7
,5
.4
.6
.7
.7
.7
.8
.8
ft*********************
137.
137.
139.
140,
141.
141.
139.
139.
140.
140.
140.
140.
140.
140.
139.
139.
143.
143.
144.
1«6,
144,
144,
144.
144,
144.
141.
Ifl2,
1«2,
1«2.
142.
Ifl2.
1«3.
1«3.
142,
143.
144.
144.
139.
133.
132.
128.
129.
129.
131.
132.
136.
137.
137.
*******
192.
192.
195.
1<»7.
198.
198.
195.
195.
196.
197.
196.
197.
196,
196,
195,
195.
217.
211.
212.
214.
209.
207.
208.
207.
206.
200.
202.
202.
201.
201.
202.
203.
203.
202.
203.
205.
205.
1*6,
185.
184.
186.
186.
181.
183.
183.
189.
190.
192.
******
106.
106.
108,
109,
109,
109,
108,
108.
108.
108.
108,
109.
108.
108.
107.
108.
120.
116.
117.
118.
115.
114.
115.
114.
114.
110.
111.
112.
111.
1U.
111.
112.
112.
111.
112.
113.
113.
108.
102.
101.
103.
103.
100.
101.
101.
104.
105.
106.
*******
**
**
**
**
*«
**
**
**
**
**
**
**
**
**
**
*
**
**
**
**
**
*
**
**
**
*
**
**
**
**
**
**
**
**
*
*
**
**
**
**
**
**
**
**
**
**
**
****
137
KVB 6017-1216
-------
**
'ft*********************************
15 MIN. DATA **
DRY STACK CAS CONCENTRATION *«
ft*
**
ft*
DATE
***** ******!
** 3/26/79
»* 3/26/79
3/26/79
* 3/26/79
» 3/26/79
* 3/26/79
* 3/26/79
3/26/79
* 3/26/79
* 3/26/79
3/26/79
3/26/79
3/26/79
*« 3/26/79
3/26/79
* 3/26/79
** 3/26/79
3/26/79
** 3/26/79
ft* 3/26/79
« 3/26/79
** 3/26/79
** 3/26/79
« 3/26/79
ft* 3/26/79
* 3/26/79
*« 3/26/79
** 3/26/79
ft* 3/26/79
»* 3/26/79
* 3/26/79
ft* 3/26/79
* 3/26/79
3/26/79
* 3/26/79
ft* 3/26/79
* 3/26/79
ft* 3/26/79
3/26/79
3/26/79
* 3/26/79
3/26/79
« 3/26/79
* 3/26/79
* 3/26/79
ft 3/26/79
** 3/26/79
** 3/26/79
TIMC
r** A* A A
W W W W W W
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
19QO
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAI
MWTt
** ** '
JO.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
»6.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.'
16.'
16.'
16.
16. t
16. J
16. i
16.'
02
) VOU
* ME*:
t * *****'
B.<
.(
.(
.(
.(
.
.(
.(
7.<
7.«
7.«
7.!
7.(
7."
7,<
7.<
7.!
7.«
7.«
7.1
7*i
*
7
'
*
7.
7.
7
'
7.
8.
7
* *
7.
7.
7.
7.
7.
7.
7.
7.
r 7.
r 7.«
r 7.«
r 7.<
1 7."
1 7.'
I 7.'
1 7.'
C02
i van
i NEA3
t********1
> .6
> .8
) .8
) .9
> .9
.8
) .7
1 .7
> 9.9
i 10.1
5 10.
> 10.
> to.
> to.
> 10.
i 10.
> 10.
> 10.
> 10.
5 10.
5 10.2
! 10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10,2
*.«
10. 0
10.1
10.2
10.3
10.4
10.5
10.1
10.
10.
10.
> 10.
i 10.
> 10.
' 10.
' 10.3
r 10.3
' 10.3
NO
PPMV
MEA3
'******!
137.
137.
137.
128.
121.
128.
135.
139.
133.
127.
127.
128.
127.
128.
129.
129.
127.
126.
123.
126.
125.
125.
126.
125,
124,
123.
121.
120*
123.
125.
123.
123.
122.
120.
118.
119.
121.
121.
120.
119.
120.
118.
118.
119.
120.
119.
119.
NO
PPHV
3*02
********
191.
190.
190.
178.
168.
180.
189.
193.
180.
169.
1/0.
172.
170.
171.
173.
I7ol
168.
164.
169.
167.
168.
168.
167.
166.
165.
162.
158.
161.
166.
184.
169.
168.
165.
161.
157.
161.
166.
165.
165.
160.
161.
158.
159.
161.
162.
161.
161.
NO
NG/J
kftftftftft ft 1
105.
105,
105.
98,
93,
99,
100.
106.
99.
93,
94,
95.
94,
94,
96,
96.
9***
ft*
**
ft*
*«
*
**
ft*
*
*
*
**
*
ft*
**
*
*
*
*
**
ft*
**
ft*
*
**
ft*
**
**
ft*
**
**
««.
**
**
ft*
**
ft*
**
**
**
ft*
*
**
**
**
**
«
ft**************************************************************
138
KVB 6017-1216
-------
**««*»**««**»«**«****«*«***»****************«*****««****
*
**
*»
**
ft
** DATE
mi**********
** 3/27/79
** 3/27/79
** 3/27/79
** 3/27/79
* 3/27/79
* 3/27/79
»* 3/27/79
3/27/79
** 3/27/79
** 3/27/79
* 3/27/79
3/27/79
* 3/27/79
* 3/27/79
« 3/27/79
* 3/27/79
3/27/79
* 3/27/79
** 3/27/79
** 3/27/79
* 3/27/71
*« 3/27/79
** 3/27/79
* 3/27/79
« 3/27/79
» 3/27/79
*« 3/27/79
** 3/27/79
* 3/27/79
** 3/27/79
3/27/79
« 3/27/79
** 3/27/79
** 3/27/79
** 3/27/79
* 3/27/79
* 3/27/79
« 3/27/79
** 3/27/79
* 3/27/79
** 3/27/79
«* 3/27/79
** 3/27/79
* 3/27/79
** 3/27/79
* 3/27/79
** 3/27/79
* 3/27/79
15 HIN
DRY STACK GAS
TIME
****** t
IS
30
as
100
115
130
145
200
215
230
2a5
300
315
330
S«5
000
415
030
045
500
515
530
545
600
615
630
645
700
715
730
745
800
815
830
845
900
-------
**
**
*
**
** DATE
l5 HIN
DRY STACK GAS
TIME
LOAD
M*TH
02
VOL*
MEA3
. DATA
CONCENTRATION
C02
VOLX
MEAS
NO
PPMV
MEAS
NO
PPMV
3X02
NO
HG/J
*
**
**
*
*
*********************«*****************«************
* 3/27/79
* 3/27/79
3/27/79
* 3/27/79
3/27/79
** 3/27/79
3/27/79
3/27/79
** 3/27/79
* 3/27/79
3/27/79
3/27/79
3/27/79
* 3/27/79
** 3/27/79
** 3/27/79
» 3/27/79
* 3/27/79
3/27/79
* 3/27/79
3/27/79
* 3/27/79
3/27/79
** 3/27/79
* 3/27/79
** 3/27/79
* 3/27/79
»* 3/27/79
« 3/27/79
*« 3/27/79
» 3/27/79
* 3/27/79
* 3/27/79
3/27/79
* 3/27/79
* 3/27/79
3/27/79
* 3/27/79
« 3/27/79
t« 3/27/79
3/27/79
»« 3/27/79
* 3/27/79
« 3/27/79
* 3/27/79
3/27/79
* 3/27/79
* 3/27/79
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
16.6
16.6
16.6
16.6
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.6
16.6
16.6
16.6
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16.7
16,6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
7.9
7.9
7.9
7.8
7.7
7.7
7.8
7.9
.1
.2
.2
.1
.1
7.9
7.7
7.6
7.6
7.6
7.6
7.7
7.7
7.7
7.7
7.6
7.7
7.7
8.0
8.0
7.9
8.1
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
10.3
10.3
10.3
10.4
10.4
10.4
10.4
10.4
10.4
10.3
10.3
10.3
10.4
10.4
10.4
10.4
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.2
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.5
10.5
10.4
118.
119.
1 !'
118.
116.
116.
117.
114.
104.
97.
96.
97.
98.
102.
107.
110.
111.
111.
111.
110.
no.
106^
109.
109.
109.
109.
108.
107.
108.
108.
109,
109,
109.
108.
107.
107.
107.
106.
105.
105.
106.
108.
108.
107.
106.
106.
106.
163.
163.
164.
162.
158.
158.
160.
158.
146.
136.
135.
136.
137.
14 t .
145.
148.
149.
150.
150.
150.
150.
148,
144.
147.
148.
148.
151.
150.
148.
151.
149.
150.
150.
150.
149.
148.
148.
148.
146.
144.
145.
146.
149.
149.
148.
147.
147.
147.
90.
90,
90.
89.
87.
87.
88.
87.
80.
75.
75.
75.
76.
78.
80.
82.
82.
82.
83.
82.
82.
92.
79.
81.
82.
82.
83.
82.
81.
83.
82.
83.
83.
83.
82.
81.
82.
81.
81.
80.
80.
81.
82.
82.
81.
81.
81.
81.
**
**
**
*
*»
*
*
**
**
*
**
*
*
*
**
**
**
**
**
*
**
*
**
»«
*«
*
»
**
**
**
*
*
*
**
*
**
**
*«
*
*
**
*
*
**
*
*****«««*«*«*«******************************
140
KVB 6017-1216
-------
ft************************
** 15 *IN
* DRY STACK GA3
*»
*
*«
** DATE
TI*E
LOAD
MNTH
02
VOLX
MEA3
A***************************
. DATA
CONCENTRATION
C02
VOLX
MEAS
NO
PPMV
HEAS
NO
PPMV
3X02
NO
NG/J
***
*
**
**
**
**
**
a**************************************************************
* 3/28/79
** 3/28/79
** 3/28/79
** 3/28/79
** 3/28/79
* 3/28/79
3/28/79
* 3/28/79
** 3/28/79
3/28/79
** 3/28/79
* 3/28/79
** 3/28/79
* 3/28/79
* 3/28/79
** 3/28/79
* 3/28/79
3/28/79
* 3/28/79
** 3/28/79
** 3/28/79
* 3/28/79
** 3/28/79
* 3/28/79
** 3/28/79
*« 3/28/79
** 3/28/79
« 3/28/79
* 3/28/79
** 3/28/79
*« 3/28/79
»* 3/28/79
»* 3/28/79
*« 3/28/79
** 3/28/79
* 3/28/79
** 3/28/79
* 3/28/79
** 3/28/79
** 3/28/79
** 3/28/79
« 3/28/79
* 3/28/79
** 3/28/79
** 3/28/79
*« 3/28/79
*« 3/28/79
** 3/28/79
15
30
as
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
9QO
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.7
1*.7
1«>.7
10.7
16.7
1*.7
1».7
16.7
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16,6
16.6
16.6
1<».4
16.4
16.4
16,4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16,4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
8.6
8.1
8.1
8.1
8.1
8.1
8.1
8.1
8.1
8.1
8.1
8.1
8.1
a.i
8.0
8.0
8.1
8.1
8.1
8.1
8.1
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
10.4
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10,5
10.5
10.5
10.5
10.5
10.5
10.6
10.6
10.2
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.
10.
10.
10.
10.
10.
10.
to.
10.
10.4
10.4
106.
105.
105.
106,
106.
104.
104.
104.
104.
104.
103.
102.
101.
101.
100.
99.
107.
102.
100.
101.
101.
101.
101.
100.
100.
99.
100.
t°l.
102.
103.
103.
104.
104.
10«.
104.
105.
106,
130.
130.
130.
130.
131.
131.
132.
132.
131.
131.
131.
146.
14S.
1«5.
147.
1«7.
144.
144.
1«3.
143.
144.
1«3.
1«1.
140.
139.
139.
138.
156.
143.
140.
141.
141.
141.
141.
140.
140.
139.
141.
141.
142.
1«3.
144.
145.
145.
146.
146.
146.
148.
178.
179.
180.
180.
181.
181.
183.
183.
181.
180.
181.
81.
80.
80.
81.
81.
79.
7".
79.
79.
79.
79.
78.
77.
77.
76.
76.
86.
79.
77.
78.
78.
78.
78.
77.
77.
77.
77.
78.
78.
7".
79.
80.
60.
80.
81.
81.
82.
98.
99.
99.
99.
100.
100.
101.
101.
100.
99.
100.
**
*
**
**
**
**
*
*
ft*
*«
**
**
»*
**
**
**
»«
**
*
**
**
**
**
**
**
*
ft*
**
ft*
**
**
ft*
ft*
**
**
**
**
ft*
**
**
**
**
ft*
**
**
*«
**
ft**************************************************************
141
KVB 6017-1216
-------
ft**************************************************************
* 15 MN, DATA »
**
*
*«
**
**
DRY STACK GAS CONCENTRATION
02
C02
LOAD VOLX VOL*
DATE
TIME
M«TH M£A3
MEAS
NO
PPMV
MEAS
NO NO
PPNV NG/J
3X02
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*
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
3/28/79
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1815
1830
1845
1900
1915
1930
19«5
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
(6.6 7.9 10.4
16.6 7.9 10.4
16.6 7.9 10.4
16,6 7.7 10.4
16,6 7.7 10.4
16.6 7.7 10.5
16.6 7.7 10.4
16.6 7.7 10.4
16.6 7.7 10,4
16.6 7.7 10,4
16.6 7.7 10. a
16.6 7.7 10.4
16.6 7.7 10.4
16,6 7,7 10,4
16,6 7.7 10.4
16,6 7,7 10,4
132.
131.
130.
131.
132.
133.
133.
134.
132.
132.
132.
182.
177.
178.
176.
177.
16,6 7.5 10,2
16.6 7.4 10.5
16.6 7.6 10.3
16.6 7,6 10,3
16,6 7.7 10.3
16.6 7,7 10,3
16.6 7.7 10.3
16.6 7.
16.6 7,
16.6 7.
16.6 7.
16.6 7.
16.6 7.
16.6 8.
16.6 7.
16.6 7.
16.7 7.
16.7 7.
16,7 7.
16.7 7.
16.7 7.
16.7 7.
16.7 7.
16.7 7.
10.3
10.3
10.3
10.3
10.3
10.3
10.1
10.1
10.1
10.1
10.1
10.1
10.2
10.2
10.2
10.2
10.2
16.6 8.0 10.1
16,6 8.2 10.1
16.6 8.2 10.1
16.6 8.2 10.1
16.7 8.2 10.1
16.7 8.2 10.1
16.7 8.
16.7 8.
1 10.1
1 10.1
«
.
,
.
»
.
.
,
.
.
.
.
,
,
.
.
.
.
.
.
,
,
.
,
.
.
.
.
.
161 10o.
179
178
179
179
iao
161
181
180
100
179
247
240
242
239
2^0
»
V
*
99.
98,
99,
99.
99.
100,
100,
99,
99,
99.
136.
132,
133.
132.
132.
-
-
-
»
.
*
.
.
4
.
.
.
.
.
.
*
,
.
.
.
.
.
,
.
,
.
.
.
.
.
ft**********************************************************
*
*«
**
*
**
«
**
*
*
*
**
**
**
*
**
**
*
**
*
**
**
**
*
. **
**
**
**
*
*
**
**
**
*
*
**
*
*
**
*
**
****
142
KVB 6017-1216
-------
* 15 "IN. OAT*
** DRY STACK GAS CONCENTRATION
ft*
*
*
» DATE
*********<
** 3/29/79
** 3/29/79
** 3/29/79
»* 3/29/79
** 3/29/79
** 3/29/79
** 3/29/79
* 3/29/79
* 3/29/79
*« 3/29/79
« 3/29/79
** 3/29/79
«« 3/29/79
** 3/29/79
** 3/29/79
** 3/29/79
» 3/29/79
** 3/29/79
* 3/29/79
** 3/29/79
* 3/29/79
** 3/29/79
** 3/29/79
** 3/29/79
* 3/29/79
** 3/29/79
** 3/29/79
«* 3/29/79
** 3/29/79
** 3/29/79
»* 3/29/79
** 3/29/79
** 3/29/79
** 3/29/79
* 3/29/79
»* 3/29/79
« 3/29/79
*« 3/29/79
** 3/29/79
*« 3/29/79
** 3/29/79
* 3/29/79
*« 3/29/79
* 3/29/79
* 3/29/79
** 3/29/79
** 3/29/79
* 3/29/79
*******
TIME
i******
15
30
as
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
lots
1030
1045
itoo
1115
1130
1145
1200
******
LOAD
MHTH
******
.8
.8
.8
.8
.7
.7
.7
.7
11.1
11.1
11.1
tl.l
12.0
12.0
12.0
12.0
12.6
12.6
12.6
12.6
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
15.8
15.8
15.8
15.8
10.5
10.5
10.5
to.s
'.7
'.7
".7
'.7
'.7
».7
'.7
'.7
*****«
02
VOLX
MEA3
t* *** *!
8.1
8.1
8.1
8.1
t.O
-t.O
1.0
-1.0
-1.0
-1.0
1.0
-1.0
t.O
8.1
-1.0
"1.0
-1.0
-1.0
1.0
-1.0
-1.0
1.0
-1.0
-t.O
-t.O
8.1
8.1
-1.0
-t.O
8.1
8.1
9.5
10.7
10.4
11.0
11.0
10.7
10.6
10.7
10.7
10.6
10.5
to. a
10.3
10.2
10.4
10.7
-t.O
******
C02
VOLX
MEAS
r*******
10.1
10. t
10.1
10.1
to.i
10.1
10.1
10. t
10.1
10.1
10.1
10.1
10.1
10.0
10.0
10.0
10.1
10.1
10.1
10,1
10.1
10.1
10.1
10.1
10.0
10.1
10.1
10.1
10.0
10.0
10.0
10.0
7.7
8.0
7.7
7.5
7.5
7.5
7.5
7.4
7.«
7.4
7.4
7.4
7.1
7,4
.0
NO
PPHV
MEAS
*******
w * « w
i.
-t.
-i.
i.
i.
i.
-i.
i.
i.
i.
-t.
i.
i.
-t.
-t.
t.
-t.
i.
-i.
-t.
t.
-t.
t.
i.
t.
i.
t.
-t.
t.
-t.
i.
i.
t.
t.
t.
-i.
i.
-i.
-i.
-i.
-i.
i.
-t.
-i.
-i.
-i.
-i.
NO
PPHV
3*0f
***** * *
1.
t.
I.
t.
-t.
-1.
t.
1.
-1.
1.
-1.
1.
-1.
t.
1.
-1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
t .
1.
1.
1.
1.
-1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
ft*
*«
NO
NG/J
*******
-I.
1.
1.
-1.
-1.
1.
1.
-1.
1.
1.
1.
-1.
1.
1.
1.
-1.
1.
1.
1 .
I.
1.
1.
1.
1.
1.
1.
1.
1.
t .
1 .
1 .
1,
1.
1.
1 .
1,
1.
1.
I.
1.
1.
1.
1.
1.
1.
t.
1.
**
**
**
**
***
**
**
ft*
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
A A
H
**
ft*
ft*
*»
**
**
**
ft*
ft*
ft*
ft*
ft*
ft*
7.4 -t. "1. -i. -»
*«**«***«*********»**********"*
143
KVB 6017-1216
-------
ft**************** ******* ft *«*»»*<
ft*
*«
ft*
ft*
ft*
ft* DATE
15 MIC
DRY STACK GAS
LOAD
02
VOLX
TIME MNTH *»EAS
*******
4. DATA
A************************
**
CONCENTRATION *
C02
VOLX
MEA3
ft*************************************
** 3/29/79
* 3/29/79
* 3/29/79
* 3/29/79
** 3/29/79
* 3/29/79
* 3/29/79
ft* 3/29/79
** 3/29/79
3/29/79
ft* 3/29/79
ft* 3/29/79
* 3/29/79
ft* 3/29/79
ft* 3/29/79
** 3/29/79
« 3/29/79
** 3/29/79
* 3/29/79
3/29/79
3/29/79
** 3/29/79
ft* 3/2*/79
* S/2»/79
»* 3/29/79
« 3/2^/79
* 3/29/79
« 3/29/79
** 3/29/79
1215 <
1.7
1230 9.7
1245 9.7
1300
1315
1330
13*5
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
.7
.8 -
.8
.8
.8
.8
.8
.8
.8
.8
.8
.8
.8
.8
.8
.8
.8
1715 10.0
1730 10.0
1745 10.0
1800 10.0
1815 10.0
1830 10.0
1845 10.0
1900 10.0
1915 10.0
3/2*/79 19JO 10.0
** 3/29/79
** 3/29/79
ft* 3/29/79
** 3/29/79
* 3/29/79
* 3/29/79
ft* 3/29/79
** 3/29/79
ft* 3/29/79
** 3/29/79
ft* 3/29/79
ft* 3/29/79
3/29/79
** 3/29/79
*« 3/29/79
3/29/79
3/29/79
3/29/79
******«
1945 10.0
2000 10.0
2015 10.0
2030 10.0
2045 10.0
2100 10.0
2115 10.0
2130 10.0
2145 10.0
2200 10.0
2215
2230
2245
2300
2315
2330
2345
2400
****
9.g
9.8
'.8
'.8
9.7
9!7
9.7
»*««
10.6
10.6
10.6
10.6
-10.6
10.6
10.6
10.7
10.7
10.7
10.6
10.5
10.5
10.6
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.7
11.1
11.2
11.2
11.2
11.2
11.2
11.3
11.3
11.2
11.2
11.2
11.2
11.4
11.2
11.2
11.2
11.3
11.4
11.4
i******
7.5
7.5
7,5
.0
.0
.0
.0
7.5
7.4
7.4
7.5
7.5
7.5
7.5
.0
.0
.0
.0
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.1
7.0
7.0
7.0
7.0
7.0
7.0
7.0
7.0
7.0
7.0
7.0
7.0
7.0
7.0
7.0
7.0
7.0
7.0
****
**
NO NO NO *
PPMV PPHV NG/J **
MEA3 3X02 **
A************************
-1 -1. -I. *
1
-I
"1
1
I
-1
-1
1
1
1
-1
1
I
1
1
1
1
-1
-1
-1
1
-1
1
-1
1
-1
-1
1
4^ A
1
-1
«*
"I
I
I
"1
1
|
I
1
*]
1
I
|
1
1
-1
"I. "1. *
1
1
1
"1
1
I
"1
1
1
-1
1
-I
I
-I
-1
-1
1
-1
"1
1
-1
1
1
1
1
"1
1
1
"1
1
4
4»4
1
1
1
-1
m\
"1
1
1
1
-I
1
-I
1
1
-1. **
1
1
1
1
-1
1
1
"1
I
1
-1
-I
-I
1
-1
1
1
1
-1
1
**
ft*
**
ft*
ft*
*
*
ft
ft*
ft
ft
ft
ft*
ft*
**
**
**
**
ft*
**
1. **
1. **
1
"1
1
-1
1
1
W4
1 4
1
1
1
1
1
1
1
-I
-1
I
"1
1
-I
"1
-1
**
ft*
**
**
ft*
**
*
ft*
ft*
*
**
**
*
**
ft*
ft*
*
*
*
**
*
**
ft*********** **************
144
KVB 6017-1216
-------
****************************************************<
**
**
**
**
*
«* DATE
15 MIN
DRY STACK GAS
TIME
LOAD
MWTH
02
VOLX
. DATA **
CONCENTRATION **
**
C02 NO NO NO *«
VOLX PPMV PPMV NG/J *
MEAS MEAS MEAS 3<02 **
A*************************************************************
** 3/30/79
«* 3/30/79
** 3/30/79
* 3/30/79
** 3/30/79
«* 3/30/79
3/30/79
* 3/30/79
* 3/39/79
»* 3/30/79
3/30/79
** 3/30/79
*« 3/30/79
* 3/30/79
** 3/30/79
** 3/30/79
* 3/30/79
* 3/30/79
* 3/30/79
** 3/30/79
** 3/30/79
* 3/30/79
** 3/30/79
** 3/30/79
** 3/30/79
** 3/30/79
** 3/30/79
*« 3/30/79
3/30/79
«* 3/30/79
*« 3/30/79
** 3/30/79
** 3/30/79
* 3/30/79
3/30/79
»* 3/30/79
3/30/79
« 3/30/79
* 3/30/79
* 3/30/79
* 3/30/79
*« 3/30/79
* 3/30/79
** 3/30/79
* 3/30/79
** 3/30/79
** 3/30/79
* 3/30/79
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
t3.8
13.8
13.8
13.8
13.9
13.9
13.9
13.9
13.9
13.9
13.9
13.9
13.9
13.9
13,9
13.9
14,2
1«.2
1«.2
14.2
12.7
12.7
12.7
12.7
12.7
12.7
12.7
12.7
12.7
12.7
12.7
12,7
12.6
12.6
12.6
12.6
12.6
12.6
12.6
12,6
12,6
12.6
12.6
12.6
12.5
12.5
12.5
12.5
11.3
11.3
11.3
11.3
10.2
10.2
10.3
10.3
10.0
9,6
9.6
9,5
9.5
10.9
10.9
10.9
10.6
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.7
10.7
10.7
10.7
10.5
10.4
10.4
10.5
10.5
10.6
11.0
11.0
11.1
11.0
11.0
11.2
11.2
11.1
11.1
7,0 -1 -1 -1 **
.0 -1
.0
.0
.0
7.0
8.0
8.0
8.0
8.0
a.i
8,6
8.6
8.6 -
8.6
7.4
7.4
7.4
7.5
7.7
7.7
7.7
7,7
7.7
7.8
7.8
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7,
-
-
-
7.8
7.8 132
7.8 128
7.8 128
7.8 127
7.8 128
7.8 132
1
1
1
-
1
-1
240
232
236
234
234
242
1
1
-1
1
-1
1
1
1
-I
-1
-
m
-
-
"
'
132
128
130
129
129
133
a****************************************************
**
**
**
**
**
**
**
**
**
*
**
**
**
**
**
**
**
**
**
*
**
**
*»
**
**
**
**
*»
**
*
**
**
**
**
**
**
*
**
**
**
**
**
**
**
**
**
**
*****
L45
KVB 6017-1216
-------
*«*»«»*****»«»*»*»***»»*»»**«*«*«*«»*******»****««**«*
ft
**
ft
ft
*«
»« DATE
*4*********/4
3/30/7*
* 3/30/7*
3/30/7*
* 3/30/7*
ft 3/30/7*
* 3/30/7*
* 3/30/7*
* 3/30/7*
** 3/30/7*
* 3/30/7*
«* 3/30/7*
3/30/7*
3/30/7*
« 3/30/7*
«* 3/30/7*
* 3/30/7*
* 3/30/7*
* 3/30/7*
** 3/30/7*
3/30/7*
« 3/30/7*
*« 3/30/7*
* 3/30/7*
* 3/10/7*
** 3/30/7*
3/30/7*
** 3/30/7*
*« 3/30/7*
** 3/30/7*
3/30/7*
*« 3/30/7*
** 3/30/7*
* 3/30/7*
* 3/30/7*
3/30/7*
ft 3/30/7*
* 3/30/7*
ft 3/30/7*
* 3/30/7*
ft 3/30/7*
3/30/7*
ft 3/30/7*
ft 3/30/7*
* 3/30/7*
ft 3/30/7*
ft 3/30/7*
3/30/7*
* 3/30/7*
15 MIN
DRY STACK GAS
TIKE
r******
1215
1230
1245
1300
1315
1330
13«5
1*00
1«15
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1015
1830
1845
1*00
1*15
1*30
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
KWTH
***
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.6
12.6
12.6
12.6
12.6
12.6
12.6
12.6
12.6
12.6
12.6
12.6
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12.5
12,6
12.6
12.6
12.6
13.8
13. 8
13.8
i3.a
02
VOLI
ME»S
r*******
11.2
10.3
10.3
10.3
10.4
10.7
10.7.
10.7
10.7
10.7
11.0
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.6
10.6
10.6
10.6
11.0
10.6
10.6
10.6
10.6
10.6
10*6
10.6
10«6
10.6
10.6
10.6
10.6
10.6
10.2
*.8
*. a
9.8
9.8
9.8
9.8
9.8
9. a
. DATA
CONCENTRATION
C02
VOL*
MEAS
******t
7.8
7.8
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.7
7.8
7.8
7.8
7.8
7.8
7.8
7.8
7.8
7.8
7,8
7.8
7.5
7.7
7,7
7,7
7.7
7.7
7.7
7,7
7.7
7.7
7.7
7.7
7.7
8.7
8.7
8.7
8.7
8.7
8.7
8.7
8.7
8.8
NO
PPMV
MEAS
[******<
126.
126.
129.
124.
123.
124.
125.
125.
125.
124.
125.
124.
125.
127.
127.
127.
127.
127.
127.
129.
129.
127.
125.
125.
125.
122.
124.
124.
124.
124.
123.
122.
120.
120.
120,
120,
H*.
11*.
II'.
125.
126.
126.
-I.
124.
124.
124.
125.
126.
NO
PP«V
3X02
[** ***<
232,
214,
217.
211.
209.
218.
220.
220.
219.
218.
226.
214.
215.
217.
218.
218.
221.
221.
221.
224.
223.
221.
217.
217.
217.
221.
215.
215.
215.
216.
214.
212.
209.
20*.
209.
209,
208.
208.
208.
210.
203.
203.
1.
200.
200.
201.
202.
203.
NO
NG/J
f *******
128.
118.
119.
116.
115.
120.
121.
122.
121.
120.
124.
118.
118.
120.
120.
120.
122.
122.
122.
123.
123.
122.
11*.
119.
119.
122.
118.
119.
11*.
11*.
118.
117.
115.
115.
115.
115.
US,
us.
115,
116,
112.
112.
I.
110,
110.
lit.
111.
112.
**
*
**
**
**
«
i***
*
**
**
**
**
**
*
**
*
**
**
**
**
*
*
«*
*
**
*
*
**
**
*«
**
**
**
*«
**
**
**
*«
»«
**
**
**
**
*
*«
*
*
**
*
**
*
*
*
**
ft*****************************
146
KVB 6017-I21C
-------
ft***********
*
**
**
**
**
** DATE
ftft4ftftftftftft;ft*1
* 3/31/79
* 3/31/79
** 3/31/79
* 3/31/79
** 3/31/79
** 3/31/79
* 3/31/79
3/31/79
3/31/79
* 3/31/79
** 3/31/79
** 3/31/79
** 3/31/79
» 3/31/79
* 3/31/79
3/31/79
* 3/31/79
3/31/79
* 3/31/79
3/31/79
* 3/31/79
* 3/31/79
* 3/31/79
*« 3/31/79
** 3/31/79
** 3/31/79
** 3/31/79
*« 3/31/79
* 3/31/79
** 3/31/79
** 3/31/79
** 3/31/79
** 3/31/79
* 3/31/79
** 3/31/79
* 3/31/79
** 3/31/79
* 3/31/79
«* 3/31/79
* 3/31/79
* 3/31/79
** 3/31/79
* 3/31/79
** 3/31/79
*« 3/31/79
»* 3/31/79
* 3/31/79
* 3/31/79
*******************************<
15 MJN. DATA
DRY STACK GAS CONCENTRATION
TIME
w ft ft: ft ft It
15
30
45
100
115
130
145
200
215
230
205
300
315
330
3«5
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 VOLZ
MWTH *EA3
fcftftftftftftftftftftftfti
13.8 .8
13. 8 .8
13.8 .8
13.8 .8
13.8 .8
13.8 .8
13.8 .8
13.8 .8
13,8 .8
13.8 .8
13.8 .8
13.
13.
13.
13.
U.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
*3.
13.
13.
13.
13.
13.
13.
13.
13.
13.
.8
10.0
10.0
10.0
10.1
10.2
10.3
10.3
10.3
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.1
10.1
10.1
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
13.8 10.0
13.8 10.0
13.8 10.0
C02
VOLX
MEAS
ft ft ft ft ft ft i
8.6
8.6
8.6
.6
.6
.6
.6
.6
.6
8.5
8.5
8.5
8.3
8.3
8.3
8.3
8.1
8.1
.0
.0
.0
.0
.0
.0
.0
.0
.0
8.1
8.2
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
8.2
NO
PPMV
HCAS
ftft ft ft ft ft 1
126.
126.
126.
126.
126.
126.
126.
126.
126.
126.
126.
125.
125.
125.
-I.
1.
125.
124.
124.
124.
123.
124.
124.
124.
124.
124.
124.
124.
124.
125.
126.
126.
129.
132.
132.
133,
134.
135.
132.
132.
135.
137.
140.
t«t.
1«2.
1«3,
1«3.
1«3.
t*****«***********
*«
**
NO
PPMV
3«0?
' ft ft ft ft ft ft 1
203.
204.
204.
204.
203.
204.
204.
204.
204.
204.
203.
202.
206.
206.
1.
-1.
210.
210.
209.
209.
208.
209.
208.
208,
208.
208.
208.
208.
208.
210.
210.
209,
213.
218.
218.
218.
220.
222.
218.
218.
223.
225.
230.
232.
233.
234.
234.
234.
NO
NG/J
1 ft ft ft ft ft ft 1
112.
112.
112.
112.
112.
112.
112.
112.
112.
112.
112.
111.
111.
114.
1.
-1.
116.
116.
115.
115.
114.
115.
115,
115.
115.
its.
115.
115.
115.
116.
116.
115.
118.
120.
120.
120.
122.
122.
120.
120.
123.
12«.
127.
128.
128.
129.
12".
129.
**
**
**
**
'** *
*
**
*
**
**
**
*
**
**
*
**
**
*
*«
**
»*
t*
*
»
**
*
**
**
**
**
*
**
*
**
*
**
**
»*
**
**
*
**
**
**
**
»*
**
*«
**
**
»«
**
A*************************************************************
147
KVB 6017-1216
-------
.ft*************************
* IS *IN
* D«» STACK GAS
*
*«
* 0»TE
TIME
LOAD
M*TH
02
VOLX
*AS
********************4
. DATA
CONCENTRATION
C02
VOLX
MEAS
MO
PPWV
MEAS
NO
PPHV
3*0*
.*****«»
**
**
**
NO
NG/J
*
*
*
/a****/***.***************************************************
*« 3/31/79
** 3/31/79
** 3/31/79
« 3/31/79
** 3/31/79
** 3/31/79
* 3/31/79
** 3/31/79
3/31/79
»* 3/31/79
»« 3/31/79
** 3/31/79
* 3/31/79
* 3/31/79
** 3/31/79
* 3/31/79
* 3/31/79
* 3/31/79
3/31/79
» 3/31/79
»* 3/31/79
** 3/31/79
«* 3/31/79
** 3/31/79
** 3/31/79
* 3/31/79
** 3/31/79
** 3/31/79
»* 3/31/79
« 3/31/79
** 3/31/79
** 3/31/79
** 3/31/79
» 3/31/79
* 3/31/79
«« 3/31/79
3/31/79
* 3/31/79
** 3/31/79
« 3/31/79
* 3/31/79
*« 3/31/79
« 3/31/79
* 3/J1/79
*« 3/31/79
* 3/31/79
** 3/31/79
3/31/79
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
1645
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
13.9
13.9
13."
13."
13."
13."
13."
13.9
14.1
14,1
14.1
I8. 1
14,1
14.1
14.1
J4. 1
I'.l
!*.!
14.1
14,1
14.1
1*, 1
1*»1
14.1
I'.l
l*.l
I'.l
14, 1
13.8
13. a
13,8
13.8
14,1
la.l
14.1
J4.J
14.1
14.1
14.1
14.1
14.1
14.1
13."
13*"
13."
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.1
10.1
10.1
10.1
10.1
10.1
10.2
10.2
10.2
10.2
10.5
10.1
10.1
10.
10.
10.
10.
10.
10.
10.
10.
10.
10.
10.
10.1
10.2
10.2
10.2
10.2
10.2
10.2
10.2
8.2
8.2
a. 2
B.2
8.2
a. 2
8.2
8.2
8.2
8.2
8.2
8.3
8.3
8,3
8,3
8,3
8.3
8.3
8.2
8.2
8.2
8.2
8.2
8.2
8.2
8.2
8.1
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
8.3
U3.
143.
143.
143.
144.
145.
146.
146.
146,
146.
145,
144,
143.
142.
141.
13".
139.
140.
140,
140.
140.
1*1
140.
13".
138.
137.
134.
133.
131.
131.
130.
130.
130.
130.
12",
12".
12".
12".
12".
12".
12".
128.
128.
128.
124.
123.
124.
124.
234.
236.
236.
236.
238.
23".
241.
241,
2*1 ,
241,
23".
238.
236.
235.
233.
230.
230.
232.
233.
233.
233.
235.
234.
233.
231.
22".
231.
221.
218.
217.
216.
216.
217.
216.
215.
215.
215.
215.
216.
215.
215,
214,
215.
214.
208.
206.
207.
208.
12".
130.
130.
130.
131.
132.
133.
133.
133.
133.
132.
131.
130.
130.
128.
127,
127.
128,
128,
12",
12".
12".
12",
128.
127.
126.
128.
122.
120.
120.
11".
11".
120.
11".
U".
118.
118.
11".
119.
11".
11".
118.
11".
118.
115.
114,
114.
115.
**
*
*
**
**
**
*«
**
**
**
**
**
»
**
*
**
**
*
»»
*
**
ft*
*
**
*»
*
ft*
ft*
*«
*«
**
*
ft*
**
**
ft
ft*
ft*
ft*
ft*
**
**
ft*
ft*
ft*
ft*
**
ft************** «******<
148
KVB 6O17-1216
-------
*« 15 "IN, DATA »«
« DRY STACK GAS CONCENTRATION *
*. **
.* 02 C02 NO NQ NO
** LOAD VOLX VOLX PP"V PPMV NG/J *
*« DATE TtNC M*TH MEAS MEAS M£AS S*0* **
w»w*«wwwww,wwwwwwwwwwwwwwwwwwwwwwwwwwwwww»ww«www*wwwwwwwwwwwww«
*« 4/
» 4/
** 4/
*« 4/
** 4/
* 4/
** 4/
w» 4/
** 4/
* 4/
w* «/
«* 4/
** 4/
* 4/
»* 4/
* 4/
* 4/
«* 4/
4/
«* 4/
** 4/
«» «/
»* 4/
** 4/
** 4/
* 4/
** 4/
** 4/
* 4/
** 4/
** 4/
** 4/
*« 4/
* 4/
»« 4/
* 4/
w 4/
** «/
»w 4/
«* 4/
»* «/
«* 4/
* 4/
*« 4/
» 4/
** 4/
** 4/
** 4/
1/79
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
1/70
IS
30
05
too
115
130
200
215
230
245
300
315
330
400
415
430
445
500
515
530
545
600
615
630
645
700
715
730
745
800
sis
830
845
000
015
050
045
1000
1015
1030
1045
1100
IMS
1130
1145
1200
13.3
13.3
13.3
13.3
13.3
13.3
13.3
13.3
13.3
13.3
13.3
13.3
13,3
13.3
13,3
13.3
13.3
13.3
13.3
13.3
13.5
13.5
13.5
13.5
13.6
13.6
13.6
13.6
13,6
13.6
13.6
13.6
13.6
13,6
13^6
13.6
13.6
13.6
13.6
13.6
13.6
13.6
13.6
13.6
13.6
13.6
13.6
13.6
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10. 5
10.4
10.3
10.3
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
ft. 3 124,
8.3 124.
8.3 125.
8.3 124,
8.3 120.
8.3 120.
8.3 120.
8.3 124.
8,3 125.
8.3 124.
8.3 120.
8,3 124.
8.2 120,
8.2 122.
8.2 121.
8.2 119.
8.2 110.
7.9 HO.
8.
8.
8.
8.
8.
a.
a.
8.
8,
8,
8.
8.
a.
a.
0 .
0 .
" ,
8,
8.
8.
8.
8.
a.
8.
8.
8.
11^.
120.
120.
121.
122.
120.
124,
124.
120,
124,
.124,
120,
125,
125,
125.
125,
125.
125,
126.
126.
126.
126.
126.
126,
120.
120,
128.
8.1 128.
8.1 128.
8.1 128.
207.
208.
208.
206.
206.
208.
207,
207.
200.
208.
208.
208.
207.
204.
202.
200.
206.
202.
202.
203.
202.
203.
204.
207.
207.
208.
208.
208.
208.
208.
200.
200,
200.
200.
210.
210.
211.
211.
211.
211.
211.
212.
216.
216.
215.
215.
215.
215.
110.
115.
115.
115.
115.
115.
110.
110.
115.
115.
115.
115.
114.
113.
112.
110.
113.
112.
111.
112.
111.
112.
113.
110.
110.
115.
115.
115.
115.
115.
115,
115,
115.
U5.
116,
116,
11*.
116.
116.
116,
116.
117.
119.
110.
119,
118.
118.
118.
ww
*
w*
*
ww
*w
*w
*w
»*
»w
ww
**
*w
w.
**
»w
**
*
ww
*
ww
w*
**
**
**
**
ww
**
ww
**
ww
ww
*»
Ww
ww
Ww
ww
ww
ww
ww
ww
w*
««
**
ww
w.
ww
ww
149
KVB 6017-1216
-------
ft
ft*
ft*
*
ft*
ft*
DATE
TIME
IS MIN
DRY STACK GAS
02
LOAD VOIX
MWTH MEAS
. DATA
CONCENTRATION
C02 NO
VOLX PPMV
MEAS MEAS
NO
PPMV
3*0?
NO
NG/J
»*
*
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*
*
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
t/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
i/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
1/79
t/79
1/79
1/79
1/79
1/79
1/79
t/79
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
13.6 10
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
13.
11
11
11
11
11
11
11
11
10
10
10
10
10
10
10
11
11
11
10
10
10
10
11
11
11
11
11
11
11
11
11
11
It
11
11
13.5 11
13.5 11
13.5 12
.2
6
.6
.6
.5
.5
.3
.2
.2
.9
.8
.7
.7
.7
.9
.9
.0
.0
.0
.9
.9
.9
.9
.0
.0
.2
.2
.2
.7
.7
.
.
.
.
.
.
.
.
.1
13.5 12.2
13.5 12
13,5 11
13,5 It
13.5 11
13.5 It
13.5 11
13.5 11
13.5 It
.1
.9
.5
.3
.2
.2
.2
.0
.1
.8
.8
.8
,9
7.0
7.1
7.2
7.3
7.4
7.5
7.6
7.7
7.7
7.7
7.6
7.5
7.5
7.5
7.5
7.6
7.7
7.7
7.7
7.6
7.5
7.5
7.4
7.1
6.9
6.9
6.9
6.9
6.9
6.9
6.9
6.9
6,9
6.8
6.7
6.8
7|l
7.2
7.3
7.4
7.4
7.5
128.
110.
111.
112.
112.
113.
114.
116.
117.
121.
124.
126.
127.
127.
122.
121.
119.
11'.
119.
119.
121.
121.
122.
121.
120.
118.
116.
116.
112.
1131
113.
112.
113.
113!
113.
lit.
109.
108.
108.
112.
116.
120.
123,
124.
125.
126.
215.
212.
214.
215.
214.
214.
213.
215.
216.
218.
221.
222.
224.
224.
217.
217.
215.
214.
214.
214.
217.
216.
217.
218.
218.
217.
215.
215.
220.
223.
223.
222.
223.
224.
225.
224.
226.
222.
221.
222.
222.
223.
223.
224.
229.
230.
230.
229.
118.
117.
118.
119.
118.
118.
118.
119.
119.
120.
122.
122.
124.
124.
120.
119.
118.
118.
118.
118.
119.
119.
120.
120.
120.
120.
119.
119.
121.
123.
123.
123.
123.
124.
124.
124.
124.
122.
122.
123.
122.
123.
123.
124.
126.
127.
127.
126.
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*
*
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*
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****»»*******«*««*«»«***»»*«**«»*«*«*««»«*
150
K7B 6017-1216
-------
**
*
ft*
DATE
TIME
15 "IN. DATA
OUT STACK GAS CONCENTRATION
02 C02 NU
LOAD VOLX VOIX PP"V
MKTH MEAS MEAS MEAS
NO
PPMV
3X02
NO
NG/J
**
**
*
**
*
*
************ **ft*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*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
ft*
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
«/
4/
«/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
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
J6.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.3
16.3
16.3
13.3
13.3
13.3
13.3
13.3
13.3
13.3
13.3
13.3
13.3
13.3
13.3
13.5
13.5
13.5
13.5
14.4
14.4
14.4
14.4
16.6
16.6
16.6
16.6
16.6
16.6
16.6
16.6
11.0
11.0
11.0
11.0
11.1
11.1
11.1
11.1
11.1
11.1
11.1
11.1
11.1
U.I
U.I
11.1
U.I
U.I
U.I
U.I
U.I
U.I
U.I
U.I
U.I
U.I
U.I
11.1
11.0
11.0
11.0
10.9
10.9
10.9
10.7
10.7
8.1
8.0
8.1
8.2
8.2
8.2
7.9
7.9
7.9
7.9
7.9
7.9
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7,5
7.5
7.5
7.5
7.
7.
7.
7.
7.
7.
7.
7.
7,6
9.1
9.9
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
127
127
127
132
134
134
133
134
134
132
131
132
134
134
134
135
133
134
134
133
132
131
131
134
132
132
132
132
134
135
136
138
141
145
146
127
117
114
116
117
115
117
119
118
117
119
119
119
t
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4
9
t
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t
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t
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230.
229.
231.
241.
244,
243.
2«4.
244.
242.
240.
2«2.
244.
244.
244.
247.
243.
244,
244.
243,
242.
240.
239.
244,
242.
242.
242.
242.
243.
245.
246.
248.
252.
259.
258.
225.
165.
158,
162.
165.
163.
166.
164.
163.
161.
163,
163.
163.
127.
126.
127.
133.
135,
134.
134.
135.
135,
133.
132.
133.
135.
135.
135.
136.
134.
135.
135.
134.
133.
132.
132.
135.
133.
133.
133.
133.
134,
135.
136.
137.
139,
143.
142.
124.
91.
87,
89.
91.
90.
91.
90,
90.
89.
90.
90.
90.
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a*************************************************************
151
KVB 6017-1216
-------
********
*
*
**
ft*
ft*
** DATE
ft*******************
IS HIM
DRY STACK CAS
02
LOAD VO4.X
TIME MMTH MEAS
»*«**«*»*««*****«««*****»**
. DATA *
CONCENTR»7ION «
**
C02 NO NO NO *»
VOLX PPHV PPMV NG/J **
HEA3 MEAS 3*0? **
A************************************************
** 4/
»* 4/
*« 4/
* «/
* «/
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*" 4/
« 4/
* «/
* 4/
«/
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4/
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/
/
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4/
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4/
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4/
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4/
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ft* «/
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« «/
« «/
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2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
2/79
1215
1230
124S
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
16.6 7.8
16.6 7.8
16.6 7.8
16.6 7.8
16.7 7.7
16.7 7.7
16.7 7.7
16.7 7.7
16.7 7.7
16.7 7.7
16.7 7.7
16.7 7.7
16.8 7.7
16.8 7.7
16.8 7.7
16.8 7.6
lT.0
17.0
17.0
17.0
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16.4
16.4
16.4
16.3
16.3
16.3
16.3
16.1
16.1
16.1
16.1
16.1
l*.l
l*.l
l*.l
16.1
16,1
16.1
16.1
16.0
16.0
16.0
16.0
16.0
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.2
.2
.2
.2
.2
.2
.2
.2
.2
.2
.2
.6
.6
.6
.6
.6
.6
.6
.6
.6
.6
.6
.6
.6
.6
.6
.6
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16,0 8.5
16.0 8.5
16.0 8.4
10.0
10.0
10.0
10,0
10.0
10.0
10.0
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
9.8
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'.7
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9.7
9.7
9.7
9.7
9.7
9.2
9.3
9.3
9.3
9.3
9.3
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9.3
9.3
9.3
9.3
9.3
9.3
9.3
9.3
9.3
120.
120.
120.
120.
119.
119.
119.
119.
116.
116.
117.
119.
119.
117.
119.
117.
125.
127.
129.
130.
129.
127.
127.
127.
127.
127.
127.
126.
127.
130.
130.
131.
132.
132.
132.
132.
132.
132.
131.
131.
131.
131.
130,
129.
126.
125.
122.
122.
164.
164.
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164.
163.
163.
162.
162.
150.
158.
160.
162.
161.
159.
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158.
175.
180.
1«1.
1«3.
182.
180.
180.
180.
179.
179.
179.
178.
186.
189.
189.
191.
193.
192.
192.
192.
193.
193.
191.
191.
191.
191.
189.
187.
182.
180.
176.
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91.
91.
90.
90.
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89.
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87.
87.
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89.
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97.
99.
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99.
99.
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99.
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JOS.
104.
104.
105.
106.
106.
106.
106.
106.
106.
105.
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104.
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152
KVB 6017-1216
-------
*****«************»**«***********»*<
** IS *IN. DATA
** DRY STACK GAS CONCENTRATION
**
** 02 C02 NO
** LOAD VOLX VQLX PPMV
*« DATE TIME MNTH M£*$ MEAS MEAS
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3/79
3/79
3/79
3/79
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3/79
3/79
3/79
3/79
3/79
3/79
3/79
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3/79
3/79
3/79
3/79
3/79
3/79
3/79
3/79
3/79
3/79
3/79
3/79
3/79
3/79
3/79
3/79
3/79
3/79
3/79
3/79
3/79
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
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1100
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1200
16.
16.
16.
16.
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10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
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10.0
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120
120
121
120
119
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109
107
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153
KVB 6017-L216
-------
**»«***«*«»**»**«»***«*«***»**«*«*«*«**«*««**««»**«*«««»««
* is MIN. DATA *«
** OR* STACK 6A3 CONCENTRATION **
*
**
** 02 C02 NO NQ NO *
** LOAD VOLX VOUX PP*V PPMV N6/J *
* DATE TIME HNTH «e*3 MEAS MEAS 3202 *
***************************************************************
* 4/ 3/79 12l5 16.3 7.8
** «/ 3/79 1230 16.3 7.8
** 4/ 3/79 1245 16.3 7.9
** «/ 3/79 1300 16.3 .2
** «/ 3/79 1315 16.1 .3
* 4/ 3/79 1330 16.1 .5
«/ 3/79 1345 16.1 .0
* 4/ 3/79 1400 16.1 .0
«/ 3/79 1415 16.1 ,0
« 4/ 3/79 1430 16,1 .0
*« «/ 3/79 1445 16.1 ,0
«/ 3/79 1500 16.1 .1
** «/ 3/79 1515 16.0 7.6
«/ 3/79 1530 16.0 7.8
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* «/ 3/79 1600 16.0 7.7 10.0
** «/ 3/79 1615 16.1 7.7 10,0
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** 4/ 3/79 1700 16,1 7.7 10. 0
* «/ 3/79 1715 16,0 7.
«/ 3/79 1730 16.0 7.
* 4/ 3/79 1745 16.0 7.
* 4/ 3/79 1800 16,o 7.
* 4/ 3/79 1815 16.0 7.
* 4/ 3/79 1830 16. 7.
** 4/ 3/79 1845 16.
* 4/ 3/79 1900 16.
* «/ 3/79 1915 15.
* 4/ 3/79 1930 IS.
4/ 3/79 1945 15.
** 4/ 3/79 2000 15.
* 4/ 3/79 2015 16.0
* 4/ 3/79 2030 16.0
** 4/ 3/79 2045 16.0
** «/ 3/79 2100 16.0
* 4/ 3/79 2115 16.0
4/ 3/79 2130 16.0
4/ 3/79 2145 16.0
4/ 3/79 2200 16.
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154
KVB 5017-1216
-------
IT************************************************
*
**
*
**
**
** DATE
TIME
15 Up
DRY STACK GA3
02
LOAD VQLX
MHTH M£A3
1. DATA
«**«
**
CONCENTRATION *
COS
VOLX
HEA3
NO NO NO
PPMV PPKV NG/J
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**
*«
**
**
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4/
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4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
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
845
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
16.0
16.0
16,0
16,0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
15.8
15.8
15.8
15.8
15.8
15.8
15.8
15.8
16.0
16,0
16,0
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16,0 9.4
16.0 .5
16.0 .4
16.0 .3
16.0 .3
16.0 .«
16.0 .3
16.0 .2
16.0 .2
16.0 7.7
16,0 7.7
16,0 7.7
16.0 7.3
16.0 7.
16,0 7.
16.0 7.
16.0 7.
16.0 7.
10.0
10.0
10.0
10.0
10.0
10.0
10.0
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10.0
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L55
KVB 6017-1216
-------
ft*
ft*
**
ft*
*
* DATE
15 *IN. D*TA
DRY STACK C*3 CONCENTRATION
02 C02 NU
LOAD VOtI VOtX PP*V
TIME MHTH MEA3 MEA3 HEAS
NO
PPMV
3X02
NO
NG/J
«
**
**
*
**
**
ft*********************************************** ***********«
** 4/
** 4/
ft* «/
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«/
4/
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4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
4/79
1215
1230
12«5
1300
1315
1330
1345
1400
141S
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1800
1015
1830
1845
19QO
1«M5
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
|6.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16.0
16,0
16.0
16.0
16.0
16.0
16.3
16.3
16.3
16.3
16.3
16.3
16.3
1*.3
1*.3
1*.3
1*.3
1*.3
16.3
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16.3
1».3
l*.l
l*.l
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7.5
7.5
7.6
7.6
7.4
7.4
7.4
6.7
7.6
7.6
8.5
8.6
8,7
7.9
7.9
7.2
7.2
7.2
7.2
7.1
7.0
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1.0
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7.2
7.2
7.1
7.1
7.1
7.1
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7.1
7.1
7.2
7.2
7.2
7.2
7.2
7.2
7.2
10.2
10.2
10.2
10.3
10.3
10.3
.0
10.2
10.1
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10. I
10.1
10.1
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10*2
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10.0
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125.
127.
127.
131.
130.
122.
122.
122.
122.
122.
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121.
122.
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123.
123.
123.
124.
124.
125.
126.
125.
126.
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122.
122.
122.
123.
122.
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124.
125.
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124.
119.
119.
118.
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166.
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184.
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167.
167.
159.
159.
159.
159.
157.
157.
107.
105.
104.
104.
105.
162.
163.
164.
163.
163.
160.
158.
104.
104.
104.
104.
105.
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162.
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89.
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90.
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ft*
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ft*************************************************************
156
KVB 6017-1216
-------
««
**
*
**
»*
*
**
>**»****«
DATE
>*****
TIME
ft**************************!
15 *IN. OAT*
DRV 3T*CK GAS CONCENTRATION
02 C02 NO
LOAD VOLX VOLX PPMV
MWTH MEAS MEA3 MEA3
>******!
NO
PPHV
3X02
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5/79
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5/79
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5/79
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5/79
5/79
5/79
5/79
5/79
5/79
5/79
5/79
5/79
5/79
5/79
5/79
5/79
5/79
5/79
5/79
5/79
5/79
5/79
5/79
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
16.3
16.3
10.3
I*. 3
16.3
16.3
16.3
16.3
1*.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
10. i
l*.l
16.1
16.1
16.0
16.0
16.0
16.0
16.1
l*.l
16.1
16.1
16.3
16.3
16.3
16.3
16.1
16.1
16.1
16.1
15.8
15.8
15.8
15.8
16.3
16.3
16.3
16.3
7.2 10
7.2 10
7.2 10
7.2 10
7.2 10
7.2 10
7.2 10
7.2 10
7.2 10
7.2 10
7.2 10
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7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
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10
10
10
10
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10.0
10
10
10
10
10
10
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10
10
10
10
10
10
10
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121.
121.
121.
121.
122.
122.
129.
129.
129.
130.
131.
130.
130.
131.
135.
136.
136.
135.
132.
134.
138.
139.
132.
131.
128.
132.
137.
127.
113.
113.
126.
126.
125.
124.
124.
125.
125.
125.
125.
125.
157.
158.
160.
160.
158.
158.
159.
159.
158.
158.
158.
158.
160.
166.
174.
174.
174.
175.
174.
173.
173.
174.
180.
181.
181.
175.
172.
174.
179.
l»t.
173.
171.
167.
172.
183.
170.
150.
150.
168.
168.
167.
165.
165.
167.
167.
166.
166.
167.
86.
87.
88,
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87.
87.
88.
88.
87.
87,
87,
87.
88.
92.
96,
96.
96.
96.
96.
95.
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100.
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99.
100,
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94.
92.
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101.
94,
83.
83.
93.
93.
92,
91.
91.
92.
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ft*
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ft**************************************************************-
157
KVB 6017-1216
-------
>»*«****«
*
**
**
*
**
**
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**
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*
DATE
ft*** ******
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
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4/
4/
4/
4/
4/
4/
4/
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4/
10.1
10.0
10.0
10.0
10,1
10,1
toll
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.1
10.1
10.1
10.1
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.5
10.6
10.5
10.2
10.2
10.2
10.2
10.2
10.2
10.1
10.1
10.1
10. 1
10.1
10.1
I W W m m -m ft
126.
126.
126.
130.
132.
125.
126.
127.
1221
122.
123.
123.
123.
122.
122.
123.
124.
123.
124.
124.
124.
121.
120.
120.
11**
iisl
174.
172.
176.
172.
1*2.
115.
114.
114.
113,
112.
112.
111.
111.
109.
110.
111.
110.
107.
107.
NO
PPMV
3X0?
t **. * 1l * A 1
167.
1651
170.
172.
162.
164.
166.
161.
15«>.
158.
160.
160.
159.
158.
159.
161.
162.
161.
163.
162.
162.
157.
156.
157.
155.
156.
155.
155.
222.
216.
223.
226.
227.
151.
151.
ISO.
14?.
14?.
148.
146.
1«5.
145.
147.
1«5.
141.
141.
NQ
HG/J
r**. ***.*.
92.
92.
91.
94.
95.
89.
90.
9t.
89.
88.
87.
86.
88.
88.
87.
87.
89.
89.
89.
90.
90.
89.
86.
86.
86.
85.
86.
85.
85.
122.
119.
123.
125.
125.
83.
83.
83.
82.
82.
82,
81.
81.
80.
80.
81.
80.
78.
78.
»*
**
**
*
**
****
«
**
*
*
**
*
*
»
*
**
*
**
*
»
**
**
**
**
*
**
*
»*
*
**
*
**
*
*
**
*»
**
»«
«
**
**
**
**
*
*
*«
**
**
**
*»
**
**
**********«**«««««**«*********«**«**«**«
158
K7B 6017-1216
-------
a*********************************************
** 15 "IN. DATA **
** DRY ST*C* GAS CONCENTRATION »*
* «
«*
**
** DATE
TIME
LOAD
WWTH
02
VOLX
HEAS
C02
VOLX
MEA3
NO
PPMV
MEA3
NO
PPMV
3*0"
NO
NG/J
»
«»
*
«******»**»*****«*««*****«**************************
** 4/ 6/79
« 4/ 6/79
** 4/ 6/79
* 4/ 6/79
** 4/ 6/79
** «/ 6/79
*« 4/ 6/79
** a/ 6/79
** 4/ 6/79
** 4/ 6/79
* 4/ 6/79
«« 4/ 6/79
*« 4/ 6/79
* 4/ 6/79
4/ 6/79
** 4/ 6/79
«« 4/ 6/79
* 4/ 6/79
*tk 4/ 6/79
« 4/ 6/79
** «/ 6/79
«* 4/ 6/79
«* 4/ 6/79
»» 4/ 6/79
** 4/ 6/79
** 4/ 6/79
«« 4/ 6/79
** 4/ 6/79
** 4/ 6/79
** 4/ 6/79
** 4/ 6/79
** 4/ 6/79
** 4/ 6/79
*« 4/ 6/79
*« 4/ 6/79
** 4/ 6/79
*« 4/ 6/79
«* 4/ 6/79
** 4/ 6/79
*« 4/ 6/79
** 4/ 6/79
«* 4/ 6/79
** «/ 6/79
*« 4/ 6/79
** 4/ 6/79
** 4/ 6/79
«* 4/ 6/79
** 4/ 6/79
15
SO
45
too
115
130
1«5
ZOO
215
230
245
300
J15
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
I'.'
17.9
17.9
17.9
f».3
I*. 3
19.3
I9. 3
I*. 6
19.6 '
19.6
19.6
19.3
19.3
19.3
19.3
1«.2
18.2
18.2
18.2
16.1
16.1
16.1
16.1
1^.1
16.1
16.1
16.1
16.1
1^.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
7.2
7.2
7,2
7.2
7.2
7.2
7.2
7,1
7.1
7.1
7.1
7.1
7.1
7.0
7.0
7.0
T.O
7.0
6.9
6.9
7.0
7.1
7,2
7.2
7.2
7.3
7.2
7.2
7.2
7.2
7.2
7.2
7.1
7.2
7.2
7.«
7.4
7.4
7.4
7.4
7.2
7.3
1.3
7.2
7.2
7.2
7.3
7.2
. A A A * A A 4
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.3
10.3
10.3
10.3
10.3
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
".»
10.1
10.0
10,0
10.0
10.0
10.0
10.0
10,0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.1
10.0
9.9
9.9
9.9
10.0
10.0
>«»****«
108.
108.
109.
109.
109.
109.
107.
106,
106.
104.
107.
106.
uo.
111.
112.
113.
115.
119,
118.
119.
122.
125.
126.
127.
130.
132.
129.
129,
130.
130.
134.
137.
138.
1«1.
141.
1«0.
135.
133.
134.
125.
123.
124.
124.
123.
123.
125.
122.
121.
'«*»***
1«1.
1«2.
1«3.
1«2.
1"2.
1«2.
1«0.
137.
138.
134.
139.
iao.
1«2.
144.
1«4,
146.
1«8.
153.
151.
153.
158.
162.
!<>«.
107.
171.
174.
170.
170.
170.
171.
175.
179.
179.
18«.
184.
185.
180.
177.
179.
166.
162.
163,
163.
161.
161.
164.
161.
159.
[*****«
78.
76.
79.
78.
78.
78.
77.
76,
76.
74.
76.
77.
79.
79.
80.
60.
82.
84.
83.
85.
87.
90.
'1.
*2.
94.
96.
94.
'3,
94.
'«.
97.
99.
99.
101.
101,
102.
99.
98.
99,
92,
89.
90.
90.
89.
89.
90,
89,
87,
!««***««
**
**
«*
**
**
**
*
**
**
**
**
*
**
**
**
«
**
**
**
**
»«
**
**
**
**
**
**
*«
**
**
**
**
»*
*
**
**
**
**
**
«
**
*«
**
**
**
»«
**
**
**«
159
KV3 6017-1216
-------
****
**
*
**
**
**
**
****
** 4/
* 4/
*« 4/
* 4/
* 4/
* 4/
* 4/
4/
* 4/
»* 4/
»* 4/
« 4/
»* 4/
* 4/
* 4/
« 4/
** 4/
* 4/
** 4/
* 4/
4/
** «/
4/
4/
* 4/
** 4/
** 4/
** a/
* «/
* 4/
* 4/
* 4/
** 4/
* 4/
*« 4/
*» 4/
* 4/
* 4/
« 4/
* 4/
* 4/
* 4/
** 4/
* 4/
* 4/
* 4/
* 4/
* 4/
«*****<
DATE
******<
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
6/79
!*****<
TIKE
>**<
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
19QO
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
!««**««***
15 MJN
DRV STACK GAS
02
LOAD VOLx
M*TH *£A3
1 *****«******
16.1 7.2
16,1 7.3
16,1 7.2
16.1 7.2
16.3 7.3
16.3 7.3
16.3 7.3
16.3 7.2
16.3 7.2
16.3 7.2
16.3 7.2
16,3 7.2
16.3 7.2
16,3 7.2
16.3 7.2
16.3 7.2
16.3 7.2
16.3 7.2
16.3 7.2
16,3 7.2
16.3 7.6
16.3 7.7
16.3 7.Q
16.3
17.9
17.9
17.9
17.9
16,4
»*.«
16,4
16.4
16^3
16,3
16,3
16.3
16.3
16,3
16,3
16,3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
.8
8
7
7
.9
%9
.5
.5
.1
Is
.8
.8
.9
.8
.8
.8
.8
.8
.8
.8
.9
.9
.9
.9
««*»****«*«*
. DATA
CONCENTRATION
C02 NO
VOLX PPMV
HEAS *£AS
ft***********
9,9 122.
10.0 123.
10.
to.
10.
10.
10.
10.
10.
10.
10.
10.
10.
10.
10.
10!
10.
10.
to.
10.
10.
10.
10.
to.
122.
121.
121.
122.
121.
124.
125.
127.
125.
125.
124.
12«!
124,
124.
124.
125.
124.
124.
124.
124.
125.
126.
10.2 126.
10.2 126,
10.2 127.
10.2 129.
10.2 175.
10.2 169.
10.1 167.
10.5 120.
10.5 120.
9.9 119,
10.0 119.
10.1 119.
10.1 118.
10.2 118.
10.2 116.
10.2 116.
10.2 117.
10.2 116.
11.9 US.
10.2 116.
10.2 115.
10.2 114.
10.2 US.
*****,
NO
PPHV
3X02
******<
160.
162.
161.
158.
159.
161.
160.
163.
164.
166.
164.
162^
162.
162.
162.
163.
163.
163.
162.
167.
167.
160.
159.
160.
159.
160.
162.
165.
218.
210.
217.
153,
153.
151.
151.
152.
150.
150.
1481
149.
148.
ISO.
149.
147.
147.
147.
i*** ***
NO
NG/J
I******
88.
89,
89,
87.
88.
89.
88.
90.
90.
91.
90.
90.
90.
90,
90,
89.
90.
90.
90.
90.
92.
92.
88.
98.
88.
88.
88.
90.
91.
120.
116.
120.
84^
83.
83.
84.
83.
83.
82.
82.
82.
82.
83.
82.
81.
81.
81.
****
*
*«
44
**
*
*
»
*
*
*
**
**
**
*
**
**
**
*
*
*
**
*»
*
**
*
*
*«
**
*«
*«
**
**
*
*
*
*
**
*
*«
**
*
**
**
**
»*
**
**
*«
**
*
**
0*
.**
******»******«*«****««»*«****»»*»**«»*«*»«
160
KVB 6017-1216
-------
«1
ft*
ft*
ft*
ft*
ft*
ft*
ft************
DATE TIME
A*********
15 MIN. DATA **
DRY STACK GAS CONCENTRATION **
**
02 C02 NO NQ NO
LOAD VGLX VOUX PPMV PPMV NG/J
MKTH ME«S MEAS MEAS 3x0*
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*
ft*
ft*
ft*
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
«/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
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
-------
**
**
*«
*
»
»» DATE
TINE
15 "IN
OUT STACK GAS
02
LOAD VQLX
H*TH *EA3
. DATA
CONCENTRATION
CQ2
VOLX
MEAS
NO
PPMV
MEAS
NO
PPMV
3X02
NO
NG/J
*
**
*
*
*
**
ft********************************************************
** 4/
* 4/
* 4/
** 4/
*« 4/
* 4/
* 4/
** «/
* 4/
«/
» «/
* «/
** 4/
* «/
** «/
* 4/
« 4/
* «/
« 4/
4/
* «/
** «/
** «/
«/
** 4/
»* 4/
«* 4/
* 4/
** 4/
** «/
* 4/
* 4/
* «/
*« 4/
** 4/
« 4/
»* 4/
* 4/
* 4/
»* 4/
4/
* «/
4/
«« 4/
* 4/
** 4/
* 4/
* 4/
7/79
7/79
7/7«
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
7/79
t2l5
1230
1205
1300
1315
1330
13«S
1400
1415
1430
1445
1500
1515
1530
1545
1600
1*15
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
t8,8
18. 8
18.8
18.8
18.2
18.2
18.2
18.2
17.
1*.
17.
17.
1*.
16.
1*.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
16.
.7
.7
.8
.6
.5
.5
.5
.7
7.0
7.0
7.0
7.0
16.7 7.0
16.7 7.2
16.7 7.2
16.7 7.2
16. 7.1
16. 7.2
16. 7.2
16, 7.2
16. 7.2
16. 7.2
16. 7.2
16. 7.2
16. 7.2
16. 7.2
16. 7.2
16. 7.2
16. 7.2
16. 7.2
16.1 7.2
16.1 7.2
10.6
10.6
10.6
10.6
10.6
10.6
10.6
10,6
10.5
10.5
10.5
10.6
10.3
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
199.
189.
tee.
188.
191.
191.
191.
190.
174.
175.
177.
177.
172.
129.
130.
130.
132.
134.
135.
135.
135.
132.
132.
132.
132.
132.
132.
132.
132.
132.
132.
132.
131.
130,
127.
12«,
122,
122,
122.
124.
122,
121.
122.
120.
121.
121.
121.
120.
233.
234.
231.
231.
237.
2«2.
2«0.
211.
218.
218.
220.
221.
218.
165.
166.
166.
169.
171.
173.
173.
173.
170.
170.
170.
170.
171.
170.
170.
171.
17«.
173.
172.
171.
170.
166.
162.
160.
160.
160.
162.
160.
158.
159.
157.
159.
158.
159.
158.
129.
129.
128.
127.
130.
133.
133.
133.
120.
120.
121.
122.
120.
91.
91.
91.
93.
90.
95.
96.
95.
94.
94.
94.
94.
94.
94.
94.
94.
"6.
"5.
«.
94.
"3.
*2.
90.
88.
8«.
88.
89.
8«.
87.
88.
86.
88.
87.
88.
87.
**
**
**
«
*«
*
*
ft*
*
**
*
*
*
**
*
*
*
*
*
**
**
**
**
*
**
*
»«
**
**
»*
**
*
**
**
*«
*
*
**
**
*
**
«
*
**
**
*
*
ft**************************************
162
KVB 6017-1216
-------
a**************************************************************
** 15 "IN. DATA
*« DRY STACK CA3 CONCENTRATION
**
** 02 C02 NO
** LOAD VOLT VOLX P*"V
** DATE TIME MNTH MEA3 MEAS MEA3
NO
PPMV
NO
NG/J
*
**
**
**
**
**
***************************************************************
** 4/
** 4/
*« 4/
** 4/
** 4/
*« 4/
** 4/
*« 4/
*« 4/
* 4/
* 4/
** a/
** 4/
** 4/
*« 4/
* 4/
** 4/
** «/
* 4/
** «/
* «/
** 4/
* 4/
* »/
** «/
** »/
* 4/
* 4/
** 4/
** /
** 4/
** 4/
* 4/
«« «/
** 4/
** /
** 4/
* /
* 4/
* 4/
* 4/
»* 4/
** 4/
* 4/
** 4/
* 4/
** 4/
** 4/
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79 -
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
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
21.1
21.1
21.1
21.1
21.1
21.1
21.1
21.1
21.1
21.1
21.1
21.1
21.1
21.1
21.1
21.1
21.1
21.1
21.1
21.1
20.5
20.5
20.5
20.5
20.5
20.5
20.5
20.5
20.5
20.5
20.5
20.5
20.5
20.5
20.5
20.5
20.4
20.4
20.4
20.4
19.9
19.9
19.9
19.9
19.6
l9|6
19.6
7.2
7.2
7.2
7.2
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.0
6.6
6.6
6.6
6.6
6.5
6.4
6.5
6.4
6.4
6.4
6.4
6.4
6.4
6.4
6.4
6.5
6.7
6.6
6.6
6.7
6.6
6.6
6.7
7.0
7.1
6.9
6.7
6.6
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.6
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.9
10.9
10.9
10.9
10.9
10.9
10.9
10.9
10.8
10.7
10.7
10.7
10.7
10,7
10.7
10.6
10.3
10.3
10.5
10.6
120.
1 J9,
117.
116.
119,
118.
117.
115.
110.
113.
110.
113.
112.
110.
109,
110,
110.
111.
111.
109.
159.
157.
158.
162.
160.
159.
159.
162.
161.
165.
164.
164.
164.
167.
167.
167.
171.
170.
169,
169,
170.
171.
174.
172.
172.
175.
182.
182.
157.
156.
154.
152.
157.
156.
155.
151.
151.
149.
150.
149.
108.
105.
103.
105.
106.
106.
106.
101.
200.
196.
196.
203.
199.
197.
196.
201.
199.
204.
203.
203.
203.
206.
207.
206.
215.
213.
212.
212.
213.
214.
221.
222.
223.
223.
229.
227.
87.
86,
85.
80,
86.
86.
85.
83.
. 83.
82.
83.
82.
82.
80.
79.
80.
80.
81.
81.
78.
110.
108.
109.
112.
109.
109.
109.
111.
110.
113.
112.
112.
112.
114.
110.
115.
119.
113.
117.
117.
118.
118.
122.
122.
123.
123.
126.
125.
**
**
**
**
**
**
**
*
**
*
*
**
**
*
**
**
**
**
**
**
**
**
**
*
**
*
**
**
**
**
**
**
**
**
**
**
*
**
**
*
*
**
**
*
**
**
**
**
163
KVB 6017-1216
-------
**
*
*«
*«
*
** DATE
15 HIM. DATA
D*» STACK CAS CONCENTRATION
02 C02 NO
LOAD VOLX VOLI PPMV
TIME NNTH MEA3 MEAS M£AS
NO
PPHV
3tQ«*
NO
NG/J
**
»
»*
**
**
»*
ft*************************************************************
** «/
«* «/
4/
* «/
4/
** /
* 4/
4/
*« «/
« /
* /
* 4/
* 4/
* «/
** «/
* 4/
* «/
*« «/
* «/
** «/
** «/
.* «/
«* 4/
* 4/
** 4/
* 4/
« 4/
** «/
« «/
* 4/
** «/
« /
** 4/
* 4/
*« 4/
* 4/
* 4/
4/
* 4X
« «/
** 4/
** 4/
* 4/
*« 4/
4/
** 4/
«* 4/
** »/
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
8/79
iais
1230
12*5
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
164S
1700
1715
1730
1745
1800
1815
1830
1845
19QO
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
20.8 6.3
20.8 .2
20.8 .2
20.8 .1
20.5 .2
20.5 .2
20.5 6.2
20.5
20.5
20.5
20.5
20.5
1«.9
19.9
19.9
1«.9
19.9
19.9
1«.9
19.9
20.4
20.4
20.4
20.4
20.8
20.8
20.8
20.8
21.1
21.1
21.1
21.1
21.1
21.1
21.1
21.1
20.5
20.5
20.5
20.5
20.4
20,4
20.4
20.4
20.8
20.8
20.8
20.8
.3
.2
.3
.3
.4
.3
.7
.8
.7
.6
.6
.6
.7
.6
.6
.6
.6
6
.6
.6
.5
.5
6
.7
.4
.4
.4
.3
.6
.7
.8
.6
.7
.»
.4
.4
.3
.«
.4
.3
.5
10.6
10. a
10.9
10.9
10.9
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.7
10.6
10.6
10.7
10.4
10.4
10.5
10.4
10.5
10.5
10.5
10.5
10.5
10.6
10.6
10.6
10.6
10.4
10.5
10.5
10.5
10.4
10.2
10.1
10. 1
10.2
10.2
10.0
10.0
10.2
10.3
10.4
10.3
10.3
182.
164.
184.
182.
180.
180.
179.
177.
176.
177.
179.
181.
170.
164.
160.
1S4.
152.
181.
175.
175.
175.
174.
171.
169.
166.
166,
165.
164.
177.
175.
184.
184,
187.
189,
189.
191.
194.
f*.
197.
200.
202.
202,
199.
199,
199.
199.
200.
199.
222.
225,
224.
221.
219.
219.
219.
217.
215.
217.
219.
223.
208.
206.
203.
194.
191.
227.
218.
221.
219.
217.
214.
211.
208.
207.
206.
204.
221.
219.
232.
228.
232.
234.
232.
240.
245.
250.
246.
253.
257.
250.
245.
244.
2«6.
245.
244.
247.
123.
124.
124.
122.
Ul.
121.
121.
120.
118.
120.
121.
123.
115.
114.
112.
107,
105.
125.
120.
122.
121.
120.
118.
116.
115.
114.
114.
113.
122.
121.
128.
126.
128.
129.
128.
132.
135.
138.
136.
140.
142.
138.
135.
134.
136.
135.
135.
136.
»*
**
*«
**
*«
*
*
*
»*
**
**
**
*«
*
**
**
**
**
*
*
*
*
*
*
**
**
*
**
*
»*
»*
*
*
**
*
*
*
»«
*
**
*«
**
*«
*
*
*«
*************«*******************************«
164
KVB 6017-1216
-------
ft*
**
ft*
ft*
ft*
DATE
15 MIN
DRY STACK GAS
02
LOAD VOLX
TIME MKTH MEAS
. DATA
CONCENTRATION
C02 NO
VOCX PPMV
MEAS MEAS
NO
PPMV
3X0*
NO
NG/J
**
**
**
ft*
**
**
ft**************************************************************
ft*
ft*
ft*
ft*
ft*
ft*
**
**
**
*
ft*
**
**
ft*
ft*
ft*
ft*
*
ft*
**
ft*
**
**
**
*
**
**
**
**
**
**
**
**
**
*
**
**
**
**
ft*
**
*
ft*
ft*
**
««
**
ft*
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
4/
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
9/79
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
20.2
20.2
20.2
20.2
20.2
20.2
20.2
20.2
20.1
20.1
20.1
20.1
20.1
20.1
20.1
20.1
19.3
19.3
19.3
19.3
21.1
21.1
21.1
21.1
21.1
21.1
21.1
.1
.1
.1
.1
.1
.1
.1
.1
.1
.1
.1
.1
1
.1
. 1
.0
.0
.1
.1
.2
.4
.1
.1
.0
.2
.1
.1
21.1 6.1
20.9 6.2
20.9 6.1
20.9 6.1
20.9 6.1
20.8 6.1
20.8 6.2
20.8 6.1
20.8 6.1
20.8 6.1
20.8 6.3
20.8 6.1
20.8 6.3
20.9 6.4
20.9 6.3
20.9 6.3
20.9 6.4
21.1 6.4
21.1 6.3
21.1 6.3
21.1 6.3
10.3
10.1
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.5
10.5
10.2
10.2
10.5
10.5
10.5
10.3
10.4
10.3
10.3
10.3
10.3
10.5
10.2
10.2
10.3
10.3
10.3
10.1
10.4
10.8
10.8
10.7
10.8
10.8
10.8
10.8
201.
201.
204.
204.
204,
204.
204.
205.
200.
200.
201.
200.
197.
199.
199.
197.
196.
195.
195.
196.
195.
195.
194.
192.
192.
195.
196.
196,
194.
195.
192.
192.
193.
194.
195.
194.
195.
197.
194.
177.
179.
176,
175.
174.
174.
172.
172.
175.
24«.
243.
247.
248.
247.
248.
248.
248.
242.
242.
243.
241.
239.
242.
240.
236.
236.
235.
236.
239.
241.
236.
235.
231.
234.
237.
238.
236.
237.
235,
233.
233.
234.
237.
235.
234.
235.
241.
234.
217.
221.
215.
215.
216.
214.
210.
211.
214.
134.
134.
136.
137.
136.
137.
137.
137,
134,
134.
134.
133.
132.
134.
132.
130.
130.
130.
130.
132.
133.
130.
129.
127.
129.
130.
131.
130.
131.
130.
129.
129.
129.
131.
130.
129.
130.
133.
129.
120.
122.
119.
119.
119.
118.
116.
116.
118.
ft*
ft*
**
**
*«
**
**
**
**
**
ft*
**
**
*
**
**
*
**
**
*
**
*
**
**
**
**
**
**
**
**
**
*«
**
*«
**
*«
**
**
**
**
**
**
*
**
**
*
**
**
a***********************************************************
165
K7B 6017-1216
-------
ft**************************************************************
**
**
»*
ft*
**
**
OATI
15 "IN. DATA
DRY STACK GAS CONCENTRATION
02 C02 NO
LOAD VOLX VOLX PPHV
TI»e MNTH »EA3 NCAS MEAS
NO
PPMV
3X0*
NO
NG/J
**
»
**
**
*«
*«
ft***********************************************!!**************
**
**
**
*»
**
ft*
*«
**
**
ft
ft
**
ft
ft
*
ft
*
ft
ft
*
ft
*
ft
ft
»
*
ft
»*
*
ft
ft
ft
**
ft
ft
**
ft
*
**
*
ft
ft
**
**
4X
4X
4X
«/
4X
«/
4X
/
4X
4/
4/
4/
4/
4/
4/
4/
4/
4X
4X
4/
4/
4/
«/
4/
4/
4X
4X
4/
4X
4/
4/
4/
4/
4/
4/
4/
4/
4/
4X
4X
4/
4/
4/
4/
4/
4/
4/
4/
9/79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9x79
9X79
9X79
»X79
9x79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
9X79
1215
1230
1245
1300
1315
1330
1345
1400
1415
1430
1445
1500
1515
1530
1545
1600
1*15
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
21.1 6.3
21.1 6.3
21.1 6.4
21.
21.
21.
21.
21.
21.
21.
21.
21.
21.
21.
21.
21.
21.5
21.5
21.5
21.5
21.5
21.5
21.5
21.5
21.5
.4
.3
.3
.3
.3
.2
.2
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.3
.4
21.5 6.4
21.5 6.4
21.5 .5
21.1 .7
21.1 .7
21.1 .4
21. «
20. .4
20. 6.4
20. 6.6
20. 6.5
19. 6.9
19. 7.0
19. 6.6
19. 6.7
19. 6.6
1«». *.6
19. 6.6
1*. 6.7
20.2 6.6
20.2 6.6
20.2 6.6
20.2 6.6
10.8
10.8
10.8
10.8
10.7
10.7
10.7
10,7
10.7
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.7
10.6
10.9
10.9
10.9
10.8
10.8
10.8
10.6
10.6
10.8
10.9
10.9
10.9
10.8
10.8
10.8
179.
179.
179.
179.
180.
180.
181.
180.
182.
182.
181.
181.
184.
180.
1^9.
180.
181.
184,
182.
185.
185.
185.
187.
188.
188.
188.
188.
188.
190.
189.
175.
181.
181.
179.
176.
175.
174.
172.
170.
170.
170.
177.
177.
177.
178.
179.
179.
181.
218.
220.
221.
222.
221.
221.
221.
220.
222.
222.
221.
221.
225.
221.
219.
221.
223.
226.
224.
227.
227.
228.
230.
231.
231.
232.
232.
234.
240.
238.
216.
224.
224.
222.
221.
218.
222.
222.
213.
211.
212.
221.
222.
223.
223.
225.
225.
227.
120.
121.
122.
122.
122.
122.
122.
121.
122.
123.
122.
122.
124.
122.
121.
122.
123.
12«.
121.
125.
125.
126.
127.
127.
128.
128.
128.
129.
133.
131.
119.
123.
123.
122.
122.
120.
122.
122.
118.
118.
117.
122.
122.
123.
123.
124.
124.
125.
*
*
*«
*
*
*
**
*
«*
**
«
*
«*
«
*
**
**
**
**
**
*
**
**
**
**
**
**
**
**
*
*
**
**
**
*
*
**
**
**
**
**
*
*
ft***********************
166
KVB 6017-1215
-------
**
**
ft*
ft*
ft*
« DATE
15 HIK
DRY STACK GAS
TIME
LOAD
MMTH
02
VOLZ
HEAS
1. DATA
CONCENTRATION
C02
VOUJ
HEAS
NO
PPMV
HEAS
NO
PPHV
3X0*
NO
NG/J
*
**
**
**
ft**************************************************************
** 4/10/79
»* 4/10/79
ft* 4/10/79
* 4/10/79
4/10/79
4/10/79
** 4/10/79
ft* 4/10/79
** 4/10/79
4/10/79
** 4/10/79
* 4/10/79
** 4/10/79
* 4/10/79
4/10/79
* 4/10/79
** 4/10/79
« 4/10/79
ft* 4/10/79
»« 4/10/79
* 4/10/79
4/10/79
** 4/10/79
ft* 4/10/79
** 4/10/79
*« 4/10/79
*« 4/10/79
* 4/10/79
*« 4/10/79
** 4/10/79
** 4/10/79
ft* 4/10/79
** 4/10/79
ft* 4/10/79
* 4/10/79
* 4/10/79
4/10/79
* 4/10/79
* 4/10/79
* 4/10/79
** 4/10/79
* 4/10/79
** 4/10/79
** 4/10/79
** 4/10/79
« 4/10/79
« 4/10/79
** 4/10/79
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
- BOO
815
830
845
900
915
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
18.5
18,5
18.5
18.5
17.6
17.6
17.6
17.6
17.3
17.3
17.3
17.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
-.3
19.3
19.3
19.3
19.3
19.6
19.6
19.6
19,6
19.6
19.6
19.6
19.6
19.6
19.6
19.6
19.9
19.9
19.9
19.9
20.1
20.1
20.1
20.1
20.1
20.1
20.1
20.1
6.5
6.5
6.4
6.5
6.3
6.2
6.3
6.3
6.3
6.4
6.5
6.7
6.5
6.5
6.3
6.5
6.6
6.9
6.9
7.2
7.2
7.4
7.0
7.0
6.9
6.9
7.0
6.9
6.8
6.9
6.9
6.9
6.9
6.9
6.9
6.9
7.0
6.9
6.9
6.9
6.9
6.7
6.7
6.9
6.9
6.5
6.3
6.3
10.8
10.8
10.8
10.8
10.9
10.9
10.9
11. 0
10.9
11.0
10.9
10.9
10.8
10.8
10.9
10.9
10.9
10.9
10.4
10.4
10.5
10.7
10.5
10.3
10.5
10.5
10.6
10.7
10.6
10.6
10,8
10.8
10.7
10.7
10.7
10.7
10.7
10.7
10.7
10.7
10.4
10.2
10.2
10,3
10.3
10,3
10.2
10.4
181.
183.
183,
184.
182.
181.
180.
177.
177.
174.
175.
172.
172.
171.
174.
174.
174.
175.
177.
178.
189.
189.
189.
189.
191.
190.
188.
188.
188.
190.
190.
190.
191.
194.
197.
201.
205.
207.
188.
182.
187|
184.
185.
183.
180.
182.
225.
228.
227.
228.
222.
221.
221.
218.
217.
214.
218.
216.
214.
212.
214.
216.
217.
225.
228.
232.
247.
251.
243.
243.
245.
244.
241.
241.
238.
2«2.
242.
2«2.
244.
247.
253.
257.
264.
265.
240.
233.
236.
235.
233.
236.
235.
224.
222.
223.
124.
126.
125.
126.
122.
122.
122.
120.
120.
118,
120.
119.
118.
117.
118.
119.
120.
124.
126.
128.
136.
139.
134.
134.
135.
135.
133,
133,
131.
134.
134.
134.
135.
136.
140.
142.
1«5.
146.
132.
128.
130.
130.
129.
130.
129.
123.
122.
123.
*«
**
*
*
*
*
*
**
**
**
*
*
**
**
**
**
**
*
*
**
*
**
*
*
**
**
**
**
*
**
**
**
*
**
*
*
**
*
*
*
**
**
167 KVB 5017-1216
-------
ft**************************************************************
ft*
ft*
ft*
ft*
ft*
* DATE
* ******** ft *ft1
ft* 4/10/79
** 4/10/79
ft* 4/10/79
* 4/10/79
4/10/79
* 4/10/79
ft* 4/10/79
* 4/10/79
** 4/10/79
* 4/10/79
ft* 4/10/79
* 4/10/79
»* 4/10/79
4/10/79
4/10/79
* 4/10/79
* 4/10/79
* 4/10/79
* 4/10/79
ft* 4/10/79
ft* 4/10/79
ft* 4/10/79
ft* 4/10/79
ft* 4/10/79
* 4/10/79
ft* 4/10/79
ft* 4/10/79
* 4/10/79
ft* 4/10/79
ft* 4/10/79
* 4/10/79
* 4/10/79
** 4/10/79
ft* 4/10/79
ft* 4/10/79
4/10/79
* 4/10/79
* 4/10/79
ft* 4/10/79
ft* 4/10/79
ft* 4/10/79
ft* 4/10/79
ft* 4/10/79
** 4/10/79
ft* 4/10/79
* 4/10/79
* 4/10/79
** 4/10/79
15 "IN. DATA
DRY STACK GAS CONCENTRATION
TIME
******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
2245
2300
2315
2330
2345
2400
LOAD
HfcTH
r :*****
20.1
20.1
20.1
20.1
19.9
19.9
19.9
19.9
20.1
20.1
20.1
20.1
20.1
20.1
20.1
20.1
20.1
20.1
20.1
20.1
19 3
19!3
19.3
1' 3
1«.3
19.3
1*.3
19 8
19*8
19,8
19.6
19.6
S',3
I9. 3
S.i
f.5
I'.S
19 6
19*6
19.6
19.6
02
VOL*
MEAS
*******
6.3
6.2
6.2
6.2
1.0
6.3
6.9
6.4
6.4
6.4
6.4
6.4
6.7
6.8
6.9
6.8
6.8
6.8
6.9
6.9
7.1
7.1
7.1
6.9
6.9
7.2
7.1
7*.0
7.0
7.0
7.1
7.3
7.4
7.4
7.4
7.4
7.5
7.5
7.2
7.2
7.4
7.2
7.1
7.1
7.1
7.3
7.3
C02
VOL*
MEAS
*******
10.4
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.5
10.2
10.2
10.2
10.2
10.2
10.2
10.3
10.3
10.4
10.5
10.4
10.4
10.3
10.3
10.2
10.3
10.5
10.4
10.3
10.3
10.5
10.5
10.3
10.4
10.4
10.4
10.3
10.2
10.3
10.3
10.3
10.2
10.3
10.5
10.4
10.4
10.6
10.6
NO
PPMV
MEAS
*******
181.
181.
182.
180.
184.
185.
186.
188.
188.
188.
191 .
1'2.
187.
186.
187.
187.
186.
184.
184.
183.
183.
179.
177.
179.
177.
176.
176.
174.
175.
173.
170.
170.
171.
170.
167.
167.
167.
167.
167.
165.
165.
165.
166.
165.
166.
170,
174,
172.
NO
PPMV
3*02
*******
221.
221.
222.
220.
156.
228.
239.
232.
232.
232.
236.
237.
237.
236.
238.
237.
236.
234.
236.
235.
237.
232.
229.
229.
227.
230.
228.
222.
225.
223.
219.
221.
225.
226.
223.
223.
222.
222.
223.
216.
217.
219.
218.
215.
215.
221.
229.
227.
NO
NG/J
*******
122.
122.
122.
121.
86.
126.
132.
128.
128.
128.
130.
131.
131.
130.
131.
131.
130.
129.
130.
130.
130.
128.
126.
126.
125.
127.
126.
122.
124.
123.
121.
122.
124.
125.
123.
123.
123.
123.
123.
119.
120.
121.
120.
11'.
118.
122.
126.
125.
*
**
**
**
**
**
***
**
**
**
**
**
**
*
**
**
*
**
**
*
**
**
«
**
*»
*
**
*
*
*«
**
**
**
*
*
**
**
*
*
**
**
*«
**
**
*«
ft*
ft*
**
**
**
**
*
**
**
**
168
K7B 5017-1216
-------
ft*
ft*
ft*
ft*
ft*
*
ft*1
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*
**
15 *IN, DATA
DRY STACK GAS CONCENTRATION
DATE
'ftftftftftftftftft
4/U/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/H/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
4/11/79
TIME
fcft ft ft ft ft
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
02
LOAD VOLX
MHTH MEAS
ftftftftftftftftftftftftftl
13.2 7.4
13.2 7.4
13.2 7.4
13.2 7.3
13.8 7.6
13.
13.
13.
14.
14,
14.
1«.
16.
16.
16.
16.
18.
18.
18.
18.
16.
16.
16.
16.
16.
16.
16.
16.
15.
15.
15.
15.
14.
14,
14.
14,
14,
14,
1«.
14,
13.
13.
13.
13.
13.
13.
13.
13,
7.6
7.4
7.3
7.2
7.1
7.1
7.2
7.2
11.0
10.5
9.5
9.2
10.0
11.0
10.9
10.9
10.5
10.1
10. 1
10.0
10.0
10.0
9.4
9.4
9.7
10.2
10.4
10.4
10.5
10.3
10.1
10.6
11.0
11.0
10.5
9.8
10.0
10.3
10.2
10.2
10.5
10.6
10.4
C02
VOLX
MEAS
rftft ftftft *i
10.6
10.5
10.4
10.3
10.4
10.1
10.2
10.4
10.5
10.6
10.6
10.6
10.5
10.6
7.9
7.9
8.5
8.9
8.5
7.4
7.4
7.5
7.5
8.2
8.3
.3
.3
.3
.8
.9
.9
.4
.3
.2
8.1
8.1
8.4
8.5
7.9
7.6
7.5
7.8
8.3
8.1
7.9
7.8
7.9
7.6
NO
PPMV
MEAS
ftft ftAft A '
170.
170.
171.
169.
167.
164.
161.
171.
171.
170.
171.
155,
147.
75.
130.
157.
140.
139.
131.
132.
132.
132.
136.
127.
120,
115.
117.
124.
125.
122.
117.
115.
114.
105.
102.
105.
106,
135.
137.
145.
148.
148.
HI.
143.
143.
138.
135.
135.
NO
PPMV
3X0*
rft ft Aft ftft ft
226.
226.
227.
223.
224.
221. .
213.
225.
223.
221.
222.
202.
193.
136.
224.
247.
215.
228.
237.
238.
238.
228.
225.
211.
198.
190.
193.
194.
196.
197.
197.
196.
195.
181.
172.
174,
184.
244.
247.
250.
239.
245.
239.
241.
240.
240.
234.
231.
NO
NG/J
** *
125.
125.
125.
123.
123.
122.
118.
124.
123.
122.
123.
111.
107.
75.
123.
136.
119.
126.
131.
131.
131.
126.
124.
117.
109,
105.
106.
107.
108.
108,
108,
108.
107,
100.
95.
96.
102.
135.
136.
138.
132.
135.
132.
133.
133.
132.
129.
127.
*
*
*
*
»
**
**
*
*
*
*
**
**
*
*
*«
*
**
*
*
*«
*
*«
ft*
*
**
*
*«
*
ft*
«
ft*
*
*
*
*
*
*«
*
*
*
ft**************************************************************
169
KVB 6017-1216
-------
*««*<
*
ft*
**
ft*
* DATE
*******»***i
4/11/79
** 4/11/79
4/11/79
4/11/79
** 4/11/79
* 4/11/79
* 4/11/79
4/U/79
** 4/11/79
4/U/79
* 4/11/79
4/11/79
** 4/11/79
* 4/11/79
4/11/79
«/ll/7t
* 4/11/79
* 4/11/79
* 4/11/79
* 4/11/79
* 4/11/79
* 4/U/79
** 4/11/79
* 4/11/79
** 4/11/79
* 4/11/79
* 4/11/79
* 4/11/79
* 4/11/79
** 4/11/79
* 4/11/79
* 4/11/79
4/11/79
** 4/11/79
** 4/11/79
** 4/11/79
** 4/11/79
4/11/79
4/11/79
« 4/11/79
** 4/11/79
** 4/11/79
4/11/79
* 4/11/79
* 4/11/79
» 4/11/79
4/11/79
* 4/11/79
I************************* ft******** *****,
15 H1N. DATA
DRY STACK GAS CONCENTRATION
TIKE
»*****
1215
1230
120S
1300
1315
1330
13«S
1400
1415
1430
1445
1500
1515
1530
1545
1600
1615
1630
1645
1700
1715
1730
1745
1000
1815
1830
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
L"AO
H*»TH
******<
1«.5
14.5
14.5
14.5
13.5
13.5
13.5
13.5
11.7
11.7
11.7
11.7
12.3
12.3
12.3
12.
12.
12.
12.
12.
13.2
13.2
13.2
13.2
12.7
12.7
12.7
12,7
12.
12.
12.
12.
I4.
1«.
1«,
1«,
11.
11.
11.
11.
10.
10.5
10. 5
10.5
11.4
11.4
11.4
11.4
02
VOLX
ME A3
»»»»**«i
10.4
10.3
10.4
10.5
10.7
10.7
10.7
11.3
11.7
11.3
11.2
12.0
11.3
10.7
10.7
11.7
11.4
11.0
11.5
9.5
10.2
10.6
10.6
10.6
10.7
10.7
10.6
10.9
11.2
10.7
10.5
11.0
10,9
10.2
9. «
9.8
9.8
13.8
11.2
10.5
10.0
.5
.5
1 .7
1 .0
.0
.2
.5
C02
VOLZ
MEAS
>****<
7.6
7.6
7.6
7.5
7.6
7.5
7.4
7.7
7.7
7.0
6.9
7.0
7.0
6.7
6.8
7.5
7.1
6.6
7.1
7.2
6.9
8.1
7.7
7.6
7.6
7.6
7.6
7.6
7.6
7.5
7.3
7.6
7.7
7.«
7.5
7.9
.4
.4
.4
.9
.0
.7
.1
.3
.6
.9
.5
.9
NO
PPWV
HEAS
»******i
135.
134,
134,
134.
131.
131.
140.
125.
120.
122.
124.
11«».
120.
125.
130.
115.
117.
124.
11«.
137.
137.
135,
136.
136.
137.
137,
136,
136,
125,
132.
134.
129.
126.
132,
142.
141.
142.
89.
120.
130.
120.
85.
82.
77.
117.
120.
119,
125.
NO
PPHV
3X02
H»»»*»*1
229.
226.
227.
231.
231.
230.
2«7.
233.
235.
228.
230.
237.
224.
220.
229.
225.
221.
225.
226.
216.
231.
235.
237.
238,
240.
239.
237.
2«3.
232.
233.
231.
233.
227.
221.
229.
228.
229.
224.
223.
224.
197.
133.
130.
137.
193.
180.
182.
196.
I**********
**
*
NO
NG/J
!******<
126.
125.
125.
127.
128.
127.
136.
129.
I2<».
126.
127.
131.
124.
122.
126.
124.
122.
124.
125.
119.
127.
130.
131.
131.
132.
132.
131,
134,
128,
128,
128.
128.
125,
122,
126.
126,
126.
123.
123.
123.
109.
74.
71.
75.
106.
99.
100.
108.
**
*
**
»
>***
**
**
»*
*
**
*
*
*
»*
*
*
*«
*
«
**
*
»*
**
**
**
**
**
«
**
**
«
*
**
*
*
*
»
**
**
**
**
*
ft*
**
ft*
**
**
A********************************************************
170
K7B 6017-1216
-------
**
**
**
**
**
** DATE
vftftAA4kAA4k^9^
** 4/12/79
* a/12/79
** 4/12/79
** 4/12/79
** 4/12/79
* 1/12/79
* 4/12/79
* 4/12/79
** 4/12/79
* 4/12/79
«« 4/12/79
4/12/79
* 4/12/79
** 4/12/79
** 4/12/79
** 4/12/79
** 4/12/79
*« 4/12/79
** 4/12/79
** 4/12/79
** 4/12/79
«* 4/12/79
** 4/12/79
* 4/12/79
*» 4/12/79
* 4/12/79
«« 4/12/79
** 4/12/79
* 4/12/79
** 4/12/79
** 4/12/79
** 4/12/79
* 4/12/79
* 4/12/79
*» 4/12/79
* 4/12/79
* 4/12/79
** 4/12/79
** 4/12/79
4/12/79
* 4/12/79
»* 4/12/79
*« 4/12/79
4/12/79
4/12/79
ft» 4/12/79
** 4/12/79
* 4/12/79
15 HIM. DATA
DHT STACK GAS CONCENTRATION
TIME
ft A^ft Aft
15
30
4S
100
115
130
145
200
215
230
205
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
M»TH
*******
16.4
16.0
16.4
16.4
16.3
16.3
16.3
1<>.3
16.3
16.3
16.3
16.3
18.3
1«.
18.
18.
1".
1*.
I".
I".
19.0
19.0
i9.o
19.0
I9.o
19.0
19.0
19.0
19.6
19.6
1'.6
19.6
1".3
19.3
1«.3
1".3
I'.S
1^.3
1'.3
1*.3
1«.6
19.6
1".
1«.
17.
17.
17.
17.
02
von
MEAS
ft****#l
9.7
9.9
10.1
10.0
10.1
12.2
10.0
9.8
10.0
10.2
10.1
10.0
9.9
10.2
.2
.5
.6
.6
.T
.7
.6
.7
.6
.7
.7
.7
.*
.6
7.9
7.7
7.7
7.7
7.7
7.7
7.9
8.0
7.-»
8.0
7.8
10.0
7.6
7.7
7.6
7.5
7.2
7.2
8. a
8.4
C02
VULZ
MEAS
#***#*!
9.1
M
9.0
8.7
8.5
a. 3
8.3
8.2
8.2
«.2
8.2
8.3
8.2
8.1
8.2
8.2
8.2
8.0
8.7
9.4
9.3
9.3
9.3
9.3
9.3
9.3
9.4
9.
9.
9.
9.
9.
9.9
10.0
10,0
10.0
10.0
10.1
10.0
10,0
10.0
9.9
10.0
10.0
10.2
10.1
10.2
10.1
NO
PPHV
MEAS
#*****'
131.
135.
lao.
1«S.
109,
146.
106.
146.
147.
152.
156.
160.
158.
160.
165.
182.
181.
182.
182.
182.
180.
176.
180,
182.
182.
181.
182.
182.
18S.
186.
186.
186.
188.
185.
179.
179.
180,
181.
181.
189.
188.
188.
188.
189.
192.
191.
186.
167.
NO
PPHV
310*
'< A **1k*1
211.
219.
233.
237.
246.
300.
240,
236.
243.
255.
260.
263.
258.
268.
25«.
263.
264.
267.
267.
267.
263.
258.
262.
266.
266.
265.
265.
266.
255.
253.
253.
252.
256.
251.
2«5.
248.
249.
250.
248.
311.
251.
255.
252.
252.
252.
250.
269.
240.
NO
NG/J
'A *****)
116.
121.
128.
131.
136.
165.
133.
130.
134,
140,
1«3.
105.
1«2.
148.
100.
105.
106.
107.
107.
107.
105.
102.
1«5.
107.
107.
106.
106.
106.
l«t.
139.
139.
139.
101.
139,
135.
137.
137.
138.
137.
171.
139.
101.
139.
139.
139,
138.
108.
133.
**
**
*«
**
**
**
***
**
**
**
**
**
«*
**
**
**
*
**
*
**
**
**
**
*
**
**
**
**
*»
**
**
**
**
*»
**
**
**
**
*
»*
*
»»
*«
*»
**
**
»*
**
*
**
**
**
**
*
**
171
K7B 6017-1216
-------
************************************************************
** 15 "IN. DATA
** Df»r STACK GAS CONCENTRATION
**
*
** DATE
TIME
LOAD
W"TH
02
VOL*
ME AS
C02
VOLX
NEAS
NU
PPHV
MEAS
NO
PPMV
3*02
NO
NG/J
*
**
»*
**
*
**
*
***************************************************************
* 4/12/79
» 4/12/79
** 4/12/79
* 4/12/79
** 4/12/79
* 4/12/79
** 4/12/79
** 4/12/79
** 4/12/79
* 4/12/79
4/12/79
** 4/12/79
** 4/12/79
** 4/12/79
* 4/12/79
* 4/12/79
* 4/12/79
4/12/79
4/12/79
** 4/12/79
* 4/12/79
4/12/79
* 4/12/79
*« 4/12/79
4/12/79
* 4/12/79
** 4/12/79
** 4/12/79
** 4/12/79
* 4/12/79
** 4/12/79
** 4/12/79
** 4/12/79
* 4/12/79
»* 4/12/79
4/12/79
4/12/79
4/12/79
»« 4/12/79
«* 4/12/79
* 4/12/79
* 4/12/79
* 4/12/79
* 4/12/79
* 4/12/79
» 4/12/79
« 4/12/79
* 4/12/79
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
1»15
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
224S
2300
2315
2330
2345
2400
15.8
15.8
15.8
15.8
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.3
16.4
16,4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.3
16.3
16.3
16.3
16.3
16.3
lfc.
16.
16.
16.
16.
16.
16.
16.3
16.3
1*.3
8.0
8.5
8.2
7.7
7.6
7.6
7.6
7.6
7.6
7.5
7.5
7.5
7.5
7.5
7.6
7.5
7.2
7.4
7.«
7.4
7.3
7.2
7.1
7.1
7.1
7.1
7.1
7.0
7.0
7.0
7.1
7.6
7.3
7.5
7.5
7.5
7.5
7.5
7.5
7.3
7.5
7.5
7.5
7.5
7.5
7.5
7.5
7.S
10.3
10.3
9.6
9.3
9.2
«>.2
9.6
«».8
9.9
9.9
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10,2
».»
9,9
9.9
9.9
».
«.»
«.»
«.
9>
9.9
9.9
9.9
9.9
153.
150.
160.
163.
165.
172.
159.
156.
154.
154.
152.
160.
162.
162.
152.
151.
152.
158.
155.
149.
152.
154.
154.
159.
157.
157.
157.
156.
154.
153.
153.
162.
157.
157.
158.
157.
157.
158.
157.
159.
159.
159.
158.
158.
157.
157.
160.
1S«.
220.
217.
226.
222.
222.
231.
213.
210.
207.
206.
203.
214.
216.
217.
205.
201.
200.
210.
206.
1*7.
201.
202.
200.
206.
203.
203.
203.
201.
199.
197.
!99.
217.
207.
210.
211.
210.
210.
211.
210.
212.
213.
212.
212.
212.
210.
210.
214.
213.
121.
119.
125.
123.
122.
127.
117.
116.
114.
113.
112.
tie.
119.
119.
113.
111.
110.
116.
114.
109,
111.
111.
110.
114.
112.
112.
112.
111.
110.
109.
110.
120.
114,
116.
117.
116.
116.
116.
116.
117.
117.
117.
U7.
117.
116.
116.
118.
117.
**
**
*
**
**
*
»
**
«»
*
**
**
*
»
**
»*
**
**
*
**
*
**
**
*
**
**
*
»
*
**
**
*
**
*
*
*
»*
**
**
**
*
*
**
172
KVB 6017-1216
-------
************
**
**
**
*
**
** OATE
************
*» 4/13/79
** 4/13/79
*« 4/13/79
»* 4/13/79
* 4/13/79
«« 4/13/79
** 4/13/79
* 4/13/79
* 4/13/79
» 4/13/79
* 4/13/79
* 4/13/79
* 4/13/79
4/13/79
* 4/13/79
** 4/13/79
* 4/13/79
** 4/13/79
*» 4/13/79
** 4/13/79
«« 4/13/79
** 4/13/79
** 4/13/79
*« 4/13/79
*« 4/13/79
** 4/13/79
» 4/13/79
** 4/13/79
»* 4/13/79
* 4/13/79
** 4/13/79
** 4/13/79
** 4/13/79
** 4/13/79
** 4/13/79
« 4/13/79
** 4/13/79
** 4/13/79
* 4/13/79
* 4/13/79
* 4/13/79
*« 4/13/79
** 4/13/79
« 4/13/79
*« 4/13/79
* 4/13/79
** 4/13/79
*« 4/13/79
a*************************************
15 MIN. DATA
DRY STACK GA3 CONCENTRATION
TIME
*******
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
BOO
815
830
845
900
915
930
945
1000
1015
1030
10«S
1100
1115
1130
1145
1200
LOAD
MMTH
*******
J8.5
18.5
1».5
18.5
18.8
18.8
18.8
18.8
18.8
18.8
18. 8
18.8
18,8
18.8
18.8
18.8
19.0
19.0
19.0
19.0
19.3
19.3
I*. 3
19.3
i9.8
19.8
1". 8
19.8
19.9
19.9
19.9
19.9
19.9
19.9
1*.*
19.9
I". 8
19.8
19.8
19.8
19.3
19.3
19.3
19.3
19.3
19.3
19.3
19.3
02
vouz
MEA3
*******
7.6
7.6
7.5
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.6
7.7
7.9
7.6
7.6
7.6
7.6
7.6
7.9
7.9
8.0
8.0
7.7
7.9
7.9
7.7
7.7
7.7
7,7
7.7
7.7
7.6
7.6
7.6
7.7
7.7
7.6
7.7
7.6
7.6
13.3
13.3
13.4
13.4
13.3
7.8
7.6
C02
VOLX
MEAS
A A* A A A A
rw w w w w w
9.9
9.9
9.9
9.9
«».
«».
».
"».
9.
9.
9.
9.
9.
9.
'.
».
.«
.8
.8
.*
.9
.«»
.»
10.0
10.0
9.9
9.9
9.9
. 10.1
10,0
10.1
10. t
10.2
10.2
10.2
10.2
10.1
10.2
10.2
10.2
10.2
10.2
10.2
10.1
10.1
10.1
5.9
5.8
NO
PPMV
MEA3
A A*** A
BfT w w w w m
160.
161.
161.
160.
159.
158.
159.
159.
159,
157.
157,
157.
157,
165.
177.
176,
175.
174,
177,
181.
180.
180.
179.
180.
180.
180.
177.
179.
177.
177.
179.
181.
183.
185.
187.
188.
I'M.
182.
179.
177.
179.
137.
97,
97.
97.
96.
166.
179.
NO
PPMV
3X0?
*ft *** A 4
216.
216,
215,
215,
214.
212.
214.
214.
213.
211.
211.
212.
214.
228.
238.
238.
237.
235.
240.
249.
249.
250.
249.
2«5.
249,
247.
239.
244.
240.
240.
244.
245.
247.
251.
252.
254.
259.
246.
2«3.
237.
241.
324.
229.
231.
232.
228.
227.
242.
**********
*«
**
NO
NG/J
*******
119.
11'.
H'.
119.
118.
117.
118.
118.
117.
116.
117,
117.
118.
126.
131.
131.
130.
130,
132.
137.
138.
138.
137.
135.
137.
136.
132.
135.
132.
132.
134.
135.
136,
138.
139.
140.
143.
135.
134.
131.
133.
179.
126.
127.
128.
126.
125.
133.
**
**
»*
**
***
*»
**
**
**
**
**
*
*»
*
**
**
*«
*
**
**
**
**
**
**
**
**
**
**
**
**
**
»*
*
**
**
**
*«
**
**
**
**
**
**
**
**
**
**
**
**
*«
**
*
173
KVB 6017-1216
-------
*****«**»*********»*»*»**«**«*»*»*******»»»»**»*»»«»*»»
ft
15 "in. DATA
* OR* STACK CAS CONCENTRATION
**
02 C02 NO
»* LOAD VOL* VOLX PPHV
*
AAi
WWl
ftft
ft
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
DATE
FftlkAAAAfe*'
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/13/79
4/J3/79
4/13/79
4/13/79
4/13/79
4/13/79
4/1J/79
4/13/79
4/13/79
4/13/79
TIHE
tfc****l
12J5
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
MNTH MEAS MEA3 MEAS
**ft**r
19!
I9.
l9.
19,
19.
|9,
19.
19,
19.
19,
19.
19.
l9.
19,
19.
19.
19.
19.
t*ww*vwwww**wi
7.7 5
7.6 5
IWW«««»W»««
,7 177.
,9 177.
7.5 7.9 179.
7.5 10
,3 179.
7.5 10.0 180.
7.4 9
7.5 9
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
7.
19^5 7.
19.5 7.
19.5 7.
19.5 7.
19.0 8.
19.0 11.
19.0 11.
19.0 11.
10,
i9 182.
.9 183.
,0 183.
10.0 104.
9,
,6 183.
10.2 183.
10. I 179.
10,
10,
10,
to,
10,
10,
10,
10,
.2 178.
,2 179.
,2 178,
,2 179,
,0 179.
0 178.
,1 177.
iO 178.
10.2 178.
10.2 179.
10
,3 179.
10.3 1?8.
to,
10,
10
.2 175.
2 145.
.2 116.
10.2 116.
1915 19.2 ii.2 10.2 117.
1930
19«S
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
19.2 11.2 10
19.2 11.2
19.2 11.2
19.0 11.2
19.0 11.2
19.0 11.2
19.0 11.2
18.5 11.2
18.5 11.2
18.5 11.2
18.5 11.2
18.5 11.2
18.5 11.2
18.5 11.2
18.5 11.2
18.5 11.2
18.5 11.2
18.5 11.2
18.5 11.2
.2 118.
120.
. 120.
, 119.
, 119.
, 119.
, 119.
119.
11*.
114.
i 11*.
116.
115.
114.
114.
tl«.
115.
115.
NO
PPMV
3X02
******1
241.
238.
239.
2«0.
241.
241.
244.
244.
245,
2«4.
243.
2«3.
242.
240.
240.
238.
237.
236.
236.
237.
238.
238.
239.
237.
243.
280.
221.
221.
218.
219.
223.
222.
221.
221.
221.
222.
220.
216.
211.
211.
212.
214.
213.
211.
211.
211.
212.
212.
HQ
NG/J
»******<
133.
131.
132.
132.
133.
133.
135.
134.
135,
134.
134.
134.
133.
132.
133.
131.
131.
130.
130.
131.
131.
131.
132.
131.
134.
154.
122.
122.
120.
121.
123.
122.
122.
122.
122.
122.
121.
119.
116.
116.
117.
118.
117.
116.
117.
116.
117.
117.
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*
*
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*
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**
**
ft***********************************
174
JCVB 6017-1216
-------
** IS «IN. OAT*
** DRT STACK GA3 CONCENTRATION
**
** 02 COS NO
** LOAD VOLX VOLX PPMV
* DATE TIME MHTH HEAS HEAS HE»3
A*********************************************
** 4/14/79
** OX
** OX
* ox
** ox
** ox
ox
** ox
*« ox
** ox
** ox
* ox
*« ox
* ox
* ox
ox
* ox
«» ox
* ox
** ox
* OX
»* ox
* ox
*« ox
*« ox
** ox
** ox
*« ox
** ox
OX
** ox
« OX
** ox
** ox
* ox
* ox
** ox
** ox
** ox
* ox
* ox
* ox
** ox
** ox
** ox
** ox
** ox
* ox
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
0X79
i5
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
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-.3
.0
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.0
.0
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.0
.0
.0
.0
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.0
.0
.0
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.0
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.0
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.0
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.0
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.0
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0.
o,
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0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
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0.
0.
0.
0.
0.
0.
0.
0.
0.
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0.
0.
0.
0.
0.
0.
0.
0.
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0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
NO
PPHV
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-It
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
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0.
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0.
0.
0.
0.
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0.
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0.
0.
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0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
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0.
0.
0.
0.
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NO
NG/J
******
1.
0.
0.
0.
0.
0,
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
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0.
0.
0.
0.
0.
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0.
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0.
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**
**
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*
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**
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**
*
**
**
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**
**
**
**
**
*
**
*
a*************************************
175
KVB 6017-1216
-------
*
**
**
*«
**
** DATE
»*»***»«»
** O/ 0/79
** O/ 0/79
** O/ 0/79
** O/ 0/79
** O/ 0/79
O/ 0/79
O/ 0/79
* O/ 0/79
O/ 0/79
O/ 0/79
* O/ 0/79
* O/ 0/79
O/ 0/79
O/ 0/79
* O/ 0/79
** O/ 0/79
** O/ 0/79
* O/ 0/79
* O/ 0/79
* O/ 0/79
* O/ 0/79
»* O/ 0/79
* 4/14/79
* 4/14/79
*« 4/14/79
* 4/14/79
« 4/14/79
* 4/14/79
** 4/14/79
4/14/79
* 4/14/79
** 4/14/79
»* 4/14/79
* 4/14/79
* 4/14/79
* 4/14/79
4/14/79
* 4/14/79
** 4/14/79
4/14/79
* 4/14/79
4/14/79
4/14/79
4/14/79
4/14/79
4/14/79
** 4/14/79
** 4/14/79
"
15 HI
DRV STACK GAS
****«*4
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
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
M»»TH
Iftft ft ft ft ft t
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
19.0
19.0
19.0
19.0
19.0
19.0
19.3
19.3
19.3
19.3
19.5
19.5
19.5
19.5
19.3
19.3
19.3
19.3
19.3
19.3
19.3
19.3
l9.o
19.0
19.0
19.0
02
VOLX
MEAS
t ft ft ft ft ft ft
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
7.0
6.8
6.8
6.7
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.7
6.6
6.5
6.6
6.6
6.6
6.6
6.6
6.6
6.7
6.9
7.0
7.1
7.3
7.2
N. DATA
CONCENTRATION
C02
VOL*
MEAS
ftftftftftftftftl
0
.0
.0
.0
.0
.0
.0
,0
.0
,0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
10.1
10.1
10.2
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.2
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.1
10.0
10.0
NO
PPMV
MEAS
****
0.
0.
0.
9.
0.
o.
0.
0.
0.
o.
0.
0.
0.
0.
o.
o.
0.
0.
0.
o*
0.
0.
177.
178.
175.
180.
184.
186.
187.
195.
192.
190.
189.
188.
186.
184.
182.
183.
185.
186.
186.
188.
183.
172.
169.
162.
159.
159.
NO
PPMV
3X02
*******
0.
0.
**
0.
o.
0.
0.
o.
o.
* *
0.
o.
o.
0.
0.
*
o.
0.
o.
0.
0.
0.
o.
0.
0.
229.
226.
222.
227.
231.
233.
235.
243.
239.
238.
236.
238.
234.
228.
227.
230.
231.
233.
233.
235.
232.
221.
218.
212.
210.
208.
*****"**»****»*************«»»** **«***«
NO
N6/J
*******
o.
.
0.
o.
0.
**
o>
Q%
o
o.
A
"
ot
o.
o.
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0.
0.
o.
o.
0.
0.
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126.
125.
123.
125.
128.
128.
130.
134.
132.
131.
130.
131.
129,
126.
125.
127,
127.
128,
129,
130,
128.
122.
120.
117.
116.
115.
*******
« w
*
»*
**
*
**
«*«
^
^
^
4*
^^
4*
4*
4*
B*
w*
t
^^
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^
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*
**
**
*
**
**
*
*
*
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*
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**
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**
**
*
*
**
*
**
*
*«*
176
KVB 6017-1216
-------
*********««**«*******«**************************************+
**
**
*
**
*
*« DATE
************
* 4/15/79
*« 4/15/79
** 4/15/79
** 4/15/79
** 4/15/79
* 4/15/79
*« 4/15/79
«* 4/15/79
*« 4/15/79
** 4/15/79
** 4/15/79
* 4/15/79
** 4/15/79
** 4/15/79
** 4/15/79
** 4/15/79
** 4/15/79
** 4/15/79
* 4/15/79
*« 4/15/79
** 4/15/79
* 4/15/79
«* 4/15/79
** 4/15/79
* 4/15/79
** 4/15/79
* 4/15/79
*« 4/15/79
** 4/15/79
** 4/15/79
** 4/15/79
** 4/15/79
* 4/15/79
»* 4/15/79
** 4/15/79
«* 4/15/79
4/15/79
** 4/15/79
* 4/15/79
** 4/15/79
» 4/15/79
4/15/79
** 4/15/79
** 4/15/79
** 4/15/79
** 4/15/79
** 4/15/79
* 4/15/79
IS "IN
DRY STACK GAS
T1HE
******!
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
9QO
915
930
945
1000
1015
1030
1045
1100
tits
1130
1145
1200
LOAD
MWTH
k******
18^2
18.2
ie|a
18.8
IB. 8
18.8
18.9
18.9
18.9
18,9
19^3
19,3
)9,3
19,6
19.6
l9«6
19.6
18.8
18.8
18.8
18,8
18.8
18. a
18.8
18.8
18.8
18.8
18.8
18.8
18.9
18.9
18.9
18.9
16.9
18.9
18.9
18.9
18. 8
18.8
18.8
18.8
18.8
18.8
18.8
18.8
02
VOLX
MEAS
*******
7.2
7.2
7.2
7.2
7.3
7.2
7.1
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.0
7.0
7.0
7.0
7.0
6.9
6.9
7.0
7.0
6.9
6.9
6,9
6.9
6.9
6.9
. DATA
CONCENTRATION
C02
VOLt
NEA3
** *****
10.0
10.0
9,9
9.9
10.0
9.9
10.0
10.0
9,9
10.0
10.0
10.0
10.0
10.0
10.0
10.0
9.9
10.0
10*0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
9.9
9.9
9.9
9.9
9.9
9.9
10.0
9.9
9.9
10.0
10.0
10.0
9.9
9.9
10.0
10.0
9.9
9.9
10.0
10.0
10.0
10.0
NO
PPMV
MEAS
*******
159.
158.
157.
156.
152.
152.
152.
152.
154.
154.
155.
156.
155.
155.
152.
152.
147.
149.
149.
150.
153.
155.
155.
155.
155.
155.
155.
155.
154.
156.
156.
158.
158.
160.
164.
165.
167.
169.
170.
169.
169.
167.
169.
170.
172.
174.
177.
177.
NO
PPMV
3*0*
, £* * ** **
207.
207.
206.
204.
201.
199.
198.
199.
201.
201.
202.
204.
202.
202.
199.
199.
192.
194.
193.
194.
199.
200.
200.
200.
200.
200.
200.
201.
200.
202.
202.
205.
205.
206.
211.
212.
216.
217.
218.
217.
217.
215.
217.
218.
221.
224.
227.
227.
NO
NG/J
*******
114.
114.
113.
113.
111.
110.
109.
110.
111.
111.
111.
112.
111.
111.
110.
110.
106.
107.
106,
107,
110.
110.
110.
110.
110.
110.
110.
111.
110.
111.
111.
113.
113.
114.
116.
117.
119.
120.
120.
120.
120.
119.
120.
120.
122.
123.
125.
125.
**
»*
*»
»*
«*
**
* * *
**
**
**
**
*
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**
**
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**
**
**
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**
**
**
**
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**
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**
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**
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**
**
**
**
**
*«
**
**
*
**
**
**
**
**
**
**
*
*
a**************************************************************
177
KVB 6017-1216
-------
**
*
**
*«
** DATE
15 HIN
DRY STACK GAS
TIME
LOAD
MKTH
02
VOCI
MEA3
1. DATA
CONCENTRATION
C02
VOLX
KEAS
NO
PPMW
MEAS
NQ
PPHV
3X0*
NO
NG/J
**
**
»*
*«
**
**
ft***************************************************
* 4/15/79
* 4/15/79
** 4/15/79
* 4/15/79
4/15/79
* 4/15/79
* 4/15/79
* 4/15/79
« 4/15/79
« 4/15/79
* 4/15/79
* 4/15/79
** 4/15/79
» 4/15/79
* 4/15/79
4/15/79
4/15/79
4/15/79
t* 4/15/79
« 4/15/79
* 4/15/79
4/15/79
* 4/15/79
«* 4/15/79
* 4/15/79
* 4/15/79
* 4/15/79
*« 4/15/79
* 4/15/79
»« 4/15/79
* 4/15/79
4/15/79
* 4/15/79
4/15/79
* 4/15/79
« 4/15/79
* 4/15/79
** 4/15/79
4/15/79
** 4/15/79
* 4/15/79
4/15/79
** 4/15/79
4/15/79
* 4/15/79
*« 4/15/79
* 4/15/79
4/15/79
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
i'.o
19.0
19.0
19.0
18.8
18.8
18.8
18.8
18.9
!«.»
18.9
18.9
I'.O
19.0
J9.0
19.0
19.0
19.0
19,0
J9.0
19.0
19.0
19.0
I'.O
j9.2
19.2
19,2
19,2
1*«5
1*.5
1* 5
19*5
i*.o
i*.o
1*».0
19.0
l*.0
I'.O
19.0
18.8
18.8
|8.8
18.9
18.9
l8,9
18,9
6.9
6.9
7.1
7.3
7.4
7.4
7.5
7.4
7.0
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.2
7.3
7.3
7.3
7.4
7.4
7.4
7.3
7.3
7.4
7.4
7.4
7.5
7.6
7.6
7.6
7.6
7.5
7.6
7.5
7.6
7.7
7.7
7.6
7.6
7.5
7.5
7.5
7.6
7.7
7.9
10.0
10.0
10.0
10.0
10.1
10.0
10.0
9.9
9.9
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.1
10.0
10.0
10.0
10.0
10.0
10.1
10.1
10.1
10.1
10.0
10.0
10.0
9.9
10.1
10.1
10.1
10,0
172.
172.
172.
177.
179.
179.
175.
175.
175.
179.
181.
181.
180.
180.
182.
183.
182.
182.
180.
180.
177.
175.
175.
175.
175.
174.
173.
174,
170.
170.
1*'.
169.
1*8.
1*7.
1*7.
1*7.
167,
167.
169.
170.
1*7.
169.
1*7.
1*8.
170.
1*7^
1*2.
221.
220.
223.
234.
237.
239.
234.
233.
225.
234.
236.
236.
235.
235.
238.
2«0.
239.
239.
236.
237.
234.
231.
231.
231.
230.
229.
229.
230.
226.
228.
227.
228.
227.
225.
224.
225.
224.
225.
228.
230.
226.
228.
224.
225.
227.
228.
227.
223.
122.
121.
123.
129.
131.
132.
129.
128.
124.
129.
130.
130.
129.
129.
131.
132.
132.
132.
130.
131.
129.
127.
127.
127.
127.
126.
126.
127.
125.
126.
125.
126.
125.
124,
124,
124.
123.
124.
126.
127.
125.
126.
123.
124.
125.
125.
125.
123.
*«
**
**
**
**
*
*«
**
*
*
**
*
*
*
*
**
*
**
*
**
**
*»
**
*
*»
**
*
*
*
*
**
**
*
*
*
**
*
**
**
*
***«******«******«******«***«****«**«*******«*****
178
KVB 6017-1216
-------
»*****»**««**«*
**
**
*
*«
»*
*« DATE
Aftlkft'ftifrAAftA'ftA
* 4/16/79
** 4/16/79
»* 4/16/79
*« 4/16/79
* 4/16/79
« 4/16/79
* 4/16/79
** 4/16/79
* 4/16/79
« 4/16/79
* 4/16/79
** 4/16/79
* 4/16/79
* 4/16/79
*« 4/16/79
** 4/16/79
* 4/16/79
** 4/16/79
»* 4/16/79
** 4/16/79
** 4/16/79
* 4/16/79
* 4/16/79
** 4/16/79
* 4/16/79
** 4/16/79
*« 4/16/79
4/16/79
** 4/16/79
* 4/16/79
** 4/16/79
** 4/16/79
*« 4/16/79
** 4/16/79
*« 4/16/79
** 4/16/79
** 4/16/79
** 4/16/79
«* 4/16/79
»* 4/16/79
*« 4/16/79
** 4/16/79
** 4/16/79
** 4/16/79
** 4/16/79
** 4/16/79
»* 4/16/79
** 4/16/79
15 HIN
DRV STACK GAS
TIME
**ft***i
15
30
45
100
115
130
145
200
215
230
205
300
315
330
345
400
415
430
445
500
515
530
545
600
615
630
645
700
715
730
745
800
815
830
845
9QO
915
930
945
1000
1030
1045
1100
1115
1130
1145
1200
LOAD
MWTH
fr***ft ft A
18^9
18.9
18.9
19.0
19.0
19.0
19.0
18.8
IB. 8
18. 8
18.8
19.0
19.0
19.0
19.0
I9. 3
19.3
I9. 3
I9. 3
I9. 3
I9. 3
I9. 3
I9. 5
I9. 5
I9. 5
I9. 5
I9. 5
I9. 5
I9. 5
I9. 6
19!6
19.6
I9- 5
I9. 5
I9. 5
I9. 5
19.6
I9. 6
19.6
I9. 6
19.9
19.9
19.9
19.9
02
VQIX
MEAS
*******
7.7
7.3
7.4
7.4
7.5
7.5
7.5
7.4
7.4
7.4
7.4
7.4
7.4
7.4
7.4
7,4
7.4
7.5
7.4
7.4
7.4
7.4
7.4
7.4
7.4
7.4
7,4
7,4
7,2
7,3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.4
7.4
7.4
7.4
7.4
7.4
7.4
7.«
. DATA
CONCENTRATION
C02
VQtX
MEAS
1 ft * * * A **
9.9
9,9
10.2
10,3
10.2
10.1
10.1
10.2
10,1
10.2
10.1
10.1
10.1
10.1
10.1
10. 1
10.1
10.1
10.3
10.0
10.3
10.2
10.2
10.2
10,2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.2
10.3
10,2
NO
PPMV
MEAS
A* A ** A A
ft V m w w w n
162.
162.
162.
162.
16*.
167.
167.
164.
162.
165.
165.
164.
165.
165.
167.
167.
167.
167,
160.
162.
161.
160.
159.
159.
160,
161 ,
162,
165.
166.
167.
167.
167.
167.
167.
166.
180.
ISO.
182.
182.
}B2.
178.
176.
175.
176.
177.
181.
185.
184,
NO
PPMV
3202
ft ft Aft ft ft. ft
220.
214.
216.
216.
218.
223.
224.
218.
2U.
220.
219.
219.
220.
220.
223.
223.
223.
223.
213.
214.
215.
212.
212.
211.
213.
214,
216.
219.
220.
219.
219.
220.
220.
220.
218.
237.
237.
240.
240,
240.
236.
233.
232.
234.
235.
239.
2«5.
2«4,
NO
NC/J
ft ft ft ft ft ftft
121.
118,
119.
119.
120,
123.
124.
120,
118.
121.
121.
121.
121.
121.
123.
123.
123,
123.
117.
118.
118.
117.
117.
116.
118.
118.
II9.
121.
121.
121.
121.
122.
121.
122.
120.
131.
131.
132.
132.
132.
130.
128.
128.
129.
130.
132.
135.
135.
**
*
*«
**
*«
4*ft
**
**
**
*«
**
**
**
»
**
**
*«
*
**
**
**
»*
»
*«
**
*
*
*
*«
**
**
*«
*»
*»
*
**
*»
**
**
**
**
**
**
**
**
**
*
**
**
*
*«
**
**
^ *** A A******** ****** A************ ***************************
179
X7B 6017-1216
-------
ft**********************************
* 15 HIN. DATA
ft DRt STACK 5*3 CONCENTRATION
**
ft
«
A*tf
mmm
ft
*
ft
ft
ft
ft
*
*
ft
*
*
ft
**
**
**
*
ft
**
«
*
ft
*
*
*
ft*
«
*
«
**
ft
ft
*
ft
**
ft
«*
ft
DATE
rA4tftA4iitftA4
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
4/16/79
TIME
I2t5
1230
1245
1300
1315
1330
1345
1400
1415
U30
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
MMTH
1t&1t1t1t1t&l
19.9
19.9
19.9
19.9
19.9
19.9
19.9
19.9
19.9
19.9
19.9
19.9
19.9
19^9
19N
19.9
19.9
19.8
19.8
i9.a
19 6
19*6
19,6
19 6
1*1*
19*6
19.6
19.6
19.0
19.0
I'.O
19.0
19,0
19,0
|9.0
19.0
}9,o
I'.O
j9,o
}9,o
02
VOLX
M£A3
t It It It Aft A
7.4
7.4
7.4
7.4
7.4
7.3
7.7
7.6
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.3
7.4
7.4
7,4
7.4
7)4
7.4
7.6
7.4
7.7
7.7
7.9
7.5
7.6
7.6
7. A
7.7
7.6
7.5
7.5
7.5
7.4
7.6
7.6
CQ2
VOLX
MEAS
, £ * £ 4k ft tf4
10.2
10.1
10.2
10.1
10.1
10.2
9.9
10.0
10.1
10.2
10.2
10.1
10. 1
10. I
10.1
10.1
10.1
10.1
10.1
10. 1
10.1
10. 1
10.1
10.0
10,0
10,1
to.i
10.1
10.1
10.1
10.1
9.9
10.0
9,9
10.0
9,9
9,9
10.0
10.0
10.0
10.0
10.0
10.1
10.1
10.1
10.1
10.1
10.1
NO
PPMV
MEAS
FAA4k£WA4
184.
184.
1*5.
186.
185.
184,
185.
185.
186.
186.
186,
187.
186.
186.
185.
185.
187.
188.
187.
184.
184.
183.
182.
182,
180.
180.
180.
180.
180,
179,
175.
173.
167.
167.
165.
168.
168.
167.
167.
167.
168.
167.
167.
165.
163.
163.
163.
162.
NO
PPMV
3*0*
[(^^^«
245 1
246.
246.
245.
243.
252.
249.
246.
246.
245.
247.
245.
245.
245.
245.
247.
248.
247.
242.
242.
a«f*
240 1
239.
239.
239.
238.
2«0.
237.
232.
233.
223.
227.
223.
230.
224.
224.
225.
224.
228.
226.
224.
220.
218.
217.
219.
217.
NO
NG/J
t
-------
ft*
**
*»
»»
**
** DATE
15 HIM, DATA
DRY STACK GAS CONCENTRATION
TIME
LOAD
MWTH
02
VOLJ
HEAS
C02
VOLX
HEAS
NO
PPMV
HEAS
NO
PPMV
3202
NO
NG/J
**
*
**
**
**
ft********************************************************.,****
** 4/17/79
** 4/17/79
** 4/17/79
* 4/17/79
* 4/17/79
** 4/17/79
** 4/17/79
** 4/17/79
** 4/17/79
* 4/17/79
* 4/17/79
** 4/17/79
** 4/17/79
** 4/17/79
** 4/17/79
* 4/17/79
«* 4/17/79
** 4/17/79
** 4/17/79
** 4/17/79
** 4/17/79
4/17/79
*« 4/17/79
** 4/17/79
** 4/17/79
** 4/17/79
** 4/17/79
* 4/17/79
«* 4/17/79
** 4/17/79
*« 4/17/79
*» 4/17/79
** 4/17/79
** 4/17/79
** 4/17/79
* 4/17/79
** 4/17/79
** 4/17/79
*« 4/17/79
** 4/17/79
** 4/17/79
** 4/17/79
» 4/17/79
** 4/17/79
* 4/17/79
* 4/17/79
** 4/17/79
*« 4/17/79
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
17.6
17.6
17.6
17,6
18^5
18.5
18.5
18.2
18.2
18.2
18.2
17.
17.
17.
17.
18.
18.
18.
18.
18.
18.
18.
18.
18.
18.
18,8
18.8
18.5
18.5
18.5
18.5
17.6
17,6
17.6
17.6
16.1
16,1
16^1
16.0
16.0
16,0
16.0
16.0
16.0
16.0
16.0
7.7
7.6
7.6
7.6
7.6
7.6
7.6
7.5
7.6
7.8
7.5
7,4
7.7
7.6
7.6
7.6
7.6
7.7
7.9
7.6
7.8
7.9
7.7
7.7
7.8
7.7
7.5
7.6
7.6
7.6
7.7
7.5
7.9
7.3
7.3
7.2
7.0
7.9
.1
.4
.6
.7
.7
.6
.5
.5
.5
.5
10.0
10.0
10.1
10.1
10.0
10,1
10.1
10.1
10. 1
10,0
10,1
10.2
10,1
10.1
10.2
10.2
10.2
10.2
9,9
10,0
10,0
10.0
10,0
10.0
10.0
10.0
10.3
10.2
10,2
10,2
10.2
10.1
10.2
10.3
10.3
10.2
10.3
10.4
,8
.6
.3
,2
.2
.2
.2
.2
.2
.2
162.
163.
162.
159.
156.
157,
156.
154.
153.
15*.
154.
154,
154.
155,
155.
155.
154.
150.
154.
155.
153.
153.
152.
151,
150.
150,
152.
152.
154.
155.
151.
1*7,
167.
167.
167.
167.
160.
160,
160.
159.
157.
157.
157.
157.
157.
157.
157.
220.
219.
218.
214.
211.
210.
210.
206.
206.
210.
206.
205.
208.
210.
208.
208.
208.
204,
214.
208.
210.
211.
208.
206.
205.
204,
204,
204,
208.
208.
206.
1*7.
1*6.
220.
220.
218.
216,
220.
225,
230.
231.
231.
231.
229.
228.
227.
227,
227.
121.
121.
120.
118.
116.
116.
116,
114.
lift!
us!
15,
16.
is.
is.
la.
13.
18.
115,
11.6.
116.
114.
111.
113.
113.
113.
113.
115.
US.
114.
109,
108.
122.
122.
120.
12l|
127)
127.
127.
127.
126.
125.
125.
125,
125.
«
«
**
**
*«
**
*
**
*
**
**
*
*«
*
*
**
**
**
«*
*
*«
**
**
*
**
**
**
*
»*
**
*»
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
**
ft**************************************************************
181
KVB 6017-1216
-------
************
*
*
«
**
*« 0*TE
*********
** 4/17/7*
* 4/17/79
»* 4/17/79
* 4/17/79
* 4/17/79
** 4/17/79
*« 4/17/79
** 4/17/79
** 4/17/79
** 4/17/79
*« 4/17/79
*« 4/17/79
** 4/17/79
** 4/17/79
* 4/17/79
«« 4/17/79
** 4/17/79
** 4/17/79
4/17/79
4/17/79
4/17/79
4/17/79
*« 4/17/79
4/17/79
* 4/17/79
* 4/17/79
** 4/17/79
»* 4/17/79
** 4/17/79
«* 4/17/79
* 4/17/79
* 4/17/79
*« 4/17/79
* 4/17/79
** 4/17/79
** 4/17/79
** 4/17/79
** 4/17/79
« 4/17/79
** 4/17/79
* 4/17/79
* 4/17/79
** 4/17/79
** 4/17/79
» 4/17/79
4/17/79
* 4/17/79
4/17/79
a*******************
15 *IN
DRY STACK GAS
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
ISIS
1«30
1845
1900
1915
1930
1945
2000
2015
2030
2045
2100
2115
2130
2145
2200
2215
2230
2245
2300
2315
2330
2345
2400
LOAD
MWTH
»****
1«>.0
16,0
16.0
16.0
16.0
16.0
16.0
16.0
IS. 8
15. 8
15.8
15.8
16.3
16.3
16.3
16.3
17.0
17.0
17.0
17. 0
17.1
17.1
17.1
17.1
16.1
16.1
16.1
16.1
lS.8
is.a
15.8
is. a
17.0
17.0
17.0
t7.o
l7.0
17.0
17.0
17.0
16.4
16.4
16.4
16.4
16.3
16.3
16.3
16.3
02
vats
"EAS
*******
8.7
8.7
8.6
8.6
8.7
8.7
8.7
8.7
8.6
8.7
8.6
8.7
8.7
7.2
7.1
7.2
7.2
7.0
6.7
6.8
6.9
7.0
6.9
6.9
6.9
7.0
7.1
7.1
7.0
7.1
7.1
6.9
7.3
7.4
7.3
7.3
7.3
7.4
7.4
7.4
7.4
7.4
7.4
7.4
7.5
7.7
7.6
7.7
***««*«**«**«*
. DATA
CONCENTRATION
C02
voux
"EAS
*******
.2
.1
.1
.1
.1
.1
.1
.1
.1
.1
.1
.1
.2
f6
10.3
10.4
10.3
10,3
10.5
10.6
10.6
10.6
10.5
10.6
10.6
10.6
10.5
10.5
10.5
10.5
10.5
10.5
10.6
10.3
10.3
10.4
10.*
10.4
10.3
10.4
10. «
10.4
10.4
10.4
10.4
10.2
10.2
10.2
NO
PPMV
MEAS
*******
159.
159.
159,
159.
159.
159.
159.
159.
159.
158.
157.
157.
157,
154.
153.
153.
154.
166.
165.
165.
166.
165.
163.
164.
164.
163.
165.
167.
168.
171.
175.
162.
174.
172.
177.
177.
177.
177.
175.
175.
174.
176.
170.
171.
166.
170.
173,
170.
*«****»»»**»**
**
**
NO
PPMV
3za«
*******
232.
232.
231.
232.
233.
233.
232.
234.
233.
232.
229.
230.
230.
201,
199.
200.
202.
214,
209.
210.
211.
213.
208.
210.
210.
211,
213.
216.
217,
221.
227.
207.
229.
229.
234.
233,
234.
234.
231.
233.
232.
233.
225.
227.
222.
231.
233.
230.
NO
NG/J
*******
128.
128.
128.
128.
129.
12<».
128,
129.
128.
128.
126.
127.
127.
111.
110.
110.
Ill,
118.
115.
116.
116.
117.
115.
116.
116.
116.
118.
119.
120.
122.
125.
11«.
126.
126.
129.
129.
129.
129.
127,
128.
128,
129,
12«.
125.
122.
127.
128.
127.
**
**
**
**
***
**
**
*
**
*
**
*
*
**
**
*
«*
**
*
**
**
*
*
**
**
**
*
*
**
**
*
**
*
**
*
*
**
**
*
**
**
*
*«
*
**
*
**
*
*
a**********************************************************
182
KVB 6017-1216
-------
ft*
*
ft*
ft*
ft*
* DATE
***********
** 4/18/79
* 4/18/79
** 4/18/79
* 4/18/79
* 4/18/79
** 4/18/79
* 4/18/79
4/18/79
* 4/18/79
* 4/18/79
* 4/18/79
* 4/18/79
* 4/18/79
*« 4/18/79
* 4/18/79
* 4/18/79
* 4/18/79
* 4/18/79
** 4/18/79
* 4/18/79
* 4/18/79
** 4/18/79
** 4/18/79
* 4/18/79
* 4/18/79
* 4/18/79
* 4/18/79
ft* 4/18/79
* 4/18/79
ft* 4/18/79
ft* 4/18/79
ft* 4/18/79
* 4/18/79
* 4/18/79
* 4/18/79
* 4/18/79
** 4/18/79
* 4/18/79
* 4/18/79
* 4/18/79
* 4/18/79
* 4/18/79
** 4/18/79
* 4/18/79
* 4/18/79
* 4/18/79
** 4/18/79
* 4/18/79
AAAA^AAAA^. ^ .*.
15 MIN. DATA
DRV STACK GAS CONCENTRATION
TIME
*****1
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
930
945
1000
1015
1030
1045
1100
1115
1130
1145
1200
LOAD
MNTH
^^ 1t1l + I
l7.6
17.6
17.6
17.6
17.4
17.4
I7.4
17.4
17.3
17. 3
17.3
17.3
17.4
17.4
17.4
17.4
17.4
17.4
17.4
17.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16,4
16.4
16^4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.4
16.7
16.7
16.7
16.7
02
VOLX
MEAS
'***«*
7.6
7.6
7.6
7.6
7.7
7.7
7.6
7.7
7.7
7.7
7.7
7.8
7.8
7.8
7.8
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.9
7.8
7.7
7.9
7.9
7.9
7.9
8.8
8.8
.8
.7
.7
.7
.0
7.9
7.9
7.9
7.9
7.8
7.7
7.7
7.7
7.7
7,7
7.7
7.7
C02
VOLX
MEAS
*ftft**ftft
10.2
10.2
10.2
10.2
10.3
10.3
10.2
10.2
10.2
10.2
10.2
10.1
10.1
10.1
10.1
10.1
10.1
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.1
10.3
10.3
10.4
10.4
10.4
10.3
9.4
9.4
.5
.5
.5
.6
.8
.8
.9
.9
.9
.9
.9
.9
.9
.9
9.9
NO
PPMV
MEAS
*******
169.
170.
169.
172.
170.
173,
167.
170.
168.
170.
162.
160.
162.
157.
158,
158,
160.
156.
162.
164.
162.
163.
161,
167.
178,
181.
183.
157.
155.
155.
154.
158.
156.
157.
130.
122.
132.
119.
121.
121.
120.
125.
122.
121.
125,
127,
125.
124.
NO
PPMV
3X0*
*******
226.
228.
228.
232.
230.
234.
226.
230.
227.
231.
220.
219,
222.
215.
216.
218.
221.
216.
223.
226.
224.
225.
223.
229.
242.
250.
253.
217.
215.
230.
228.
234.
229.
231.
190.
170.
183.
164.
166.
167.
164.
170.
165.
164.
170.
17(1.
170.
168,
NO
NG/J
*******
125.
126.
125.
128.
127.
129.
125.
127.
125.
127.
121.
121 .
122.
119.
119,
120,
122.
119.
123.
125.
* * * 9
124,
124.
123.
126.
138^
139.
120.
119.
127.
126,
129,
126,
127,
105.
94,
101.
90.
92.
92.
90.
93.
91.
91.
96 )
94,
93.
**
*
»*
**
**
***
**
*
**
**
*
*
**
*
*
**
**
*
*
*«
*
**
**
*
**
*
**
ft*
**
**
**
**
*
**
**
ft*
*«
**
**
**
**
**
**
**
**
**
**
**
133
KVB 6017-1216
-------
*****«***«*«<
**
«*
15 MIN, DATA
OUT STACK CAS CONCENTRATION
>*«****«****»»«*»
**
**
»* DATE TIME
********««***««
* 4/18/79 1215
« 4/18/79 1230
«« 4/18/79 1245
** 4/18/79 1300
«« 4/18/79 1315
*« 4/18/79 1330
«* 4/18/79 1345
** 4/18/79 1400
« 4/18/79 1415
*« 4/18/79 1430
« 4/18/79 1445
4/18/79 1500
« 4/18/79 1515
* 4/18/79 1530
** 4/ie/79 1545
* 4/18/79 1600
* 4/18/79 1615
** 4/18/79 1630
« 4/18/79 1645
** 4/18/79 1700
*« 4/18/79 1715
*« 4/18/79 1730
* 4/18/79 1745
** 4/18/79 1800
** 4/18/79 1815
* 4/18/79 1830
* 4/18/79 1845
** 4/18/79 1900
* 4/18/79 1915
** 4/18/79 1930
* 4/18/79 1945
«* 4/18/79 2000
«* 4/18/79 2015
* 4/18/79 2030
«* 4/18/79 2045
* 4/18/79 2100
** 4/18/79 21IS
*« 4/18/79 2130
« 4/18/79 2145
* 4/18/79 2200
*« 4/18/79 2215
« 4/18/79 2230
* 4/18/79 2245
** 4/18/79 2300
* 4/18/79 2315
** 4/18/79 2330
*» 4/18/79 2345
* 4/18/79 2400
*******«****
02
J.OAO VOLX
HWTH MEAS
16.7
16.7
16.7
16.7
17.0
17.0
17.0
17.0
17.0
17.0
17,0
17,0
17.0
17.0
17.0
17*.0
17.0
17.0
17.0
17.1
17.1
17.1
17.1
16.1
16.1
16.1
16.1
15,8
15.8
15.8
ts.e
17.0
17.0
17.0
17.0
17.0
17.0
17.0
17.0
16.4
16.4
16.4
16.4
16.3
16.3
16.3
16.3
>****
C02
VOL*
MEAS
8.5
8.0
7.3
7.2
7,2
7.4
7.9
7.7
7,2
7.2
7.2
7.5
7.8
7.8
7.7
7.7
7.7
8.0
8.7
8.2
8.1
8.2
6.9
1.0
7.9
7.9
8.5
8.5
8.7
8.2
8.2
8.2
8.2
8.1
8.1
8.2
8.1
8.1
8.1
8.1
.0
.0
.0
.1
.2
.2
.2
.2
»«*******
NO
PPMV
MEAS
NO
PPMV
3«02
9.9 125.
10.0 122.
10.0 122.
10.0 123.
10.0 122.
10.0 123.
10.1 122*
10.1 122.
10.1 121.
10.1 120.
10.1 121.
10.1 122.
10.1 125.
10.0 125.
9.9 124.
9.9 124.
9,9 124.
9.9 125.
9.9 121.
9.9 121.
10.0 121.
10,0 120.
10.0 120.
10.1 -1.
10.1 130.
.0 129.
9,5 130.
9.5 132.
9.5 131.
9.5 120.
9,7 120.
9.7 120.
9.7 119.
9.7 120.
9.7 118.
9.7 118.
9.7 117.
9.7 116.
9.7 115.
9.7 115.
9,8 114,
9.8 123.
9.8 123.
9.6 122.
9.6 123.
9.6 124,
9.5 !23.
9.5 123.
,«*«**««******
*
NO **
HG/J «*
*«
180. 99, «
170. 94. **
161. 89. **
161. 89. »*
161. 89. **
163. 90, *
169, 93. **
166. 92. *
159. 88. *
157. 87. »*
159. 88. »*
164. 90. *
171. 94.
171. 94,
169. 93. *
168. 93.
168. 93, *
173. 96, **
178. 96. *
172. 95, *
169. 93. . *«
169. 93, *
154, 85.
! -1. **
160. 99, *
179. 99,
187. 103. **
191. 105, «
192, 106, »*
169. 93. *
169, 93. **
169. 93. *
168. 93. **
168, 93. »*
166. 91. **
166. 92. »*
164. 91. »*
162. 89. *»
161. 89. *
161. 89. *
159. 88.
171. 94. *
171. 94. *
172. 95. *
173. 96. **
175. 96. *
173. 96. »*
174. 96. *
**»»*»»«***
184
KVB 6017-1216
-------
ft**********'
ft*
ft*
ft*
ft*
ft* DATE
** 4/19/79
ft* 4/19/79
** 4/19/79
** 4/19/79
ft* 4/19/79
ft* 4/19/79
ft* 4/19/79
* 4/19/79
** 4/19/79
* 4/19/79
*« 4/19/79
ft* 4/19/79
* 4/19/79
** 4/19/79
** 4/19/79
** 4/19/79
ft* 4/19/79
** 4/19/79
* 4/19/79
* 4/19/79
** 4/19/79
ft* 4/19/79
** 4/19/79
** 4/19/79
ft* 4/19/79
* 4/19/79
ft* 4/19/79
* 4/19/79
*« 4/19/79
** 4/19/79
ft* 4/19/79
ft* 4/19/79
*« 4/19/79
«* 4/19/79
ft* 4/19/79
** 4/19/79
* 4/19/79
*« 4/19/79
ft* 4/19/79
** 4/19/79
ft* 4/19/79
ft* 4/19/79
** 4/19/79
ft* 4/19/79
ft* 4/19/79
«* 4/19/79
* 4/19/79
* 4/19/79
* ***** **************«********'
15 HIM, DATA
CRT STACK GAS CONCENTRATION
TIME
******<
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
HMTH
02
VOLX
MEA3
C02
VOLX
HEAS
NO
PPMV
MEAS
*****************
**
*
NO
PPMV
3XQ2
NO
NG/J
**
ft*
**
**
.*******»**<**<**«******************
17J6
17.6
17.6
17.4
17.4
17.4
17.4
17.3
17.3
17.3
17.3
17.4
17.4
17.4
17.4
17.4
17.4
17.4
17.4
16.4
16,4
16.4
16.4
16,4
1*I«
16.4
!*.«
l*Ia
16. *
1*I»
!*.«
!*.«
16.0
16.0
16.0
16.0
16.4
16,4
16.4
16.4
16.7
16.7
16.7
16.7
8.2
8.2
8.1
8.1
8.1
8.1
8.1
8.2
8. a
3.4
8.3
8.3
8.2
8.2
8.2
8.2
8.3
8.3
8.1
8.0
8.0
8.0
8.0
8.0
8.0
7.9
7.9
7.9
7.9
7.8
7.7
7.7
8.2
8.2
8.3
8.0
7.8
7.8
7.8
7.8
7.7
7.7
7.7
7.7
7.7
7.6
7.6
7.7
9.5
9.5
9.5
9,5
9.5
9.5
9.5
9.5
9.5
9.4
9.3
9.3
9.4
9.4
9.4
9,4
9.4
9.4
9.3
9,4
9.5
9.6
9.6
9,5
9,6
9.6
9.6
9.6
9.7
'.7
9.7
9.7
9.7
'.7
9.4
9.4
9.4
9,4
9,9
9.8
9,9
9.9
.0
9.9
10.0
10.0
.0
10.0
123.
123.
122.
122.
122.
121.
121.
122.
126.
129.
130.
130.
78,
79.
79.
79.
122.
127.
125.
125.
124.
125.
125,
125,
126.
125.
126.
127.
126.
126.
126,
125,
134,
128.
129.
130,
122,
119,
116.
116.
115.
1 1".
119.
118.
116.
117.
118.
118.
173.
173,
172.
172.
172.
169.
169.
173.
180.
184.
185.
185.
111.
112.
112.
112.
174.
180.
175.
173.
173.
170.
174.
174.
174.
173.
174.
175,
174.
173.
172.
171.
189,
1*1.
l8ol
1*7.
162.
159.
159.
156.
156.
0 f- t- » «
o -o in mm *
95.
95.
95.
95.
95.
93.
93,
96,
99,
101,
102.
102.
61.
62.
62.
62.
96.
99.
97,
96.
95.
96,
96.
96.
96.
95,
96,
97.
96.
'5.
95.
94.
104,
100,
101,
99.
92.
89.
88.
88.
86.
86.
89.
88.
87.
87.
88.
89,
* A A A ***«
*
*«
**
*
*
**
**
ft*
*
**
**
**
**
**
*
*»
**
**
*
**
**
**
**
**
**
ft*
*
*«
**
**
**
ft*
**
ft*
**
**
*
*
*
**
**
**
**
**
**
*«
**
ft*
*****
185
KVB 6017-1216
-------
ft*********************************************************
ft*
*«
ft*
ft*
ft*
«« DATE
^^^^A0*^^*^.|
WwwWWW WWW WITH
* 4/19/79
4/19/79
4/19/79
« 4/19/79
** 4/19/79
ft* 4/19/79
* 4/19/79
* 4/19/79
** 4/19/79
« 4/19/79
ft* 4/19/79
** 4/19/79
** 4/19/79
* 4/19/79
4/19/79
ft* 4/19/79
ft* 4/19/79
* 4/19/79
4/19/79
* 4/19/79
* 4/19/79
** 4/19/79
* 4/19/79
« 4/19/79
«« 4/19/79
* 4/19/79
* 4/19/79
** 4/19/79
** O/ 0/79
O/ 0/79
* O/ 0/79
« O/ 0/79
** O/ 0/79
ft* O/ 0/79
* O/ 0/79
ft* O/ 0/79
*» / 0/79
* O/ 0/79
ft* O/ 0/79
ft* O/ 0/79
0/ 0/79
ft* O/ 0/79
ft* O/ 0/79
O/ 0/79
ft* O/ 0/79
* O/ 0/79
* O/ 0/79
O/ 0/79
15 "IN. DATA
OS* STACK GAS CONCENTRATION
TIME
1 A* A A* A
* w W W W W *l
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
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
LOAD
MKTH
****** *
16^7
16.7
16.7
16.8
16.8
16.8
16.8
16,6
16.6
16.6
16.6
16.4
16.4
16.
16.
16.
16.
16.
16,
16.
16.
16.
16.
16.
16.
16.
16.
.0
.0
.0
Io
.0
.0
m
t
t
t
t
t
«
.
.0
.0
.0
.0
02
VOL I
MEAS
Fft A AAHttl
7.8
7.8
7.7
7.7
7.7
7.7
-1.0
-1.0
U.2
-1.0
12.4
12.4
12.5
12.7
12.8
12.9
12.5
12.5
12.3
12.0
12.0
12.0
12.0
12.0
IU7
11.5
12.5
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
C02
VOLX
MEAS
r******i
10.0
10.0
.0
9.9
9.9
9.9
9,9
10.0
.0
.0
.0
9.2
12.0
.0
9.7
9.7
9.7
9.7
.0
9.6
9.7
lo
9.7
9.7
.0
9.7
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
NO
PPMV
MCA3
»******!
121.
121.
118.
119.
118.
119.
119.
147.
105.
-I.
-1.
124.
124.
123.
125.
127.
128.
127.
124.
123.
122.
I2l!
12
-------
TECHNICAL REPORT DATA
(Please read Irusrucnons on the reverse before completing}
. REPORT NO.
EPA-600/7-80-085b
2.
3. RECIPIENT'S ACCESSION NO.
A. TITLE AND SUBTITLE
Thirty-day Field Tests of Industrial Boilers: Site 2-
Residual-oil-fired Boiler
5. REPORT DATE
April 1980
6. PERFORMING ORGANIZATION CODE
'. AUTHOH(S)
W.A. Carter and R.J. Tidona
8. PERFORMING ORGANIZATION REPORT NO.
9. PERFORMING ORGANIZATION NAME AND ADDRESS
KVB, Inc.
P.O. Box 19618
Irvine, California 92714
10. PROGRAM ELEMENT NO.
EHE624
11. CONTRACT/GRANT NO.
68-02-2645, Task 4
12. SPONSORING AGENCY NAME AND AOORESS
EPA, Office of Research and Development
Industrial Environmental Research Laboratory
Research Triangle Park, NC 27711
13. TYPE OF REPORT AND PERIOD COVERED
Task Final; 3/79-3/80
14. SPONSORING AGENCY CODE
EPA/600/13
15. SUPPLEMENTARY NOTES
541-2477.
project officer is Robert E. Hall, Mail Drop 65, 919/
is. ABSTRACT
repOrt is a. final one for a test program to evaluate the long-term
effectiveness of combustion modifications on industrial boilers. Previous short-term
tests had been performed on industrial boilers to determine the effect of combustion
modifications on such air pollutant emissions as NOx, SOx, CO, HC, and particu-
late. The objective of this program was to determine if the combustion modification
techniques which were effective for the short-term tests are feasible for longer
periods. The report gives results of a 30-day field test of a 26. 4 MW output (90,000
Ib steam/hr) residual-oil-fired boiler using staged combustion air and low excess
air to control NOx emissions. Results indicate that these combustion modifications
are effective long-term NOx controls for this type of residual-oil-fired boiler. The
as-found NOx concentration was 158 ng/J (281 ppm at 3% O2, dry). With staged com-
bustion and low excess air firing, the mean NOx emission level was 110 ng/J (196
ppm at 3% O2 , dry). Boiler efficiency increased by 0. 7% under low NOx firing
conditions .
17.
KEY WORDS AND DOCUMENT ANALYSIS
DESCRIPTORS
b.IDENTIFIERS/OPEN ENDED TERMS
c. COSATl Field/Group
Pollution
Boilers
Residual Oils
Combustion
Field Tests
Sulfur Oxides
Nitrogen Oxides
Carbon Monoxide
Hydrocarbons
Dust
Pollution Control
Stationary Sources
Industrial Boilers
Combustion Modification
Staged Combustion
Low Excess Air
Particulate
13B
13A
2 ID
2 IB
14B
07B
07C
11G
13. DISTRIBUTION STATEMENT
Release to Public
19. SECURITY CLASS (This Report!
Unclassified
21. NO. OF
201
'AGES
2O. SECURITY CLASS
Unclassified
22. PRICE
EPA Form 2220-1 (3-73)
187
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