FINAL REPORT
EMISSIONS EVALUATION
OF
BATTERIES 1B AND 2 PUSHING EMISSIONS CONTROL SYSTEM
BATTERY 1B COMBUSTION STACK
BATTERY 2 COMBUSTION STACK
KOPPERS INDUSTRIES
MONESSEN COKE PLANT
MONESSEN, PENNSYLVANIA
OPTIMAL PROJECT NO. 937
DECEMBER 6, 1996
PREPARED BY
PAUL JADLOWIEC
MANAGER-SOURCE TESTING
OPTIMAL TECHNOLOGIES
575 WILLIAM PITT WAY
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Air Quality Services
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TABLE OF CONTENTS
1.0 EXECUTIVE SUMMARY 1
2.0 SCOPE AND OBJECTIVES 2
3.0 PROCESS DESCRIPTION 3
3.1 Batteries 1B and 2 Pushing Emission Control System 3
3.2 Batteries 1B and 2 Combustion Stacks 3
4.0 PROCEDURES 4
4.1 Field Work .4
4.1.1 Field Data Sheets 4
4.1.2 Testing Station and Traverse Locations 4
4.1.2.1 Batteries 1B and 2 Pushing Emission Control
System 4
4.1.2.2 Battery 1B Combustion Stack 4
4.1.2.3 Battery 2 Combustion Stack 4
4.1.3 Gas Flow and Gas Temperature Measurements 5
4.1.4 Carbon Dioxide and Oxygen Determination 5
4.1.5 Moisture Content Sampling 5
4.1.6 Determination of Particulate Matter Emissions 5
4.1.7 Determination of Carbon Monoxide Emissions 6
4.1.8 Determination of Volatile Organic Compound
Emissions 6
4.1.9 Determination of Nitrogen Oxides Emissions 6
4.1.10 Determination of Visible Emissions 7
4.1.11 Sample Recovery 7
4.2 Analysis 7
4.3 Calculations 7
4.4 Field Equipment Calibrations 7
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5.0 SUMMARY OF RESULTS
9
5.2
5.3
TABLES
Table 1
Table 2
Table
3
Table
4
Table
5
Table
6
Table
7
Table
8
Table
9
Table
10
Batteries 1B and 2 Pushing Emissions Control System 9
5.1.1 Particulate Emissions 9
5.1.2 Nitrogen Oxides Emissions 9
5.1.3 Volatile Organic Compound Emissions 9
5.1.4 Carbon Monoxide Emissions 9
5.1.5 Visible Emissions 9
Battery 1B Combustion Stack 9
5.2.1 Particulate Emissions 9
5.2.2 Nitrogen Oxides Emissions 10
5.2.3 Volatile Organic Compound Emissions 10
5.2.4 Carbon Monoxide Emissions 10
5.2.5 Visible Emissions 10
Battery 2 Combustion Stack 10
5.3.1 Particulate Emissions 10
5.3.2 Nitrogen Oxides Emissions 10
5.3.3 Volatile Organic Compound Emissions 11
5.3.4 Carbon Monoxide Emissions 11
5.3.5 Visible Emissions 11
Summary of Emission Results
Batteries 1B and 2 Pushing Emissions Control System, Particulate
Emissions
Batteries 1B and 2 Pushing Emissions Control System, NOx, VOC,
and CO Emissions
Batteries 1B and 2 Pushing Emissions Control System, Visible
Emissions
Battery 1B Combustion Stack, Particulate Emissions
Battery 1B Combustion Stack, NOx, VOC, and CO Emissions
Battery 1B Combustion Stack, Visible Emissions
Battery 2 Combustion Stack, Particulate Emissions
Battery 2 Combustion Stack, NOx, VOC, and CO Emissions
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APPENDICES
Appendix A
Appendix B
Appendix C
Appendix D
Appendix E
Field Data Sheets
Laboratory Reports
Calculations
Field Equipment Calibration
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Koppers Industries
Morvessen Coke Plant
December 6, 1996
1.0 EXECUTIVE SUMMARY
Optimal Technologies, Inc. (Optimal) was contracted by Koppers Industries, Inc. to
perform emission testing at the coke plant located in Monessen, Pennsylvania.
Testing was conducted at the following sources:
Batteries 1B and 2 Pushing Emission Control System;
Battery 1B Combustion Stack; and
Battery 2 Combustion Stack.
The following emissions were sample at each source:
Particulate Matter;
Nitrogen Oxides (NOJ;
Volatile Organic Compounds (VOC);
Carbon Monoxide (CO); and
Visible Emissions.
Testing and analyses were conducted using the principles of U.S. Environmental
Protection Agency (EPA) Methods specified in 40 CFR, Part 60, Appendix A and
Pennsylvania Department of Environmental Protection (PADEP) source testing
methodology. The source testing was performed to demonstrate compliance with the
permit limitation of 0.04 grains per dry standard cubic feet (0.04 gr/dscf) of Particulate
Matter for each of the subject sources. Testing results for NOx, VOC, CO, and visible
emissions are provided for informational purposes. Table 1 summarizes the emission
results.
TABLE 1
SUMMARY OF EMISSION RESULTS
Emission Parameter
Measured Emission
Battery 1B and 2
Pushing Emission
Control System
Battery 1B
Combustion
Stack
Battery 2
Combustion
Stack
Particulate Matter
NOx
VOC
CO
Visible Emissions
0.0035 gr/dscf
8.24 Ib/hr
1.06 Ib/hr
21.10 Ib/hr
0.0 %
0.0037 gr/dscf
122.93 Ib/hr
1.32 Ib/hr
46.98 Ib/hr
0.3 %
0.0084 gr/dscf
61.93 Ib/hr
2.28 Ib/hr
9.11 Ib/hr
0.1 %
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Koppers Industries
Monessen Coke Plant
December 6, 1996
2.0 SCOPE AND OBJECTIVES
The scope of this project was to determine the following emissions from Batteries 1B
and 2 Pushing Emission Control System and Batteries 1B and 2 Combustion Stacks
using approved reference sampling methods:
• Total Particulate
• Nitrogen Oxides
• Volatile Organic Compounds
• Carbon Monoxide
• Visible Emissions
The average of three sampling runs constituted the test for each parameter. The
particulate emission test results will be used to demonstrate compliance with the 0.04
gr/dscf particulate emission limit. Testing results for the other pollutants are provided
for informational purposes.
The field sampling program was performed from November 18 through 22, 1996. One
test run was conducted each day on November 18, 19, and 20, 1996 for Batteries 1B
and 2 Pushing Emission Control System. Three test runs were conducted each day
on November 21 and 22, 1996 for Batteries 2 and 1B Combustion Stacks,
respectively.
The Optimal test personnel consisted of Messrs. William Stanziana, Paul Jadlowiec,
Jim Phillippi , Joseph Stanger, David Sonnet, and Ms. Denise Smith. Mr. Greg
Shamitko served as plant liaison for this test program. The PADEP was represented
on November 18,1996 by Mr. Daniel Haney, Air Quality Specialist, and on November
22, 1996 by Mr. Donald F. Rinald, Air Pollution Control Engineer.
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Koppers Industries
Monessen Coke Plant
December 6, 1996
3.0 PROCESS DESCRIPTION
3.1 BATTERIES 1B AND 2 PUSHING EMISSION CONTROL SYSTEM
Batteries 1B and 2 pushing emissions are collected through the use of a Minister-Stein
system and baghouse which includes a hood above the car (hot car) into which the
hot coke is pushed. The traveling hood has the ability to move with the hot car and
evacuate the emissions to a baghouse thereby removing particulate matter from the
gas stream prior to discharge to the atmosphere. Typically, twenty-seven (27) ovens
are pushed during an eight-hour turn at the Monessen Coke Plant.
3.2 BATTERIES 1B AND 2 COMBUSTION STACKS
Desulfurized coke oven gas is used as the underfiring fuel for Batteries 1B and 2. The
products of combustion from the underfiring for each battery are exhausted through
single exhaust stacks.
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Koppers Industries
Monessen Coke Plant
December 6, 1996
4.0 PROCEDURES
4.1 FIELD WORK
4.1.1 Field Data Sheets
All field data sampling sheets are contained in Appendix A.
4.1.2 Testing Station and Traverse Locations
4.1.2.1 Batteries 1B and 2 Pushing Emission Control System
The sampling station for Batteries 1B and 2 Pushing Emission Control System is
located on an existing platform approximately 50 feet above elevation. The inside
diameter of the metal exhaust stack is 71.25 inches. The two sampling ports are
located approximately 12 feet, or 1.5 diameters, upstream from the stack exit and 36
feet, or six diameters, downstream from the inlet plenum. Twenty-four sampling points
were selected, 12 at each test port, using EPA Method 1-Sample and Velocity
Traverses for Stationary Sources.
4.1.2.2 Battery 1B Combustion Stack
The sampling station for Battery 1B Combustion Stack is located on an existing
platform approximately 50 feet above elevation. The inside diameter of the exhaust
stack is 13 feet. The four sampling ports are located more than 100 feet, or eight
diameters, upstream from the stack exit and approximately 50 feet, or four diameters,
downstream from the inlet plenum. Twenty-four sampling points were selected, six at
each test port, using EPA Method 1.
4.1.2.3 Battery 2 Combustion Stack
The sampling station for Battery 2 Combustion Stack is located on an existing platform
approximately 50 feet above elevation. The inside diameter of the exhaust stack is 10
feet. The four sampling ports are located more than 100 feet, or 10 diameters,
upstream from the stack exit and approximately 50 feet, or five diameters, downstream
from the inlet plenum. Twenty-four sampling points were selected, six at each test
port, using EPA Method 1.
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Koppers Industries
Monessen Coke Plant
December 6, 1996
4.1.3 Gas Flow and Gas Temperature Measurements
The gas flow rate and temperature profiles for the gas stream were measured by
conducting simultaneous velocity and temperature traverses concurrently with the
Particulate Matter emission sampling. Gas velocity head was measured with a
calibrated "S"-type Pitot tube that was connected to an inclined manometer. A
Chrome-Alumel thermocouple attached to a digital indicator was used to measure the
gas temperature at each of the traverse points. The gas flow and gas temperature
measurements followed the principles of EPA Method 2--Temperature and Velocity
Traverses for Stationary Sources.
The gas flow data collected for the Particulate Matter emission tests were used to
calculate the emission rates of NOx. VOCs, and CO that were measured during each
Particulate Matter sample run.
4.1.4 Carbon Dioxide and Oxygen Determination
A Fyrite analyzer was used to determine the molecular weight of the flue gas for the
measurement of gas flow during sampling. Three grab samples were collected during
each sample run using the principles of EPA Method 3-Gas Analysis for the
Determination of Dry Molecular Weight. The following parameters were measured:
percent carbon dioxide (C02) by volume and percent oxygen (02) by volume. The
percent nitrogen (N2) by volume was determined by difference.
4.1.5 Moisture Content Sampling
Moisture sampling was conducted using the principles presented in EPA Method 4-
Moisture Content in Stack Gases concurrently with Particulate Matter emission
sampling. Parameters evaluated in order to determine the gas stream moisture
content were: sample gas volume, sample gas temperature, sample gas pressure,
impingers moisture gain, and silica gel moisture gain.
4.1.6 Determination of Particulate Matter Emissions
EPA Method 5- Determination of Particulate Matter Emissions from Stationary
Sources was used in this test program. The sampling and analytical procedures
described in the PADEP "Source Testing Manual," 1995, Revision No. 2 was
incorporated in the test program. Particulate Matter was withdrawn isokinetically from
the gas streams of each source and collected in a stainless steel-lined probe and
nozzle and on a heated glass fiber filter. A series of glass impingers were used to
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Koppers Industries
Monessen Coke Plant
December 6, 1996
collect moisture and the "back-half catch was analyzed by procedures described the
PADEP "Source Testing Manual." A calibrated dry gas meter measured the gas
sample volume that exceeded 61 dry standard cubic feet (dscf) for Batteries 1B and 2
Combustion Stacks and 36 dscf for Batteries 1B and 2 Pushing Emission Control
System The average of three 120-minute sampling runs constituted the test for
Battery 1B and 2 Combustion Stacks and three 48-minute sampling runs constituted
the test for Battery 1B and 2 Pushing Emission Control System.
When testing Battery 1B and 2 Pushing Control System, each of the 24 sampling
points were sampled for two minutes. Sampling started when the fan damper opened
and coke started to be pushed. Twenty-four pushes, one push per point, constituted
each sampling run.
4.1.7 Determination of Carbon Monoxide Emissions
The principles of EPA Method 10-Determination of Carbon Monoxide Emissions from
Stationary Sources were used for this test program. A gas sample was continuously
extracted from each source at one sampling point in the gas stream and a portion of
the sample was conveyed to a CO analyzer. The analyzer measured the CO
concentration using the principles of nondispersive infrared (NDIR) analyses. Three
60-minute samples were collected for Battery 1B and 2 Combustion Stacks and three
48-minute samples were collected for Battery 1B and 2 Pushing Emission Control
System.
4.1.8 Determination of Volatile Organic Compound Emissions
The principles of EPA Method 25A-Determination of Volatile Organic Compound
Emissions from Stationary Sources Using A Flame Ionization Analyzer (FIA) were
used for this test program to determine VOCs. A gas sample was continuously
extracted from each source at one sampling point in the gas stream and a portion of
the sample was conveyed to a VOC Analyzer. The VOC analyzer was calibrated with
propane and the emissions were reported as propane. Three 60-minute samples were
collected for Battery 1B and 2 Combustion Stacks and three 48-minute samples were
collected for Battery 1B and 2 Pushing Emission Control System.
4.1.9 Determination of Nitrogen Oxides Emission
The principles of EPA Method 7E-Determination of Nitrogen Oxides Emissions from
Stationary Sources (Instrumental Analyzer Procedure) were used for this test program.
A gas sample was continuously extracted from each source at one sampling point in
the gast stream and a portion of the sample was conveyed to a NOx analyzer. The
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Koppers Industries
Monessen Coke Plant
December 6, 1996
analyzer measured the NOx concentration using the principles of chemiluminescence.
Three 60-minute samples were collected for Battery 1B and 2 Combustion Stacks and
three 48-minute samples were collected for Battery 1B and 2 Pushing Emission
Control System.
4.1.10 Determination of Visible Emissions
Visible emissions were determined using a certified visible emission observer. The
principles of EPA Method 9-Visual Determination of the Opacity From Stationary
Sources was used. Observations were made simultaneously with Particulate Matter
sampling at each source.
4.1.11 Sample Recovery
Recovery of samples was conducted on-site in the Optimal Air Van.
4.2 ANALYSIS
Analysis for the "front half total particulate was conducted by Optimal in their
Pittsburgh, Pennsylvania laboratory. The analysis for the "back half' particulate was
conducted by Air Quality Services, Inc. Copies of all laboratory reports are contained
in Appendix B.
4.3 CALCULATIONS
Emission calculations were completed using a computer spreadsheet format. The
results of each pertinent parameter are detailed on the spreadsheet for each sampling
run and are contained in Appendix C.
4.4 FIELD EQUIPMENT CALIBRATIONS
The following field equipment calibration data are contained in Appendix D:
• Nozzle Diameter
• Thermocouple
• Dry Gas Meter and Orifice
• Pitot Tube
• Field Barometer
• Calibration Gas Certificates
• Analyzer Drift
• Analyzer Response Time
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Koppers Industries
Monessen Coke Plant
December 6, 1996
• Analyzer System Bias
• NOx Analyzer Interference
• NOx Analyzer NO to N02 conversion
4.5 OPERATION DATA
Copies of the Pushing Schedules for Batteries 1B and 2 for all sampling periods are
contained in Appendix E.
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Koppers Industries
Monessen Coke Plant
December 6. 1996
5.0 SUMMARY OF RESULTS
5.1 BATTERIES 1B AND 2 PUSHING EMISSION CONTROL SYSTEM
5.1.1 PARTICULATE MATTER EMISSIONS
Table 2 summarizes the results of the Particulate Matter emission sampling. The
measured emissions ranged from 0.0015 to 0.0048 gr/dscf. The average Particulate
Matter emission concentration was 0.0035 gr/dscf.
5.1.2 NITROGEN OXIDES EMISSIONS
Table 3 summarizes the results of the NOx emission sampling. The measured NOx
emissions ranged from 7.27 Ib/hr to 10.10 Ib/hr. The average NOx emission was 8.24
Ib/hr.
5.1.3 VOLATILE ORGANIC COMPOUND EMISSIONS
Table 3 summarizes the results of the VOC emission sampling. The measured VOC
emissions ranged from 0.78 Ib/hr to 1.28 Ib/hr. The average VOC emission was 1.06
Ib/hr.
5.1.4 CARBON MONOXIDE EMISSIONS
Table 3 summarizes the results of the CO emission sampling. The measured CO
emissions ranged from 17.74 Ib/hr to 23.74 Ib/hr. The average CO emission was
21.10 Ib/hr.
5.1.5 VISIBLE EMISSIONS
Table 4 summarizes the results of the visible emissions observations. At no time did
the opacity exceed 0 percent.
5.2 BATTERY 1B COMBUSTION STACK
5.2.1 PARTICULATE MATTER EMISSIONS
Table 5 summarizes the results of the Particulate Matter emission sampling. The
measured emissions ranged from 0.0022 to 0.0060 gr/dscf. The average Particulate
Matter emission concentration was 0.0037 gr/dscf.
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Koppers Industries
Monessen Coke Plant
Decembers, 1996
5.2.2 NITROGEN OXIDES EMISSIONS
Table 6 summarizes the results of the NOx emission sampling. The measured NOx
emissions ranged from 118.96 Ib/hr to 130.61 Ib/hr. The average NOx emission was
122.93 Ib/hr.
5.2.3 VOLATILE ORGANIC COMPOUND EMISSIONS
Table 6 summarizes the results of the VOC emission sampling. The measured VOC
emissions ranged from 0.31 Ib/hr to 2.49 Ib/hr. The average VOC emission was 1.32
Ib/hr.
5.2.4 CARBON MONOXIDE EMISSIONS
Table 6 summarizes the results of the CO emission sampling. The measured CO
emissions ranged from 11.97 Ib/hr to 103.65 Ib/hr. The average CO emission was
46.98 Ib/hr.
5.2.5 VISIBLE EMISSIONS
Table 7 summarizes the results of the visible emissions observations. The average
opacity was 0.3 percent. At no time did the opacity exceed 15 percent.
5.3 BATTERY 2 COMBUSTION STACK
5.3.1 PARTICULATE MATTER EMISSIONS
Table 8 summarizes the results of the Particulate Matter emission sampling. The
measured emissions ranged from 0.0033 to 0.0165 gr/dscf. The average Particulate
Matter emission concentration was 0.0084 gr/dscf.
5.3.2 NITROGEN OXIDES EMISSIONS
Table 9 summarizes the results of the NOx emission sampling. The measured NOx
emissions ranged from 53.86 Ib/hr to 69.69 Ib/hr. The average NOx emission was
61.93 Ib/hr.
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5.3.3 VOLATILE ORGANIC COMPOUND EMISSIONS
Table 9 summarizes the results of the VOC emission sampling. The measured VOC
emissions ranged from 1.97 Ib/hr to 2.53 Ib/hr. The average VOC emission was 2.28
Ib/hr.
5.3.4 CARBON MONOXIDE EMISSIONS
Table 9 summarizes the results of the CO emission sampling. The measured CO
emissions ranged from 1.17 Ib/hr to 22.75 Ib/hr. The average CO emission was 9.11
Ib/hr.
5.3.5 VISIBLE EMISSIONS
Table 7 summarizes the results of the visible emissions observations. The average
opacity was 0.1 percent. At no time did the opacity exceed 15 percent.
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TABLE 2
SUMMARY OF RESULTS
BATTERIES 1B AND 2 PUSHING EMISSIONS CONTROL SYSTEM
PARTICULATE EMISSIONS
Parameter
Run 1
Run 2
Run 3
Average
Gas Flow (acfm)
124629
121357
122769
122918
Gas Flow (dscfm)
116094
112527
117286
115302
Gas Temp (°F)
88.8
83.5
74.2
82.2
Gas Moisture (%)
2.0
2.2
1.5
1.9
Oxygen (%)
21.0
21.0
21.0
21.0
Carbon Dioxide (%)
0.0
0.0
0.0
0.0
Isokinetic Ratio (%)
104.4
104.0
103.8
104.1
Particulate Emissions:
(gr/dscf)
(Ib/hr)
0.0048
4.8
0.0041
4.0
0.0015
1.5
0.0035
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TABLE 3
SUMMARY OF RESULTS
BATTERIES 1B AND 2 PUSHING EMISSIONS CONTROL SYSTEM
NOx, VOC, AND CO EMISSIONS
Parameter
Run 1
Run 2
Run 3
Average
NO, Emissions:
(ppm)
8.85
12.55
8.67
10.02
(Ib/hr)
7.35
10.1
7.27
8.24
VOC Emissions:
(ppm)
1.42
1.01
1.59
1.34
(Ib/hr)
1.13
0.78
1.28
1.06
CO Emissions:
(ppm)
35.11
48.48
42.76
42.12
(Ib/hr)
17.74
23.74
21.83
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TABLE 4
SUMMARY OF RESULTS
BATTERIES 1B AND 2 PUSHING EMISSIONS CONTROL SYSTEM
VISIBLE EMISSIONS
Run 1
Run 2
Run 3
Average
Average Opacity
0
0
0
0
Lowest Opacity
0
0
0
0
Highest Opacity
0
0
0
0
No. ofMin. >20%
0
0
0
0
No. of Min. > 60%
0
0
0
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TABLE 5
SUMMARY OF RESULTS
BATTERIES 1B AND 2 PUSHING EMISSIONS CONTROL SYSTEM
PARTICULATE EMISSIONS
Parameter
Run 1
Run 2
Run 3
Average
Gas Flow (acfm)
112451
111017
94771
106080
Gas Flow (dscfm)
45658
44549
37880
42696
Gas Temp (°F)
607.1
602.2
606.4
605.2
Gas Moisture (%)
16.5
17 9
17.9
17.4
Oxygen (%)
11.7
12.3
12.0
12.0
Carbon Dioxide (%)
5.3
5.7
6.0
5.7
Isokinetic Ratio (%)
106.3
106.9
106.5
106.6
Particulate Emissions:
(gr/dscf)
0.0060
0.0022
0.0028
0.0037
(Ib/hr)
2.3
0.8
0.9
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TABLE 6
SUMMARY OF RESULTS
BATTERY 1B COMBUSTION STACK
NOXt VOC, AND CO EMISSIONS
Parameter
Run 1
Run 2
Run 3
Average
NO, Emissions:
(PPm)
364.40
410.04
440.19
404.88
(Ib/hr)
118.96
130.61
119.23
122.93
VOC Emissions:
(ppm)
0.98
8.17
4.53
4.56
(Ib/hr)
0.31
2.49
1.17
1.32
CO Emissions:
(PPm)
127.4
534.59
72.58
244.86
(Ib/hr)
25.32
103.65
11.97
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TABLE 7
SUMMARY OF RESULTS
BATTERY 1B COMBUSTION STACK
VISIBLE EMISSIONS
Run 1
Run 2
Run 3
Average
Average Opacity
0.3
0.3
0.2
0.3
Lowest Opacity
0
0
0
0
Highest Opacity
15
15
15
15
No. of Min. > 20%
0
0
0
0
No. of Min. > 60%
0
0
0
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TABLE 8
SUMMARY OF RESULTS
BATTERY NO. 2 COMBUSTION STACK
PARTICULATE EMISSIONS
Parameter
Run 1
Run 2
Run 3
Average
Gas Flow (acfm)
53721
48632
50941
51098
Gas Flow (dscfm)
24011
21141
22186
22446
Gas Temp (°F)
542.5
554.6
562.0
553.0
Gas Moisture (%)
13.4
14.7
13.8
14.0
Oxygen(%)
12.7
12.3
11.0
12.0
Carbon Dioxide (%)
4.5
4.0
5.0
4.5
Isokinetic Ratio (%)
90.9
91.4
103.9
95.4
Particulate Emissions:
(gr/dscf)
(Ib/hr)
0.0054
1.1
0.0033
0.6
0.0165
3.1
0.0084
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TABLE 9
SUMMARY OF RESULTS
BATTERY 2 COMBUSTION STACK
NOx, VOC, AND CO EMISSIONS
Parameter
Run 1
Run 2
Run 3
Average
NOx Emissions:
(PPm)
362.54
356.27
439.30
386.04
(Ib/hr)
62.24
53.86
69.69
61.93
VOC Emissions:
(ppm)
15.38
16.20
12.97
14.85
(Ib/hr)
2.53
2.34
1.97
2.28
CO Emissions:
(ppm)
217.66
12.69
35.3
88.55
(Ib/hr)
22.75
1.17
3.41
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TABLE 10
SUMMARY OF RESULTS
BATTERY 2 COMBUSTION STACK
VISIBLE EMISSIONS
Run 1
Run 2
Run 3
Average
Average Opacity
0.2
0
0.1
0.1
Lowest Opacity
0
0
0
0
Highest Opacity
15
5
10
10
No. of Min. > 20%
0
0
0
0
No. of Min. >60%
0
0
0
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Dlslance upstream ifo^iHIow disluibance (Distance A):
IOC> indrcs / diamelef - dd
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O
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U(
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Ol!tU«4A«C(
scHUKATic or sampling location
tHAVCRJl
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or sue* l.o.
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no *u«ut M MCMI
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turn oi/mot of mrru
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Inside ol near wall lo outside of nipple {nipple length):
IP''
Slock Inside diameter. inches
0
I
Distance downstreamJrom How disturbance (Distance B):
-recr r
eK~ iSP -iwctTCs i diametei * J dd
Distance upstream disturbance (Distance A):
y fO& Incites / diameter - 7 dd
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t;
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Correction Factor, 0,973-
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FIELD* DATA SHEET '
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1,117
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Page | of ~£_
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Page 7_ of "2"
Traverse I Elapsed
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JBffiT ' ^ } EPA METHOD 5
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-------
Push Emissions Data Only
Koppers
Monessen, PA Facility
Push Baghouse Emissions Test
VOCs, CO, and NO*
November 18,1996
DATE/TIME
voc
ppm
CO
OPTO
NOx
ppm
Push 1
11/18/96 08 23:51
3
2 1
11/18/96 08:24:11
3
5 1
11/18/96 08 24 31
3
53! 3
11/18/96 0824:51
3
67
9
11/18/96 08 25:11
3
42
9
11/18/96 08 25:31
3
20
5
Push 2
1
11/18/96 08 5837
2
33! 3
11/18/96 08:58:57
S
931 18
11/18/96 08:59:17
3
82
20
11/18/96 08 59 37
2
45
16
11/18/96 08:59 57
2
32! 141
11/18/96 09 00:17 | 2
30! 141
Push 3 j
' 1
11/18/96 09 08 57 ! 2
31; 3 i
11/18/96 09.09 17
11/18/96 09 09 37 "
2
56
9
'9!
2
42 i
11/18/96 09:09 57 | 2
25j 9 j
11/18/96 09 10 17
11/18/96 09 10:37""
2
131 5!
2
5!
1 I
-si
9]
Push 4
11/18/96 09 21 57
1| 45,
11/18/96 09 22.17
1
62 i
11/18/96 09 22 37
1
451 9]
11/18/96 09 22 57
2
33] 9
11/18/96 09 23 17
2
29' 7
11/18/96 09 23 37
2
28 j 7
Push 5
. J..
11/18/96 09:35 17
1
4
1
11/18/96 09 35.37
1
35
3
11/18/96 09:35:57
11/18/96 09 36:17
1
54
9
1
41
12
11/18/96 09 36:37
1
27
9
11/18/96 09:36:57
2
14
5
Push 6
11/18/96 09:49:57
2
36
5
11/18/96 09:50:17
2
46
9
11/18/96 09 50:37
2
33
9
11/18/96 09:50:57
2
25
9
11/18/96 09:51:17
2
24
7
11/18/96 09 51 37
2
24
7
Push 7
11/18/96 09:59.17
2
3
1
11/18/96 09 59 37
2
17
1
11/18/96 09:59 5?
2
45
7
11/18/96 10:00:17
2
43
9
11/18/96 10 00 37
2
28
9
11/18/96 10:00:57
2
14
3
Push 8
11/18/96 10 43 09
1
56
9
11/18/96 10:43:29
1
47
9
11/18/96 10:43 49
1
32
9
11/18/96 10:44:09
1
27
7
11/18/96 10:44 29
1
28
7
11/18/96 10:44 49
2
28
7
Push 9
11/18/96 10:54:29
1
40
5
11/18/96 10 54 49
1
51
9
11/18/96 10:55 09
1
36
9
11/18/96 10:55 29 I 1
27
7
11/18/96 10:55 49
1
24
7
11/18/96 10:56 09
1
21
7
Push 10
11/18/96 11:15.34
1 1
43
5
11/18/96 11 15:54 j 1
66
12
11/18/96 1116:14 j 1
49
12
11/18/96 11 16 34 , 1
35
9
11/18/96 11 16 54 | 1
28
7
11/18/96 11:17 14 ' 1
28
-------
Push Emissions Data Only
Hoppers
Monessen, PA Facility
Push Baghouse Emissions Test
VOCs, CO, and NOx
November 18,1996
voc
CO
NOx
DATE/TIME
ppm
ppm
ppm
Push 11
11/18/96 11.27:29
2
431
3
11/18/96 11:27:49
1
58!
12
11/18/96 11:28 09
1
40
12
11/18/96 11 28:29
1
291
9
11/18/96 11:28:49
1
25j
7
11/18/96 11 29:09
1
2l!
7
Push 12
I
11/18/96 11 39:04
1
36
3
11/18/9611.39:24
59
12
11/18/96 11:39:44
1
43
12
11/18/96 11.40:04
1
30
9
11/18/96 11:40:24
1
25
7
11/18/96 11:40:44
1
25
7
Push 13
11/18/96 11:49:32
1
44
7
11/18/96 11 49 52
1
46
9
11/18/96 11 50 12
1
34
9
11/18/96 11:50:32
1
28
9
11/18/96 11:50:52
1
27
9
11/18/96 11:51 12
1
21
7
Push 14
11/18/96 12:01:45
3
56
9
11/18/96 12:02:05
3
471
14
11/18/96 12 02:25
3
29
121
11/18/96 12:02:45
2
21
9
11/18/96 12:03:05
2
19
9
11/18/96 12:03:25
2
20
9
Push 15
11/18/96 12:11:22
2
23
3
11/18/96 12:11:42
2
51
9
11/18/96 12:12 02
1
44
12
11/18/9612:12:22
1
31
9
11/18/96 12:1242
1
27
9
11/18/96 12:13:02
1
26
9
Push 16
11/18/96 13:01:20
1
38
5
11/18/96 13:01:40
1
60
12
11/18/96 13:02:00
1
47
12
11/18/96 13:02:20
1
32
9
11/18/96 13:02:40
2
26
7
11/18/96 13:03:00
2
27
7
Push 17
11/18/96 13:11:27
2
35
3
11/18/96 13:11:47
1
57
9
11/18/96 13:1207
1
40
12
11/18/96 13:12:27
1
26
9
11/18/96 13:12:47
1
22
9
11/18/96 13:13:07
1
18
7
Push 18
11/18/96 13:23:31
2
67
9
11/18/96 13 23 51
67
14
11/18/96 13:24:11
41
12
11/18/96 13:24:31
30
9
11/18/96 13:24:51
27
9
11/18/96 13:25:11
26
7
Push 19
11/18/96 13:34:37
29
3
11/18/96 13:34:57
52
9
11/18/96 13:35:17
42
12
11/18/96 13:35:37
29
9
11/18/96 13:35:57
24
9
11/18/96 13:36 17
24
9
Push 20
11/18/96 13:44:57 i 1
20
1
11/18/96 13:45:17 | 1
55
9
11/18/96 13:45:37
I 3
65
14
11/18/96 13:45:57
I 3
55
14
11/18/96 13:46:17
I
42
12
11/18/96 13:46:37
33
-------
Koppers
Monessen, PA Facility
Push Baghouse Emissions Test
VOCs, CO, and NOx
November 18,1996
VOC
CO
NOx
DATE/TIME
ppm
ppm
ppm
Push 21 I
11/18/96 13 55:43
40
7
11/18/96 13:56:03
47;
12.
11/18/96 13.56:23
34
_9|
11/18/96 13:56:43
Zi"
9
11/18/96 13:57:03
25
9
11/18/96 13:57:23
25
9;
Push 22
I
jD
11/18/96 14:06 29 ; 1
40
11/18/96 14 06:49 | 1
1 49
13!
11/18/96 14:07 09
1
I 35
10'
11/18/96 14:07 29 i 1
29
9,
11/18/96 11:07:49 1) 24
_ij
11/18/96 14:08:09
1
22
9
Push 23
I
11/18/96 14:15:48
. 21.. 51
9:
11/18/96 14:16:08
1
.... «_
14
11/18/96 14:16:28
37
12,
11/18/96 14:16:48
1 I 27
9
11/18/96 14:17:08
L . .!
24
7
11/18/96 14:17:28
24
9
Push 24 |
11/18/96 14:36 12 ! 1| 20
1
11/18/96 14 36:32
11 53
9
11/18/96 14 36 52
48
12
11/18/96 14:37:12
29' 9
11/18/96 14:37 32
1 1
14
31
11/18/96 14:37:52
6
1
Average ppm
I «
35.21 8.5
VOC CALIBRATION DRIFT CORRECTION CALCULATION
Cavg
I Co
1 Cm
1 Cma
I C
-------
Koppers
Monessen, PA Facility
Push Bag house Emission* Test
VOCs, CO, and NO*
November 19,1996
voc
CO
NOx
DATE/TIME
ppm
Dpm
PP™
Push 1
1 i
11/19/96 07:53*42
1:
HI
1
11/19/96 07 54:02
1 .
51 j
5
11/19/96 07:54 22
1 >
67!
12
11/19/96 07 54:42
1 r
51
12
11/19/96 07:55.02
11
32
7
11/19/96 07:55:22
11
14
3
Push 2
I
11/19/96 08:13:06
4
85
12
11/19/96 08 13 26
2
100
29
11/19^96 08:13:46 I 0|
65
23
11/19/96 08 14 06 . 0 j 41
18
11/19/96 08 14 26 i 01
36 j
14
11/19/96 08 14 46
o!
35;
14
Push 3 ; ! ;
11/19/96 08 28 50 i 2: 20
1
11/19/96 08 29 10
1: 58.
7
11/19/96 08 29 30
1,
60,
12
11/19/96 08:29 50 ¦ 1.
42a
9
11/19/96 08 30 10
1:
21
5
11/19/96 08 30 30
1| 71
3
Push 4 | ;
11/19/96 0850:20
ll
38
3
11/19/96 08.50 40
2|
76
14
11/19/96 08 51 00
1
63
14
11/19/96 08:51 20
1
41
, 12
11/19/96 08 51 40
11
36
9
11/19/96 08:52:00
36
9
Push 5
11/19/96 9:07.40
1
38
3
11/19/96 9 08:00
2
77
14
11/19/96 9 08 20
1
61
15
11/19/96 9 08 40
1
42
12
11/19/96 9 09:00
1
35
10
11/19/96 9 09 20
1
34
9
Push 6
11/19/96 09:25:05
2
37
3
11/19/96 09:25 25
5
100
20
11/19/96 09:25:45
2
103
29
11/19/96 09 26.05
1
S9
23
11/19/96 09:26:25
0
36
16
11/19/96 09:26:45
0
29
14
Push 7
11/19/96 09:37 08
1
21
1
11/19/96 09:37:28
1
51
7
11/19/96 09:37:48
1
53
12
11/19/96 09:38.08
1
41
12
11/19/96 09:38:28
1
34
9
11/19/96 09:38:48
1
27
9
Push 8
11/19/96 09:47:09
1
32
3
11/19/96 0947:29
1
64
14
11/19/96 09 47 49
0
57
16
11/19/96 09:48:09
0
38
12
11/19/96 09 48:29
0
30
9
11/19/96 09:48:49
0
28
9
Push 9
11/19/96 09:57 17
0
6
1
11/19/96 09:57:37
4
65
7
11/19/96 09:57:57
2
108
36
11/19/96 09:58:17
0
73
29
11/19/96 09:58:37
0
37
20
11/19/96 09:58 57
0
19
9
Push 10
1
11/19/96 10:0647
i 4
85
14
11/19/96 10:07,07
2
100
29
11/19/96 10,07 27
0
63
23
11/19/96 10 07 47
0
36
16
11/19/96 1008:07
0
27
14
11/19/96 10:08:27
0
26
12
Push Emissions Data Only
-------
Push Emissions Data Only
Hoppers
Monessen, PA Facility
Push Baghouse Emissions Test
VOCs. CO, and NOx
November 19,1996
voc
CO
NOX
DATE/TIME
ppm
ppm
ppm
Push 11
11/19/96 11 08 43
0
44
3
11/19/96 11 09 03 1 3
101
' 16
11/19/96 11 09 23
0
82
16
11/19/96 11 09 43
0
47
12
11/19/96 11 10 03 ,
0
25
7
11/19/96 11 10 23 I
0
11
3
Push 12 |
11/19/96 11 33:04
2
60
9
11/19/96 11 33 24
2
89
16
[11/19/96 11 33 44
1
69
16
11/19/96 11 34 04
1
44
14
,11/19/96 11 34 24
0
33
12
11/19/96 11 34 44
0
30
9
Push 13
11/19/96 11 43 04
1
63
7
fl 1/19/96 11 43 24
1
83
16
ll 1/19/96 11 43 44
1
55
16
il 1/19/S6 11 44 04
0
35
12
|_11/19/96 11 44 24
0
27
12
M 1/19/96 11 44 44
0
19
7
Push 14
11/19/96 11 51 55
2
49
5
11/19/96 11 52 15
1
75
16
11/19/96 11 52 35
0
55
16
11/T9/96 11 52 55 ^
0
36
14
11/19/96 11 53 15
0
29
12
11/19/96 11 53 35
0
27
12
Push 15
11/19/96 12 02 20
1
24
1
11/19/96 12 02 40
1
58
9
11/19/96 12 03 00
0
55
14
11/19/96 12 03 20
0
38
12
11/19/96 12.03 40
0
32
12
11/19/96 12 04 00
0
28
9
Push 16
11/19/96 12:11:49 H
3
48
5
11/19/96 12.12 09
2
78
16
11/19/96 1212:29
1
55
16
11/19/96 12 12:49
1
35
14
11/19/96 12 13 09
0
27
12
11/19/96 12 13 29
o
26
9
Push 1?
11/19/96 12:20 29
4
51
7
11/19/96 12 20 49
4
110
25
11/19/96 12 21 09
1
89
29
11/19/96 12 21 29
0
45
20
11/19/96 12 21 49
0
27
16
11/19/96 12 22.09
0
17
9
Push 18
11/19/96 13:08 50
1
53
5
11/19/96 13:09 10
1
75
14
11/19/96 13 09 30
0
S3
14
11/19/96 13.09 50
0
36
12
11/19/96 13 10 10
0
32
9
11/19/96 13:10 30
0
32
9
Push 19
11/19/96 13 20 27
5
80
9
11/19/96 13 20 47
4
106
27
11/19/96 13 21 07
1
72
25
11/19/96 13 21.27
1
38
18
11/19/96 1 3 21 47
0
30
16
11/19/96 13 22 07
0
28
14
Push 20
11/19/96 13 30 38
1
62
7
11/19/96 13:30 58
3
100
20
11/19/96 13 31 18
0
79
20
11/19/96 13 31 38
0
44
16
11/19/96 13 31 58
0
32
12
11/19/96 13 32 18
0
29
-------
Hoppers
Monessen, PA Facility
Push Baghouse Emissions Test
VOCs, CO, and NO*
November 19,1996
DATE/TIME
Push 21
VOC
ppm
CO
ppm
NOx
PPm
11/19/96 13 41:09
11/19/96 13 41 29
limm JI3_4J 49
11/19/96 13 42 09
_69!
64 T~
11/19/96 13:42:29
11/19/96 13 42:49
°j_
0!
Push 22
11Z19'?!13 5!_2JL
1*1/19/96 13 51:48
* 1L
' 30 i
28"
i
25
11/19/96 13:52.
11/19/96*13 52
11/19/96 13.52:48
11/19/96 13:53 08
08
2»X
1'
J;
2r
0I
61 !
"86;
89 [
"78.
—
32 I
Push 23
11/19/96 14_0_1:37_
11/19/96 14 01:57
11/19/96 14:02:17
11/19/96 14:02:37
11/19/96 14~02.57"
11/19/96*1-4 03 17 "J"
64
75""
-h
OJ
0*"
0r
~or
Push 24
11/19/96 14:12:00
11/19/96 14 12:20
f-
11/19/96 14 12:40
11/19/96 14 "13 00
11/19/96 14 13 ?0"
11/19/96 14"13 40
lAveraqe ppm
0;
°T"
'"0"
r
" oi"
~Fl
"W"
48:
35"
'33T
jbT
"T:
3/'"
60
54'
Je:
9'
12!
16j
'141
-J2J
_9|
' .9;
_I i
7 i
16"j
^18:
-Mi
J6j
_ 9"
1~6"=
161
12j
"121
"" 9l
48.61
IT4I
VOC CALIBRATION DRIFT CORRECTION CALCULATION
Cavq
I Co
I Cm
I Cma
I Caw
1.0
I 0.0
I 24.1
**
1.01
CO CALIBRATION DRIFT CORRECTION CALCULATION
Cava
I Co
I Cm
I Cma
I Cijas
48.6
I 0.0
I 80 .8
I 80.6
I 48 48
NOx CALIBRATION DRIFT CORRECTION CALCULATION
Cava
I Co
I Cm
I Cma I Cqas
12.4
I 0.0
[ 25.2
I 25.5 I 1255
Cgas * Effluent gas corrartration, corrected tor drift, ppm.
Cavg = Average gas concentration from analyzer
Co - Average of initial and final system cattxaijon bias check for zero.
Cm = Average of initial and final system caUxatton bias cfieck for caGbrabon gas
Cma = Actual concentration of cahbration gas
Pusfi Emissions Data Onty
-------
Koppers
Monessen, PA Facility
Push Baghouse Emissions Test
VOCs, CO, and NO*
November 20,1996
voc
CO
NO*
DATE/TIME
ppm
ppm
ppm
Push 1 I
11/20/96 07 36 56 !
2
44
¦ 5
11/20/96 07,37 16
2
59
S
11/20/96 07 37:36
2
48
10
11/20/96 07 37:56
2
38
8
11/20/96 07 38:16
2
35
8
11/20/96 07:38:36 !
2
35
8
Push 2 j
11/20/96 07 47 46 i
2
4
0
11/20/96 07 48 06 i
1
24
0
11/20/96 07 48 26 I
11/20/96 07 48 46" 1
1
48
6
1
45
9
11/20/96 07 49.06 :
1
32
9
11/20/96 07 49:26 ;
1
19
5
Push 3
11/20/96 08:01:03 I
2
42
4
11/20/96 08 01 23 ! 2
63
9
11/20/96 08.01:43 I
2
S1
10
11/20/96 08:02:03 !
1
38
9
11/20/96 08:02:23 ; 1
33
8
11/20/96 08 02 43 I
1
33
8
Push 4
11/20/96 08 11:47 | 2
30
1
11/20/96 08 12:07
2
58
7
11/20/96 08 12.27 I
1
51
9
11/20/96 08:12:47
1
35
9
11/20/96 08 13 07 '
1
20
4
11/20/96 08:13:27
1
9
1
Push 5
11/20/96 08 29 00
2
38
4
11/20/96 08 29 20
2
57
10
11/20/96 08 29 40
2
48
10
11/20/96 08 30 00
2
37
9
11/20/96 08 30 20
2
34
8
11/20/96 08:30:40
2
34
8
Push 6
11/20/96 08 44,58
2
28
1
11/20/96 08:45:18
2
67
8
11/20/96 08 45 38
2
62
10
11/20/96 08:45:58
2
40
9
11/20/96 08 46 18
2
20
4
11/20/96 08 46:38
2
7
1
Push 7
11/20/96 08:55:41
2
33
4
11/20/96 08.56:01
3
68
15
11/20/96 08 56:21
2
56
13
11/20/96 08:56 41
2
38
11
11/20/96 08 57:01
2
33
9
11/20/96 08.57:21
2
31
9
Push 8
11/20/96 09:05:55
2
34
1
11/20/96 09:06:15
2
65
9
11/20/96 09:06:35
2
52
10
11/20/96 09:06 55
2
32
8
11/20/96 09.07 15
2
14
3
11/20/96 09:07:35
2
5
1
Push 9
11/20/96 09:16:55
4
89
19
11/20/96 09:17 15
2
73
18
11/20/96 09 17:35
2
44
15
11/20/96 09:17:55
2
35
11
11/20/96 09 18.15
I 1
34
11
11/20/96 09.18:35
! 1
33
11
Push 10
!
11/20/96 09 26 14
i
17
0
11/20/96 09 26 34
1
52
6
11/20/96 09 26:54
1
56
9
11/20/96 09 27 14
1
39
9
11/20/96 09:27:34
2
21
4
11/20/96 09 27:54
2
8
1
Push Emissions Data Only
-------
Koppers
Monessen, PA Facility
Push Baghous« Emissions Test
VOCs, CO, and NO*
November 20,1996
voc
CO
NO*
DATE/TIME
PPm
pom
ppm
Push 11 I
'11/20/96 10 31 45 |
2
68
6
;11/20/96 10.32 05 I
2
79
10
(11/20/96 10 32 25
3
71
11
11/20/96 10 32.45
2
57
10
11/20/96 10 33:05
2
47
9
[l 1/20/96 10 33 25
2
44
8
L Push 12 ~1
[11/20/96 1041:10
1
39
3
'11/20/96 10.41 36
1
58
9
j11/20/96 10 41 50
1
44
10
•11/20/96 10-42 10
26
6
,11/20/96 10 42:30 ; 1
11
1
111/20/96 10 42,50 | 1
5
0
' Push 13
111/20/96 10 51.33
1
36
4
|11/20/96 10:51.53
1
61
10
:11/20/96 10 52:13 I
1
51
10
•11/20/96 10 52.33
1
40
9
'11/20/96 10 52:53 | 1
36
8
¦11/20/96 10 53 13 j 1
34
9
Push 14
'11/20/96 '.1 01.50 i 1
18
0
!11/20/96 11 02 10 I 2
54
7
,11/20/96 11 02.30 : 1
58
12
11/20/96 11 02:50 I
1
38
10
11/20/96 11 03 10 1
17
4
11/20/96 11 03:30
1
5
1
r Push 15
111/20/96 11:13 53
81
11
11/20/96 11 14 13
1
78
13
11/20/96 11 14:33
1
52
13
11/20/96 11 14:53
1
38
10
11/20/96 11 15:13
1
33
9
11/20/96 11.15 33
1
33
9
Push 16
11/19/96 11 23:55
49
5
11/19/96 11 24:15
1
75
16
11/19/96 11 24:35
1
55
16
11/19/96 11.24 55
1
36
14
11/19/96 11:25.15
1
29
12
11/19/96 11.25:35
1
27
12
Push 17
11/20/96 11:36.40
1
60
8
11/20/96 11:37:00
1
60
11
11/20/96 11 37:20
1
44
11
11/20/96 11:37-40
1
35
9
11/20/96 11.38:00
1
32
8
11/20/96 11:38:20
1
32
8
Push 18
11/20/96 11:46:58
2
40
4
11/20/96 11:47:18
2
68
11
11/20/96 11:47:38
2
56
12
11/20/96 11:47:58
2
35
8
11/20/96 11:48 18
2
15
3
11/20/96 11 48:38
2
5
1
Push 19
11/20/96 13:06:59
56
7
11/20/96 13:07:19
65
10
11/20/96 13:07:39
52
10
11/20/96 13.07:59
42
8
11/20/96 1308:19
38
8
11/20/96 13.08:39
38
7
Push 20
11/20/96 13 17,30
2
43
4
11/20/96 13 17:50
2
75
13
11/20/96 13:18:10
1
56
15
11/20/96 13:18:30
1
36
12
11/20/96 13:18 50
1
22
7
11/20/96 13 19:10
10
4
Push Emissions Date Only
-------
Koppers
Monessen, PA Facility
Push Baghouse Emissions Test
VOCs, CO, and NO*
November 20,1996
DATE/TIME
VOC
ppm
CO
ppm
NOx
ppm
Push 21 |
11/20/96 13:28:13 , 1
61 I 8
11/20/96 13 28 33 ! 1
63
11
11/20/96 13 28:53 | 1
46
10
11/20/96 13:29:13 ! 1
37
9
11/20/96 13:29:33 1 1
36
9
11/20/96 13.2953 1
36
9
Push 22 I
11/20/96 13 38 10 . 2
21
1
11/20/96 13:38:30 ! 2
61
8
11/20/96 13:38 50 I 2
65
12
11/20/96 13:39:10 ; 2
45
11
11/20/96 13:39:30 i 2
27
7
11/20/96 13:39:50 ' 2
11
4
Push 23 I
11/20/96 13:50 12 ¦ 5
50
5
11/20/96 13 50 32 I 4
92
17
11/20/96 13:50:52
1
66
16
11/20/96 13:51:12
1
39
12
11/20/96 13 51:32 1 1
29
9
11/20/96 13.51 52 1
26
9
Push 24 i
11/20/96 14:00:19 j 1
28
1
11/20/96 14:00:39 ; 5
133
32
11/20/96 14:00 59 , 2
134
46
11/20/96 14 01:19 ! 1
64
29
11/20/96 14 01 39 | 1
27
16
11/20/96 14 01:59 ' 1
10
6
Averaqeppm I 1.6
42.6
8.7
VOC CALIBRATION DRIFT CORRECTION CALCULATION
Cavq
1 CO
1 Cm
1 Cma
1 Cqas
1.6
1 0.0
I 24.5
I 24.4
1.59
CO CALIBRATION DRIFT CORRECTION CALCULATION
Cavq
I Co
I Cm
I Cma
I Cgas
42.6
I 0.0
I 80.3
I 80.6
I 42.76
NO* CALIBRATION DRIFT CORRECTION CALCULATION
Cavq
1 Co
1 Cm
1 Cma
1 Cqas
8.7
, 0.0
I 25.6
I 25.5
8.67
Cgas * Effluent gas concentration, corrected for drift, ppm.
Cavg = Average gas concentration from analyzer
Co = Average of initial and final system calibration bias check for zero.
Cm = Average of initial and final system calibration bias cfteck for calibration gas.
Cflia - Actual concentration of caUbrabort gas
Push Emissions Data Only
-------
Koppers
Monessen, PA Facility
Combustion Stock No. 1
VOCs, CO, and NOx
November 22,199S
Run No. 1
voc
CO
NOx
DATE/TIME
PPtn
ppm
ppm
11/22/96 09:00:04!
1
249
497
11/22/96 09:01 047
4
47
223
11/22/96 09:02:04!
3
75
322
11/22/96 09:03:041
2
169
335
11/22/96 09:04:04!
2
285
348
11/22/96 09:05:04:
293
368
11/22/96 09:06:04
1
413
380
11/22/96 09:07:04
1
65
373
11/22/96 09:08:04
1
5
353
11/22/96 09:09:041
1
5
357
11/22/96 09:10:04 i 1
69
381
11/22/96 09:11 04 ] 1
59
390
11/22/96 09:12:04!
1
21
402
11/22/96 09:13:041
1
21
420
11/22/96 09:14:04 ; 0
33
431
11/22/96 09:15:04'
1
3
425
[Tl/22/96 09:16:041
119
447
11/22/96 09:17:04!
1
349
457
11/22796 09:18:04]
4
533
461
11/22/96 09:19:04
1
489
467
11/22/96 09:20:04
0
523
472
11/22/96 09:21:04
4
49
228
11/22/96 09:22:04
3
31
291
11/22/96 09:23:04
2
19
309
11/22/96 09:24:04
2
13
323
11/22/96 09:25:04
1
9
350
11/22/96 09:26:04
1
7
363
11/22/96 09:27:04
1
5
366
11/22/96 09:28:04
1
5
373
11/22/96 09:29:04
1
3
401
11/22/96 09:30:04
1
25
422
11/22/96 09:31:04
1
147
441
11/22/96 09:32:04
1
187
450
11/22/96 09:33:04
1
343
449
11/22/96 09:34:04
1
209
453
11/22/96 09:35:04
0
81
433
11/22/96 09:36:04
0
35
433
11/22/96 09:37:04
0
13
443
11/22/96 09:38:04
0
5
453
11/22/96 09:39:04
0
7
456
11/22/96 09:40:04
0
1
459
11/22/96 09:41:04
4
37
204
11/22/96 09:42:04
3
81
308
11/22/96 09:43:04
2
159
342
11/22/96 09:44:04
2
237
362
11/22/96 09:45:04
1
339
380
11/22/96 09:46:04
1
37
384
11/22/96 09:47:04
1
5
390
11/22/96 09:48:04
5
394
11/22/96 09:49:04
1
3
401
11/22/96 09:50:04
1
3
403
-------
Koppers
Monessen, PA Facility
Combustion Stack No. 1
VOCs, CO, and NOx
November 22,1996
Run No. 1
VOC
CO
NOx
DATE/TIME
ppm
ppm
ppm
11/22/96 09:51:04
1
3
411
11/22/96 09:52:04
1
17
425
11/22/96 09:53:04
1
345
436
11/22/96 09:54:04
0J
597
439
11/22/96 09:55:041 1
611
444
11/22/96 09:56:041 0
49
430
11/22/96 09:57:041 0
11
433
11/22/96 09:58:04
r 0
I 3
441
11/22/96 09:59:04
0
17
449
Averaqe ppm
I 1.1
126.4
394.6
VOC CALIBRATION DRIFT CORRECTION CALCULATION
Cavq
I Co
I Cm
I Cma
I Cgas
1.1
0.1
25.0
24.4
0.98
CO CALIBRATION DRIFT CORRECTION CALCULATION
Cavq
I Co
I Cm
I Cma
I Cqas
126.4
i -1.0
[ 278.0
I 279.0
I 127.40
NOx CALIBRATION DRIFT CORRECTION CALCULATION
Cavq
I Co
I Cm
I Cma
I Cqas
361.8
I 0.0
I 486.5
I 490.0
I 364.40
Cgas = Effluent gas concentration, corrected for drift, ppm.
Cavg = Average gas concentration from analyzer.
Co = Average of initial and final system calibration bias check for zero.
Cm = Average of initial and final system calibration bias check for calibration
Cma = Actual concentration of calibration gas.
-------
Koppers
Monessen, PA Facility
Combustion Stack No. 1
VOCs, CO, and NOx
November 22,1996
Run No. 2
voc
CO
NOx
DATE/TIME
PPm
PPm
PPm
11/22/96 12:15:15
4
809
446!
11/22/96 12:16:15
4
117'
462|
11/22/96 12:17:15
6
31
464,
11/22/96 12:18:15
5
9
463
11/22/96 12:19:15
5
7
470
11/22/96 12:20:15
5
15
462
11/22/96 12:21:15
37
37
220
11/22/96 12:22:15
32
27
304
11/22/96 12:23:15
20
87
341
11/22/96 12:24:15
14
275
354
11/22/96 12:25:15
11
409
363
11/22/96 12:26:15
9
449
389
11/22/96 12:27:15
8
524
409
11/22/96 12:28:15
6
537
407
11/22/96 12:29:15
5
605
408
11/22/96 12:30:15
5
744
413
11/22/96 12:31:15
4
823
423j
11/22/96 12:32:15
4
900
433
11/22/96 12:33:15
4
890
425
11/22/96 12:34:15
4
904
426
11/22/96 12:35:15
3
1025
450
11/22/96 12:36:15
3
851
447
11/22/96 12:37:15
3
1103
450
11/22/96 12:38:15
3
1236
463
11/22/96 12:39:15
3
1189
464
11/22/96 12:40:15
4
1014
467
11/22/96 12:41:15
37
57
236
11/22/96 12:42:15
29
129
328
11/22/96 12:43:15
22
199
347
11/22/96 12:44:15
14
299
366
11/22/96 12:45:15
11
439
382
11/22/96 12:46:15
9
367
382
11/22/96 12:47:15
7
407
403
11/22/96 12:48:15
6
387
407
11/22/96 12:49:15
5
449
407
11/22/96 12:50:15
4
543
431
11/22/96 12:51:15
4
541
422
11/22/96 12:52:15
4
515
439
11/22/96 12:53:15
3
601
448
11/22/96 12:54:15
3
728
442
11/22/96 12:55:15
3
715
451
11/22/96 12:56:15
3
707
446
11/22/96 12:57:15
3
817
461
11/22/96 12:58:15
3
809
453
11/22/96 12:59:15
2
817
461
11/22/96 13:00:15
3
723
460
11/22/96 13:01:15
36
71
240
11/22/96 13:02:15
29
197
328
11/22/96 13:03:15
22
285
341
11/22/96 13:04:15
14
363
372
11/22/96 13:05:15
10
409
390
-------
Koppers
Monessen, PA Facility
Combustion Stack No. 1
VOCs, CO, and NOx
November 22,1996
Run No. 2
VOC
CO
NOx
DATE/TIME
ppm
ppm
ppm
11/22/96 13:06:15
8
431
406
11/22/96 13:07:15
7
493
424
11/22/96 13:08:15
5
543
412
11/22/96 13:09:15
4
543
434 I
11/22/96 13:10:15
4
653H
424
11/22/96 13:11:15
3
667
430
11/22/96 13:12:15
3
7291 445
11/22/96 13:13:15
3
708
448
11/22/96 13:14:15
3
826
458
Average ppm
8.9
529.8
409.2
VOC CALIBRATION DRIFT CORRECTION CALCULATION
Cavg
I Co
| Cm
I Cma
I Cqas
8.9
0.9
24.8
24.4
8.17
CO CALIBRATION DRIFT CORRECTION CALCULATION
Cavg
I Co
I Cm
[ Cma
I Cnas
529.8
0.0
276.5
279.0
l 534.59
NOx CALIBRATION DRIFT CORRECTION CALCULATION
Cavg
I Co
I Cm
I Cma
I Cqas
409.2
I 0.0
7 489.0
I 490.0
I 410.04
Cgas = Effluent gas concentration, corrected for drift, ppm.
Cavg = Average gas concentration from analyzer.
Co = Average of initial and final system calibration bias check for zero.
Cm = Average of initial and final system calibration bias check for calibration g
Cma = Actual concentration of calibration gas.
-------
Koppers
Monessen, PA Facility
Combustion Stack No. 1
VOCs, CO, and NOx
November 22,1996
Run No. 3
voc
CO
NOx
DATE/TIME
ppm
ppm
ppm
11/22/96 15:00:27
5
12
212
11/22/96 15:01:27
5
27
204
!11/22/96 15:02:27
5
41
247
111/22/96 15:03:27
5
45
264
111/22/96 15:04:27
5
49
394
!11/22/96 15:05:27,
5
58
403
11/22/96 15:06:27
6 i
68 I
413;
11/22/96 15:07:27
7
62
428
11/22/96 15:08:27
8
72
429
11/22/96 15:09:27
5
75
439
11/22/96 15:10:27
4
83
444
11/22/96 15:11:27
5|
89
449
11/22/96 15:12:27
8
90
458:
11/22/96 15:13:27
14l
90l
354
11/22/96 15:14:27
15
103
462
11/22/96 15:15:27
9
109
464
11/22/96 1 5:16:27
8
118
464
11/22/96 15:17:27
5
115
473
11/22/96 15:18:27
8
109
482
11/22/96 15:19:27
9
135
473
11/22/96 15:20:27
6
120
484
11/22/96 15:21:27
4
128
485
11/22/96 15:22:27
4
128
488
11/22/96 15:23:27
3
128
493
11/22/96 15:24:27
7
117
500
11/22/96 15:25:27
9
124
499
11/22/96 15:26:27
5
117
504
11/22796 15:27:27
3
127
503
11/22/96 15:28:27
6
110
513
11/22/96 15:29:27
4
16
175
11/22/96 15:30:27
4
7
307
11/22/96 15:31:27
4
13
352
11/22/96 15:32:27
3
23
375
11/22/96 15:33:27
4
28
394
11/22/96 15:34:27
3
33
407
11/22/96 15:35:27
4
36
420
11/22/96 15:36:27
3
47
425
11/22/96 15:37:27
3
40
444
11/22/96 15:38:27
4
43
446
11/22/96 15:39:27
4
48
454
11/22/96 15:40:27
4
48
462
11/22/9615:41:27
3
55
462
11/22/96 15:42:27
4
56
470
11/22/96 15:43:27
4
55
478
11/22/96 15:44:27
3
63
480
11/22/96 15:45:27
3
63
483
11/22/96 15:46:27
3
61
491
11/22/96 15:47:27
5
68
490
11/22/96 15:48:27
4
72
491
11/22/96 15:49:27
4
74
495
11/22/96 15:50:27
3
71
503
-------
Koppers
Monessen, PA Facility
Combustion Stack No. 1
VOCs, CO, and NOx
November 22,1996
Run No. 3
VOC 1
CO
NOx
DATE/TIME
ppm I
ppm
ppm
11/22/96 15:51:27
4 I
73
505
.11/22/96 15:52:27
3 :
75
506
11/22/96 15:53:27
2 I
74
508
ITT/22/96 15:54:27
4'
76] 510
11/22/96 15:55:27
3 i
81 : 509
11/22/96 15:56:27
3 |
81
I ..512J
11/22/96 15:57 27
~2"T
103
507'
lTT/22/96 15:58:27
6':
68
529
11/22/96 15:59:27
4 i
11
183;
Average ppm
I 4.91
71.8
I 436.6
VOC CALIBRATION DRIFT CORRECTION CALCULATION
Cavg
I Co 1
Cm
I Cma
1 Cgas
4.9
i 0.5 |
24.2
I 24.4
1 4.53
CO CALIBRATION DRIFT CORRECTION CALCULATION
Cavg
1 Co |
Cm
I Cma
1 Cqas
71.8
0.0 !
276.0
! 279.0
1 72.58
NOx CALIBRATION DRIFT CORRECTION CALCULATION
Cavg
1 Co 1
Cm
I Cma
1 Cgas
436.6
1 0.0 I
486.0
1 490.0
1 440.19
Cgas = Effluent gas concentration, corrected for drift, ppm.
Cavg = Average gas concentration from analyzer.
Co ~ Average of initial and final system calibration bias check for zero.
Cm = Average of initial and final system calibration bias check for calibration g
Cma = Actual concentration of calibration gas.
-------
Koppers
Monessen, PA Facility
Combustion Stack No. 2
VOCs, CO, and NOx
November 21,1996
Run No. 1
voc
CO
NOx
DATE/TIME
ppm
ppm
DDm
11/21/96 08:20:4
5
617
335
11/21/96 08:21:4
4
609
337
11/21/96 08:22:41
4
465!
366!
11/21/96 08 23:4
4
331 |
389;
11/21/96 08:24:4:
4
1831
390 I
11/21/96 08:25:4
66
239_[
109
11/21/96 08:26:4
54
325}
259 I
11/21/96 08:27:4
34
3351
307
11/21/96 08:28:4
24
299
334
11/21/96 08:29:4
18
265
357
11/21/96 08:30:4
14
239
373
11/21/96 08:31:4
11
229
386]
11/21/96 08:32:4
10
213
398
11/21/96 08:33:4
9
179
409
11/21/96 08:34:4
8
153
421
11/21/96 08:35:4
8
171
427
11/21/96 08:36:4
8
227
438
11/21/96 08:37:4
7
111
445!
11/21/96 08:38:4
7
171
446
11/21/96 08:39:4
7
89
443
11/21/96 08:40:4
6
7
381
11/21/96 08:41:4
6
5
362
11/21/96 08:42:4
6
5
384
11/21/96 08:43:4
6
5
406
11/21/96 08:44:4
6
5
407
11/21/96 08:45:4
80
77
123
11/21/96 08:46:4
46
49
260
11/21/96 08:47:4
31
29
314
11/21/96 08:48:4
21
19
344
11/21/96 08:49:4
16
13
364
11/21/96 08:50:4
12
9
382
11/21/96 08:51:4
10
7
396
11/21/96 08:52:4
8
67
406
11/21/96 08:53:4
8
357
410
11/21/96 08:54:4
7
383
413
11/21/96 08:55:4
6
171
421
11/21/96 08:56:4
6
693
351
11/21/96 08:57:4
6
969
299
11/21/96 08:58:4
5
812
351
11/21/96 08:59:4
4
469
360
11/21/96 09:00:4
4
415
380
11/21/96 09:01:4
4
243
3961
11/21/96 09:02:4
4
177
400
11/21/96 09:03:4
4
133
415
11/21/96 09:04:4
4
149
449
11/21/96 09:05:4
67
299
118
11/21/96 09:06:4
55
303
259
11/21/96 09:07:4
36
205
304
11/21/96 09:08:4
25
177
332
11/21/96 09:09:4
18
199
354
11/21/96 09:10:4
14
177
i 373
-------
Koppers
Monessen, PA Facility
Combustion Stack No. 2
VOCs, CO, and NOx
November 21,1996
Run No. 1
VOC
CO
NOx
DATE/TIME
ppm
ppm
ppm
11/21/96 09:11:4
L 11
181
388 I
11/21/96 09:12:4
l io'
261
397 I
11/21/96 09:13:4
§1
129
411 !
11/21/96 09:14:4
, 8
119
417j
11/21/96 09:15:4
F 7
121] 424!
11/21/96 09:16:41 7
19
371 ]
11/21/96 09:17:4 j 6
5
336 j
11/21/96 09:18:4
6
5
339
11/21/96 09:19:4
6
5
345
Average ppm
1 15.0
215.5
361.8
VOC CALIBRATION DRIFT CORRECTION CALCULATION
Cavg
I Co
1 Cm
1 Cma
I Cgas
15.0
I 0.5
! 23.5
i 24.4
I 15.38
CO CALIBRATION DRIFT CORRECTION CALCULATION
Cavg
I Co
I Cm
| Cma
I Cgas
215.5
I 0.0
I 79.8
i 80.6
I 217.66
NOx CALIBRATION DRIFT CORRECTION CALCULATION
Cavg
I Co
1 Cm 1 Cma
1 Cgas
361.8
I 0.0
1 489.0 | 490.0
1 362.54
Cgas = Effluent gas concentration, corrected for drift, ppm.
Cavg = Average gas concentration from analyzer.
Co = Average of initial and final system calibration bias check for zero.
Cm = Average of initial and final system calibration bias check for calibratio
Cma - Actual concentration of calibration gas.
-------
Hoppers
Monessen, PA Facility
Combustion Stack No. 2
VOCs, CO, and NOx
November 21,1996
Run No. 2
voc
CO
NOx
DATE/TIME
ppm
ppm
DPm
11/21/96 11:01:51
4
3
385
11/21/96 11:02:51
4
3
393
11/21/9611:03:51
4
3
399
11/21/96 11:04:5i
4!
1
400
11/21/96 11:05:5 i
105
73
126
11/21/96 11:06:5!
59
43
235
11/21/96 11:07:5:
381
27
300
11/21/96 11:08:5:
27
17
341
11/21/96 11:09:5!
20
13
362
11/21/96 11:10:5
16 i
9
384
11/21/96 11:11:51
13:
9
396
11/21/96 11:12:5
Jlj
7
408
11/21/96 11:13:5
10'
7
420
11/21/96 11:14:5!
9; 5
432
11/21/96 11:15:5
9
5
438
11/21/96 11:16:5:
- -gl
5
442
11/21/96 11:17:5'
8'
5
453
11/21/96 11:18:51
8'
5
384
11/21/96 11:19:51
7
5
381
11/21/96 11:20:5!
71
5
409
11/21/96 11:21:5
7
5
388
11/21/96 11:22:5
6
5
390
11/21/96 11:23:5
6
5
423
11/21/96 11:24:5
6
5
467
11/21/96 11:25:5
90
113
169
11/21/96 11:26:5
50
43
279
11/21/96 11:27:5
33
25
319
11/21/96 11:28:5
22
15
296
11/21/96 11:29:5
16
11
290
11/21796 11:30:5
12
7
289
11/21/96 11:31:5
10
5
296
11/21/96 11:32:5
8
5
301
11/21/96 11:33:5
7
3
321
11/21/96 11:34:5
6
3
365
11/21/96 11:35:5
6
3
390
11/21/96 11:36:5
5
3
403
11/21/96 11:37:5
5
3
412
11/21/96 11:38:5
5
3
417
11/21/96 11:39:5
5
3
422
11/21/96 11:40:5
5
3
415
11/21/96 11:41:5
5
3
349
11/21/96 11:42:5
4
3
368
11/21/96 11:43:5
4
I 1
374
11/21/96 11:44:5
4
1
378
11/21/96 11:45:5
87
77
126
11/21/96 11:46:5
51
43
232
11/21/96 11:47:5
33
25
287
11/21/96 11:48:5
22
17
316
11/21/96 11:49:5
16
13
332
11/21/96 11:50:5
13
9
354
11/21/96 11:51:5
10
7
323
-------
Koppers
Monessen, PA Facility
Combustion Stack No. 2
VOCs, CO, and NOx
November 21,1996
Run No. 2
VOC
CO
NOx
DATEHIME
ppm
ppm
ppm
11/21/96 11
52:5
9
7
313
11/21/96 11
53:5
8
5
329
11/21/96 11
54:5
6
5
338
11/21/96 11
55:5
6
5
352
11/21/96 11
56:5
5
5
353
11/21/96 11
57:5
5
5
376
11/21/96 11
58:5
5
5
410
11/21/96 11
59:5
5
5
438
11/21/96 12
00 5
5
5
446
Average ppm
[ 18.3
I 12.8
3S5.61
VOC CALIBRATION DRIFT CORRECTION CALCULATION
Cavg
I Co
I Cm
I Cma
I Cgas
16.3
0.1
I 24.5
I 24.4
I 16.20
CO CALIBRATION DRIFT CORRECTION CALCULATION
Cavq
I Co
I Cm
I Cma
I Cgas
12.8
0.2
I 80.2
I 80.6
I 12.69
NOx CALIBRATION DRIFT CORRECTION CALCULATION
Cavq
I Co
I Cm
I Cma
I Cgas
355.6
I 0.2
I 489.0
I 490.0
I 356.27
Cgas = Effluent gas concentration, corrected for drift, ppm.
Cavg = Average gas concentration from analyzer.
Co = Average of initial and final system calibration bias check for zero.
Cm = Average of initial and final system calibration bias check for calibrate
Cma = Actual concentration of calibration gas.
-------
Koppers
Monessen, PA Facility
Combustion Stack No. 2
VOCs, CO, and NOx
November 21,1996
Run No. 3
voc
CO
NOx
DATE/TIME
ppm
ppm
ppm
11/21/96 14:25:1
3
13
479
11/21/96 14:26:1
79
243
232
11/21/96 14:27:1
46
43
326
11/21/96 14:28:1
30
27
365
11/21/96 14:29:1
20
19
391
11/21/96 14:30:1
14
407
11/21/96 14:31:1
11
11
424
11/21/96 14:32:1
8
11 i
443 I
11/21/96 14:33:1
7
91
454!
11/21/96 14:34:1
7
7 i
467,
11/21/96 14:35:1'
6
7
479
11/21/96 14:36:1
5
486 I
11/21/96 14:37:1
5
7 j 494
11/21/96 14:38:1
5
7
499
11/21/96 14:39:1
5
509
11/21/96 14:40:1
5l
7'
5151
11/21/96 14:41:1
5
7
520
11/21/96 14:42:1
5
7
526
11/21/96 14:43:1
5
7
529
11/21/96 14:44:1
6
7
537
11/21/96 14:45:1
5
9
523
11/21/96 14:46:1
64
133
271
11/21/96 14:47:1
39
37
300
11/21/96 14:48:1
26
23
308
11/21/96 14:49:1
17
15
326
11/21/96 14:50:1
13
11
337
11/21/96 14:51:1
9
9
360
11/21/96 14:52:1
7
7
370
11/21/96 14:53:1
6
5
397
11/21/96 14:54:1
5
5
455
11/21/96 14:55:1
4
5
470
11/21/96 14:56:1
4
5
485
11/21/96 14:57:1
4
3
496
11/21/96 14:58:1
3
3
500
11/21/96 14:59:1
3
3
509
11/21/96 15:00:1
3
3
516
11/21/96 15:01:1
3
5
522
11/21/96 15:02:1
3
3
527
11/21/96 15:03:1
3
3
526
11/21/96 15:04:1
3
3
539
11/21/96 15:05:1
3
7
519
11/21/96 15:06:1
78
227
250
11/21/96 15:07:1
46
45
353
11/21/96 15:08:1
30
81
386
11/21/96 15:09:1
21
19
413
11/21/96 15:10:1
16
13
377
11/21/96 15:11:1
12
15
342
11/21/96 15:12:1
10
377
347
11/21/96 15:13:1
8
207
358
11/21/96 15:14:1
7
29
372
11/21/96 15:15:1
7
51
405
-------
Koppers
Monessen, PA Facility
Combustion Stack No. 2
VOCs, CO, and NOx
November 21,1996
Run No. 3
VOC
CO
NOx
DATE/TIME
ppm
ppm
ppm
11/21/96 15:16:1
6
101
439
11/21/96 15:17:1
6! 9
409
11/21/96 15:18:1
6! 8
431
!l 1/21/96 15:19:1
5
39
497
111/21/96 15:20:1
5
41
514
111/21/96 15:21:1
5
57
521
111/21/96 15:22:1
5
43
527
111/21/96 15:23:1
5
15
536
|11/21/96 15:24:1
5
7
• 543
lAverage ppm
I 13.1
I 35.9
I 439.3
VOC CALIBRATION DRIFT CORRECTION CALCULA1
Cavg
| Co
I Cm
I Cma
I Cgas
13.1
! -0.4
25.0
; 24.4
I 12.97
CO CALIBRATION DRIFT CORRECTION CALCULATION
Cava
I Co
I Cm
I Cma
I Cgas
35.9
i 0.2
! 81.7
I 80.6
I 35.31
NOx CALIBRATION DRIFT CORRECTION CALCULATION
Cavg
I Co
I Cm
I Cma
I Cgas
439.3
I 0.2
! 490.0
I 490.0
I 439.28
Cgas = Effluent gas concentration, corrected for drift, ppm.
Cavg = Average gas concentration from analyzer
Co = Average of initial and final system calibration bias check for zero.
Cm = Average of initial and final system calibration bias check for calibratio
Cma = Actual concentration of calibration gas.
-------
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ETA Revised 05-01-92
OONTHUHJ ON VfO P0*»l NUfcBBt
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£ <^F3
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ETA Revised 05-01-92
CONTMJED ON WO FOAJ NIASSI
-------
-------
EPA METHOD S
BLANK ANALYTICAL DATA FORM
Client: Koppers
Project No: 937
Location: Coke Push Baghouse
No. 1 Comb. Stack
No. 2 Comb. Stack
Sample date:
Analysis date:
Technician:
11/18-22/96
11/25-26/96
PJ
ACETONE BLANK
UNIT
Acetone rinse container No.
286
Density of acetone (pa)
g/rnl
0.7857
Acetone blank volume (Va)
ml
140
Average gross wt.
mg
67121.80
Average tare wt.
mg
67121.70
Weight of blank (Ma)
mq
0.10
Acetone blank wt. (Ca=Ma/(Va x Pa))
ma/a
0.0009
Note:
In no case should a blank resdue greater than 0.01 mg/g or 0.001%
-------
EPA METHOD 5
ANALYTICAL PARTICULATE DATA
Client: Koppers
Sample date:
11/18-20/96
Project No: 937
Analysis date:
11/25-27/96
Location: Coke Push Baghouse
Technician:
PJ
IUNIT
RUN 1
RUN 2
RUN 3
ACETONE RINSE
Acetone rinse container No.
268
269
270
Density of acetone (pa)
g/ml
0.7857
0.7857
0.7857
Acetone rinse volume (Vaw)
ml
100
100
100
Acetone blank (Ca)
mg/g
0.0009
0.0009
0.0009
Wa =(Ca) (Vaw) (pa)
mg
0.07
0.07
0.07
Average gross wt.
mg
93600.00
104019.60
106843 30
Average tare wt.
mg
93588.85
104011.20
106840.00
Acetone blank wt. (Wa)
mg
0.07
0.07
0.07
Wt. of particulate in acetone rinse (Ma)
mg
11.08
8.33
3.23
FILTER
Filter No.
312
314
313
Average gross wt.
mg
412.65
412.10
413.10
Average tare wt.
mg
412.25
410.85
412.70
Wt. of particulate on filter (Mf)
mg
0.40
1.25
0.40
FINAL WEIGHT
Wt. of particulate in acetone rinse (Ma)
mg
11.08
8.33
3.23
Wt. of particulate on filter (Mf)
ma
0.40
1.25
0.40
TOTAL WT OF PARTICULATE (Mn)
mg
11.48
9.58
-------
EPA METHOD 5
ANALYTICAL PARTICULATE DATA
Client: Koppers
Sample date:
11/22/96
Project No: 937
Analysis date:
11/25-27/96
Location: No. 1 Combustion Stack
Technician:
PJ
UNIT
RUN 1
RUN 2
RUN 3
ACETONE RINSE
Acetone rinse container No.
271
272
273
Density of acetone (pa)
g/mi
0.7857
0.7857
0.7857
Acetone rinse volume (Vaw)
ml
130
105
130
Acetone blank (Ca)
mg/g
0.0009
0.0009
0.0009
Wa =(Ca) (Vaw) (pa)
mg
0.09
0.07
0.09
Average gross wt.
mg
94072.80
95309.50
101265.70
Average tare wt.
mg
94044.85
95299.05
101255.90
Acetone blank wt. (Wa)
mg
0.09
0.07
0.09
Wt. of particulate in acetone rinse (Ma)
mg
27.86
10,38
9.71
FILTER
Filter No.
318
344
345
Average gross wt.
mg
418.10
412.75
416.60
Average tare wt.
mg
411.05
411.00
413.40
Wt. of particulate on filter (Mf)
mg
7.05
1.75
3.20
FINAL WEIGHT
Wt. of particulate in acetone rinse (Ma)
mg
27.86
10.38
9.71
Wt. of particulate on filter (Mf)
, mfl
7.05
1.75
3.20
TOTAL WT OF PARTICULATE (Mn)
ma
34.91
12.13
-------
EPA METHOD 5
ANALYTICAL PARTICULATE DATA
Client: Koppers
Sample date:
11/21/96
Project No: 937
Analysis date:
11/25-27/96
Location: No. 2 Combustion Stack
Technician:
PJ
UNIT
RUN 1
RUN 2
RUN 3
ACETONE RINSE
Acetone rinse container No.
283
284
285
Density of acetone (pa)
g/ml
0.7857
0.7857
0.7857
Acetone rinse volume (Vaw)
ml
100
140
140
Acetone blank (Ca)
mg/g
0.0009
0.0009
0.0009
Wa =(Ca) (Vaw) (pa)
mg
0.07
010
0.10
Average gross wt.
mg
66668.40
66093.90
66609.20
Average tare wt.
mg
66651.85
66083.45
66534.55
Acetone blank wt. (Wa)
mg
0.07
0.10
0.10
Wt. of particulate in acetone rinse (Ma)
mg
16.48
10.35
74.55
FILTER
Filter No.
318
344
345
Average gross wt.
mg
418.10
412.75
416.60
Average tare wt.
mg
411.05
411.00
413.40
Wt. of particulate on filter (Mf)
mg
7.05
1.75
3.20
FINAL WEIGHT
Wt. of particulate in acetone rinse (Ma)
mg
16.48
10.35
74.55
Wt. of particulate on filter (Mf)
mg
705
1.75
3.20
TOTAL WT OF PARTICULATE (Mn)
mg
23.53
12.10
-------
AIR QUALITY SERVICES, INC.
4527 Clairton Boulevard
Pittsburgh, FA 15236
(412) 881-5630
TABLE I
ANALYSIS OF IMPINGER WATER FOR INSOLUBLE PARTICULATE
OPTIMAL TECHNOLOGIES, INC.
U-PARC
575 WILLIAM PITT WAY
PITTSBURGH, PA 15238
SAMPLES RECEIVED: NOVEMBER 26, 1996
PROJECT PURCHASE ORDER #18476
OPTIMAL
TECHNOLOGIES
ID
AQS
LABORATORY
NUMBER
PARTICULATE
WEIGHT
MILLIGRAMS
COKE
PUSH
RUN
BAGHOUSE
#1
73282
0.45
COKE
PUSH
RUN
BAGHOUSE
#2
73283
0.27
COKE
PUSH
RUN
BAGHOUSE
#3
73284
0.07
#1
COMB
RUN
STACK
#1
73285
0.74
#1
COMB
RUN
STACK
*2
73286
0.62
#1
COMB
RUN
STACK
#3
73287
0.94
#2
COMB
RUN
STACK
#1
73288
0.95
#2
COMB
RUN
STACK
#2
73289
1.10
*2
COMB
RUN
STACK
#3
73290
1.40
BLANK
73291
0.001
FILTERS WERE WEIGHED ON A MICRO BALANCE CALIBRATED WITH WEIGHTS
_f$CJS$BLE TO THE-JJAT^NAL INSTITUTE OF STANDARDS AND TECHNOLOGY.
"""" .¦?yA*
• *' JOB 5430
-------
-------
KOPPERS
COKE PUSH BAGHOUSE
NOVEMBER 18,19 AND 20,1996
PROJECT NO. 937
PARTICULATE EMISSIONS
SYMBOL DESCRIPTION RUN NO I RUN NO 2 RUN NO 3 AVERAGE
Theta =
Duration of test, mm.
48
48
48
48
Vm -
Dry sample volume (meter conditions), cu. ft.
38.257
36.723
37.476
37.485
SQRT(dP)=
Average of square roots of pitot pressure, in. water
1.297
1.261
1.292
1.283
dli
Orifice pressure drop, in. water
2.15
2.02
2.13
2.10
Ts
Average slack temperature, deg F
88.8
83.5
74.2
82.2
Tm =
Average dry gas meter temperature, deg. F
546
45.0
38.0
45.9
C02
C02 in stack gas, %
0.0
0.0
0.0
0.0
02
02 in stack gas, %
21 0
21.0
21.0
21 0
CO+N2 »
CO and N2 in stack gas, %
79.0
79.0
79.0
790
Pbar =
Barometric pressure, in. Hg.
29.61
29.24
29 40
2942
Pa
Static pressure, in. water
-0.62
-0.60
-0.58
-060
Ps
Stack pressure (absolute), in. Hg.
2956
29.20
29.36
29.37
Cp
Pilot correction factor, dimenskuiless
0.84
0.84
0.84
0.84
Y
Dry gas meter correction factor
0.972
0.972
0.972
0.972
Dn
Diameter of nozde, in.
0.1820
0.1820
0.1820
0.1820
Ds
Diameter of stack, in.
7125
71.25
71.25
71.25
Vk
Volume of Liquid collected in impmgers and silica gel, mi
16.4
17.6
12.1
15.4
Fh
Front half catch, nag
11.48
9.58
3.63
8.23
Bh
Back half catch, mg
0.45
0.27
0.07
026
Mn
Total particulate catch, mg
11.93
9.85
3.70
849
CALCULATED VALUES
An =
Area of the nozzle, sq. ft.
«= 1.807E-04 1
807E-04
1.807E-04
1.807E-04
A
Area of the stack, sq. ft.
27.688
27.688
27.688
27.688
Md
Dry molecular weight of stack gas, dry basts, Ib/ib-mole
28.84
28.84
28.84
28.84
Vw(std) -
Volume of liquid collected, ca. ft.
0.772
0.828
0.570
0.723
Ms -
Molecular weight of stack gas, wet basis, Ib/lb-mole
28.62
28.60
28.68
28.63
Vm(std) =
Dry sample volume (standard conditions), dscf
37.945
36.643
38.137
37.575
Vs
Stack velocity, ft/sec
75.02
73.05
73.90
73.99
Bws -
Moisture content of the gas stream, %
2.0
2.2
1.5
1.9
Qs
Stack gas flow, acfin
124629
121357
122769
122918
Qsd
Stack gas flow, dscfm
116094
112527
117286
115302
I
Isokinetic ratio, %
104.4
104.0
103.8
104.1
PARTICULATE EMISSION SUMMARY
Cs
Particulate concentration, gr/dscf
0.0048
0,0041
0.0015
0.0035
E
Particulate emission rate, lb/hr
48
4.0
1.5
-------
KOPPERS
NO. 1 COKE OVEN BATTERY COMBUSTION STACK
NOVEMBER 22,1996
PROJECT NO. 937
PARTICULATE EMISSIONS
SYMBOL DESCRIPTION RUN NO. I RUN NO. 2 RUN NO. 3 AVERAGE
Theta
Duration of test, nun
-
120
120
120
120
Vm
=
Dry sample volume (meter conditions), en. ft.
=
90.898
89.514
76.077
85.496
SQRTfdPJ
!=
Average of square roots of pilot pressure, ia. water
=
0.171
0 169
0.144
0.161
dH
=
Orifice pressure drop, in. water
=
1868
1.858
1.289
1.672
Ts
Average stack temperature, deg. F
=
607.7
602.2
606.4
605.4
Tm
=
Average dry gas meter temperature, deg. F
=
49.9
518
52.2
51.3
C02
=
C02 m stack gas, %
-
5.3
5.7
6.0
5.7
02
=
02 in stack gas. %
=
11.7
12.3
12.0
12.0
CO+N2
s
CO and N2 in stack gas, %
=
83.0
82.0
82.0
82.3
Pbar
=
Barometric pressure, in. fig.
-
29.54
29.54
29.54
29.54
Pa
=
Static pressure, in. water
=
-1.67
-1.63
-1.65
-165
Ps
=
Stack pressure (absolute), in. Hg.
=
29.42
29.42
29.42
29.42
Cp
=
Pitot correction factor, dimeasioaless
=
0.84
0.84
0.84
0.84
Y
=
Dry gas meter correction factor
=
0.985
0.985
0.985
0.985
Dn
=
Diameter of nozzle, in.
0.6200
0.6200
0.6200
0.6200
Ds
=
Diameter of stack, in.
=
156.0
156.0
156.0
1560
Vic
=
Volume of liquid collected in impmgears and silica gel, ml
-
386.8
418.2
353.4
386.1
Fh
=
Front half catch, mg
=
34.91
12.13
12.91
19.98
Bh
=
Back half catch, mg
0.74
0.62
094
0.77
Mn
Total particulate catch, mg
CALCUlJVTED VALUES
35.65
12.75
13.85
20.75
Ah
=
Area of the nozzle, sq. ft.
-
2.097E-03 2.097E-03
2.097E-03
2.097E-03
A
=
Area of die stack, sq. ft.
=
132.732
132.732
132.732
132.732
Md
*
Dry molecular weight of stack gas, dry basis, ib/Ib-mols
29.32
29.40
29.44
29.39
Vw{std)
s=
Volume of liquid collected, cu. ft.
=
18.207
19.685
16.635
18.176
Ms
m
Molecular weight of stack gas, wet basis, Ib/Ib-mole
-
27.45
27.36
27 39
27.40
Vm(std)
=
Dry sample volume (standard conditions), dscf
=
91.924
90.186
76.481
86.197
Vs
XT
Stack velocity, fl/sec
14.12
13.94
11.90
13.32
Bws
=
Moisture content of die gas stream, %
=
16.5
17.9
17.9
17.4
Qs
=
Stack gas flow, acfm
=
112451
111017
94771
106080
Qsd
=
Stack gas flow, dscfm
-
45658
44549
37880
426%
I
=
Isokinetic ratio, %
=
106.3
106.9
106.5
106.6
PARTICULATE EMISSION SUMMARY
Cs
3
Particulate concentration, gr/dscf
=
0.0060
0.0022
0.0028
0.0037
E
*
Particulate emission rate, Ib/hr
=
2.3
0.8
0.9
-------
KOPPERS
NO. 2 COKE OVEN BATTERY COMBUSTION STACK
NOVEMBER 21,1996
PROJECT NO. 937
PARTICULATE EMISSIONS
SYMBOL DESCRIPTION RUN NO I RUN NO. 2 RUN NO. 3 AVERAGE
TbeU
=
Duration of test, mm
-
120
120
120
120
Vtn
=
Dry sample volume (meter conditions), ca ft.
69.131
62.633
74.318
68.694
SQRT(dP)
1=
Average of square roots of pitot pressure, in. walw
=
0.143
0.128
0.134
0.135
dH
=
Orifice pressnre drop. in. water
=
1.271
1.010
1.173
1.151
Ts
=
Average slack temperature, deg. F
=
542.5
554.6
562.0
553.0
Tm
3=
Average dry gas meter temperature, deg. F
=
47.5
58.1
55.5
53.7
C02
SB
C02 in slack gas, %
=
43
4.0
5.0
4.5
02
=
02 in stack gas, %
=
12.7
12.3
11.0
12.0
CO+-N2
ss
CO and N2 in slack gas, %
=
82.8
83.7
84.0
83,5
Pbar
=
Barometric pressure, in. Hg.
=
29.42
29.40
2936
29.39
Pa
=
Static pressure, in. water
-1.40
-1.30
-1.37
-1.36
Ps
m
Stack pressure (absolute), in. Hg.
=
29.32
29.30
29.26
29.29
Cp
=
Pitot correction factor, dimenxkmicss
=
0.84
0.84
0.84
0.84
Y
=
Dry gas meter correction factor
=
0.985
0.985
0.985
0.985
Dn
*
Diameter of nozzle, in.
¦at
0.6200
0.6200
0.6200
0.6200
Ds
=
Diameter of stack, in.
=
120.0
120.0
120.0
120.0
Vic
•
Volume of liquid collected in impingers aad silica gel, ml
=
230.3
226.4
251.5
236.1
Fh
Front half catch, mg
=
23.53
12.10
77.75
37.79
Bh
—
Back half catch, mg
=
0.95
1.10
1.40
1.15
Mb
Total particulate catch, mg
24.48
13.20
79.15
38.94
CALCULATED VALUES
An
=
Area of the nozzle, sq. ft.
2.097E-03 2.097E-03
2.097E-03
2.097E-03
A
=
Area of the stack, sq. ft.
=
78.540
78.540
78.540
78.540
Md
az.
Dry molecular weight of stack gas, dry basis, Ib/lb-mofe
=
29J23
29.13
29.24
29.20
Vw(std)
ss
Volume of liquid collected, cu- ft.
=
10.840
10.657
11.838
11.112
Ms
=
Molecular weight of stack gas, wet basis, fij/Ib-raofc
*
27.73
27.49
27.69
27.64
Vm(std)
=
Dry sample volume (standard conditions), dscf
m
69.855
61.911
73.762
68.509
Vs
=
Stack velocity, ft/sec
-
11.40
10.32
10.81
10 84
Bws
ms
Moisture content of the gas stream, %
=
13.4
14.7
13.8
14.0
Qs
—
Stack gas flow, acfm
a
53721
48632
50941
51098
Qsd
_
Stack gas flow, dstfm
* ¦
24011
21141
22186
22446
I
=
Isokinetic ratio, %
=
90.9
91.4
103.9
95.4
PARTICULATE EMISSION SUMMARY
Cs
*
Particulate concentration, gr/dscf
ss
0.0054
0.0033
0.0165
0.0084
E
Particulate emission rate, lb/hr
=
1.1
0.6
3,1
-------
HOPPERS
COKE PUSH BAGHOUSE
NOVEMBER 18,19,20,1996
NOx, VOC AND CO EMISSIONS
Ron No. I Run No, 2 Ron No 3 Avg,
Qsd = Stack gas flow, dsc&n - I16094 1I2527 117286 115302
NOx EMISSIONS
Cppm = NOx concentration, ppm = 8.85 12.55 8.67 10.02
E = NOx Emissions, IbAr = 7.35 10.10 7.27 8.24
VOC EMISSIONS
Cppm = VOC concentration, ppm - 1.42 101 1.59 1.34
E = VOC Hnussioiis. Ib/hr as propane = 1.13 0.78 1.28 1.06
CO EMISSIONS
Cppm = CO concentration, ppm = 35.11 48.48 42.76 42.12
-------
KOPPERS
NO. 1 COMBUSTION STACK
NOVEMBER 22,1996
NOx, VOC AND CO EMISSIONS
Qsd = Stack gas flow, dscfm
Cppm = NOx coacealraUoo, ppm
E - NOx Emissions, Ib/hr
Run No. 1 Ron No. 2 Run No. 3
45658 44549 37880
NOx EMISSIONS
VOC EMISSIONS
Cppm = VOC concentration, ppm
E = VOC Emissions, lb/hr as propane
364.40
118%
0.98
0.31
410.04
130.61
8.17
2.49
440.19
119.23
4.53
1.17
Avg.
426%
404.88
122.93
4.56
1.32
CO EMISSIONS
Cppm = CO concentration, ppm
E = CO Emissions, lb/hr
127.40
25.32
534.59
103.65
72.58
11.97
244.86
-------
KOPPERS
NO. 2 COMBUSTION STACK
NOVEMBER 21,1998
NOx, VOC AND CO EMISSIONS
Run No 1 Rim No 2 Run No 3 Avg.
Qsd = Stack gas flow, dsc&n = 24011 21141 22186 22446
NOx EMISSIONS
Cppm = NOx concentration, ppm = 362.54 356.27 439.30 386.04
E = NOx Emissions. Ib/hr = 62.24 53.86 69.69 61 93
VOC EMISSIONS
Cppm = VOC cooceatrafcan, ppm = 15.38 16-20 12.97 14.85
E = VOC Emissions, H>/hr as propane = 2.53 2.34 1.97 2.28
CO EMISSIONS
Cppm = CO concentration, ppm = 217.66 12.69 35.31 88.55
-------
-------
NOZZLE CALIBRATION DATA FORM
Calibrated by
sii5S
Nozzle
identification
number
ozzle Diameter
AD,
mm (in.)
avg
mm (in. )
G.
Q; O O O
wheret
aDt , , = three different nozzles diameters, mm (in.)j each
' ' ' diameter must be within (9.025 mm) 0.001 in.
k AD = maximum difference between any two diameters, mm (in.),
AD £(0.10 mm) 0.004 in.
-------
STACK GAS THERMOCOUPLE CALIBRATION
Clienl:
Location: Mo*-* ¦s'v-'-t 0_-sc
Dale: i2~5~c7c
Tecluiician: $ S k &W.C, h C!J s. <.
Hvit J
Com fe» Q+OllK%
TEMPERATURE
SOURCE
TEMPERATURE
REFERENCE
•/. DIFFERENCE
r c<_ V H
a r
6 Y
\>£
6u+-/
A 1 3
a 9
Ou
H 7 O
1 Go
-------
DRY GAS METER AND ORIFICE CALIBRATION
09/12/96 OPERATOR: JEP . CONSOLE: 80902
WET TEST METER GAS VOLUMES AND TEMPERATURES
Orifice
Initial
Final
Net
Avg.
Manometer
Reading
Reading
Volume
Temp.
Setting .
ft
Temp.
ft
Temp.
(in. H20)
(cf)
(deg F)
(cf)
(deg F)
(ft)
(F)
Vw
Tw
Vw
Tw
Vw
Tw
1.00
0.000
66.5
5.000
66.5
5.000
66.5
1.50
0.000
66.5
5.000
66.5
5.000
66.5
2.00
0.000
66.5
5.000
66.5
5.000
66.5
3.00
0.000
66.5
4.997
66.5
4.997
66.5
DRY TEST METER VOLUMES AND TEMPERATURES
Orifice
Manometer
Initial
Final
Temperature
Net
Avg.
Setting
Reading
Reading
Inlet
Outlet
Volume
Temp.
(in. H20)
(cf)
(cf)
(deg f)
(degf)
(ft)
(degf)
Vd
Vd
Ti
Td
Vd
Td
1.00
960.949
966.121
74.0
72.0
5.172
73.0
1.50
967.170
972.359
76.0
72.0
5.189
74.0
2.00
973.397
978.601
77.0
73.0
5.204
75.0
3.00
979.627
984.821
74.0
72.0
5.194
73.0
Orifice
Total
Barometer
Manometer
Test
Reading
Setting
Time
Inches
(in. H20)
(min.)
("He)
1.00
9.150
29.10
1.50
7.483
29.10
2.00
6.567
29.10
3.00
5.317
29.10
Average
Gamma
delta H
0.976
1.897
0.974
1.900
0.971
1.947
0.967
1.924
0.972
-------
DRY GAS METER AND ORIFICE CALIBRATION
10/17/96 OPERATOR: JEP CONSOLE: 80872
WET TEST M KTER CAS VOU HUES AND TEMPERATURES
Orifice
Initial
Final
Net
Avg
Manometer
Reading
Reading
Volume
Temp
Setting
ft
Temp
ft
Temp
(m. H20)
(of)
I" )
(cl)
(deg F)
(«)
(10
Vw
Tw
Vw
Tw
Vw
Tw
1.00
\ M)
0_000 _
DOCK)
0 000 ""
0 000
70 5
^ 70 5
" 705
70 5
5 002
70.5
5 002
70 5
4.999
70.5
4999
705
2.00
voo
5 000
70.5
5 000
70 5
5.000
700
5 CXXJ
70 3
DRY TEST M ETER VOLUMES AND TEMPERATURES
Orifice
Manometer
Initial
Final
Temperature
Net
Avg.
Setting
Reading
Reading
Inlet
Outlet
Volume
Temp.
(in. H20)
(cQ
(cf)
(degf)
(degf)
(ft)
(degf)
Vd
Vd
Ti
Td
Vd
Td
1.00
956 447
961 628
850
81.0
5.181
83.0
1.50
962.663
967 823
85.0
81.0
5 160
83.0
2.00
968865
974 044
85.0
81.0
5.179
83.0
3.00
975.066
980 246
86.0
81.0
5.180
83.5
Orifice
Total
Barometer
Manometer
Test
Reading
Setting
Time
Inches
(in. H20")
(min.)
cm
1.00
8.867
29 30
1.50
7.317
29 30
2.00
6333
29 30
3.00
5 167
29 30
Average
Gamma
delta H
0.986
1.762
0.988
1.802
0.983
1.799
0.982
1.793
0.985
-------
TYPE S PITOT TUBE CONSTRUCTION SPECIFICATIONS
TYPE S PITOT TUBE NO. - DATE .'My-fC. TECHNICIAN PJ~
CONSTRUCTION STANDARDS ;
t. pi - batwian 0.41 and O.tS c«n(lmt(«rt
i. - Pt i.oi 01 <*£ i.io o«
s, gl . a2 < 10*
4. I1.IKI'
I. 2 ca
«. W £ 0.08 cai
f
»«••&¦«• C2
»-»•! Mil
r— ^ lat <«•»->
k' ^ ^
-------
TYPE S PITOT TUBE ALIGNMENT SPECIFICATIONS
Client
Location
Date
Technician
P . km; t« C
FITOT ALIGNMENT STANDARDS
1. %Z 3/4 In.
i, lp mutt bt Mgh«r than Hp
3. Zjl.10 e«
tit*
1
DM I »«t»t Ml
(M r*«it
tBD
3>
4. t > 3 to.
tIM I *tf*f tVM
*s>
«t«m m«ii
JWJ
X -
9.,o
Z,l
n
imnai «oin»
MlOvM »»«•»
itmimii tmi
• t*!«» fUM
tl lp Mgh«r IfttA Hp ss
1/4 k. '«t «. • t/« «.
niin*i itmi
-------
Barometer Calibration
Field Barometer Number 2
February 1,1996
Date
Time
NWS
Field
Barometer
Corrected
Difference
01/18/96
07:00 AM
30.08
29.24
30.08
0.00
01/18/96
12:00 PM
30.02
29.15
29.99
0.03
01/19/96
07:00 AM
29.43
28.75
29.59
-0.16
01/19/96
12:00 PM
29.74
28.84
29.68
0.06
01/22/96
07:00 AM
30.42
29.47
30 31
0.11
01/22/96
12:00 PM
30.40
29.45
30.29
0.11
01/24/96
07:00 AM
29.51
28.64
29.48
0.03
01/24/96
12.00 PM
30.27
29.45
30.29
-0.02
01/25/96
07:00 AM
30.40
29.46
30.30
0.10
01/25/96
12:00 PM
30.14
29.24
30.08
0.06
01/29/96
07.00 AM
30.12
29.25
30.09
0.03
01/29/96
12:00 PM
30.15
29.25
30.09
0.06
Average 0.034
Note: Correction for Altitude = 0.855
Note: Correction for Gravity = -0.015
-------
pennState
C53
Continuing Education
Visible Emissions Evaluation Program
this certifies that
JIM PHILLIPPI
has met the specifications of Federal Reference Method 9 and qualified as a visible emissions evaluator. Maxi-
mum deviation on white and black smoke did not exceed 7.5% opacity and no single error exceeding 15%
opacity was incurred during the certification test conducted by The Pennsylvania State University.
Certified, from and to i \
{ '1^. t 1 5 7 —
Recertified, from and lo
i And Dean for
g tnd Disunce Educt
Project Director of ViiibJe Emuiions
Training Program
-------
Scott Specialty Gases
6141 rASl ONHOAD.ro BOX MO. I'lUMSl F.AOVIt IF. PA 18949-0310
(215) 766-8861 FAX (215) 766-0320
CERTIFICATE OF ANALYSIS: EPA PROTOCOL GAS
Citfflnturt
Optimal !«'< lmolitpjrs !n«
f»7r» W.llinm Pill Wn\
Piltslun,\K PA 152.1*
ANALYTICAL 1NFORMA HCN
A»wy l^boriloiy
S i>tt SfVtiully Ciiws, liw .
f»l4t Kiisldn Ri*n<.i
P.O. Box 310
PlMiiislfSMlvilln, I'A 18919-1)311)
I'luchase Order S32536
Scott Project * 01-74924-002
/lilt retltfu-alnm ti'rts /h i fin til il in cor,liny I,t } I'A itnfcitbtlill/ I'roltK'til I'fr A:Ci (.'<•»of Gfl.voiis Crtlilrrrttioil Slaiulartls;
I I'nirriliirr Srcliiitt Nmiitwr .VO.-l. Si[>l{ iiihtT.
Cylinder Nitinlx-i AI.M(H15:-1
Cylindci I'tpBHuro 21HI0 r :'(V'
(>rliiir»ltoii D'le: 01 -0.1% Expiration Date
I'lrvioufi Certification L)*lrc None
01-03-98
ANALYZEP VYMNUt-R
Components
Nitric Oxide
Total Oxiilti of .Nitrogen
Balance Gas: Nitrogen
Certified Concentration
24.9 pjnn
2S.t> ppnt
Analytical Uncertainty
±1% N1ST Traceable
Reference Value Only
~ IK» not ««.* tvltrn « yliml«-f in IfM lit m ISO plif,.
* At inly IK nl mw i-Mnlnly h imlg»ivr » I uf tlx* mfHitfttmcnt iHtKfWl^
REFERENCE SIANUARl
Type Expiration C ate
N'l'KM :>.<>?<>
VIW,
Cylinder Number
C1.M003365
Concentration
19.86 ppm NO in N?
INSTRUMENTATION
liiFtruiiicnt/MocteVSciial " Last Dale Calibrated Analytical Principle
NO: I lori!m/( I ,A2X)/S7CWW'i8l( 12-29-95 Chcnitliinunnscent
ANALYZER READING?' (Z°Zcr« Gjw R"»Refcr*i»c« Gm T"Test Um r-Corrgt.iHon Coefficient)
Components
Nh.KNVI-
Plrsl Tria l Analynis
|)nlr I ? ?t» '>5» I l«iMv V«Jh
7.\ »:
ft-3.02.VIKt 01
1>hinxmti+oo
A"9.*AI6K02
C-o.ooooti+oo
K-O.OOW1M 110
-------
Scott Specialty Gases
PHONE: (115) 76&-W&I FAX: (IIS) 7WB3D'
CERTIFICATE OF ANALYSIS: Interference-Free™ EPA Protocol Gas
Customer
Assay Laboratory
OPTIMAL TECHNOLOGIES INC
ScMtSpedaby Gmta,fnc.
Purchase Ordei 532512
575 WILLIAMPtTTWAYr "
6141 Zantrn Road
Scott Project# 7190504A -
PITTSBURGH. PA 15238
PtmmMMUt, PA 19949
«r * " •
if •
ANALYTICAL INFORMATION
Thlt nrrtflreiim mperformed metordktf to SPA TrocMbtittytS oimtiPcrAuay and Ctntflcaitan of Gas*om Cahbroitan Stmdardr. Prvcmfyrw G1; Stptmmbr, 199$.'
Cylinder Number . • ALM0400J4
Cylinder Pre»»urc+ 1910 pstg
ANALYZED CYLINDER
Components
Nitric Oxide
Total Oxides in Nitrogen
Nitrogen
Prerkms Certification Dates
Certified Concentration
98.2 ppm
98.2 ppm
Balance Gas
Certification Dale 9/25/95 V
Expiration Date 9/25/97.
Analytical Accnracv* :;y.\
± 1% Directly NIST Traceable'
Reference Valne Only
.it, .
* Do no! iu# wbm cylindtr prtourt Is below 130 ptig. i
* Analytical accuracy u inchuh* of iuual known erroraomrtmt which at Itatt inchidt prtevtan ofIht imasummdprocesses.
REFERENCE STANDARD -» ^ -
Type/Sample No. . : Expiration DateCytinderNamber
NTRMI684 .. -
'*6/7/97
AIM049084
Concentration
94.4 ppm NO in N2
INSTRUMENTATION
Instrtanent/ModeVSertai # ¦
Nicola FTIR/8220/AAB930Q174
; ' r '*• -
ANALYZER READINGS
LaatDateCaRbrated
9/7/95 :NO
Analytical Method
Scott Enhanced FTIR
.1
(frZwCiil MMtwaetCM WntCw r-CorrttdkwiOxffldatQ
Component*
/VW'
Flint Triad Aiminls
'niSjfijf': -itiif'ttM*"
n* Ait \jy,n* t?M .
n-MJt "*'*«-
*t£u"
it- ut
m- mm
a- *ji
A*g.
.V'.w «•<¦* -
JEL
' Sacwai Triai Aaafrils
It * *0T '
Kf MM
Ki-
ll- Alt
n» Mil
rut
Tt- M.U
T2- MM
*1» MJT
_fl2
LIADllDOttVTt
.. . i."».
*- o.trm
D- X4SX4T
AALmi . \
A• 1NM)
c* tm*4 J
¦ g» • .
; V
Special Notes:
Analy;
-------
19/96 05:22 ©215 766 2070
SCOTT SPECIALTY
003/003
Scott Specialty Gases
6141 EASTON ROAD. P.O. BOX ?I0, FtUMSTEADVIllE. PA 18949-0310 (215) 766-8061 FAX <21S) 7660320
CERTIFICATE OF ANALYSIS: EPA PROTOCOL GAS
Customer
Assay Laboratory
Optima! Technologies Inc
Scott SptvioUy Gnscn, !ih".
Purchase Order S325.16
575 William PHt Way
6141 Easton Road
Scott Project # 01-74924-001
PillsburRh, PA 15238
P.O. B4-96 Expiratiou Date 01-04-98
Previous Certification Dates Noik*
Certified Concentration
262 ppm
264 ppm
Analytical Uncertainty*
±1% NIST Traceable
Reference Value Only
~Do not me when cyUml*> Is let* ih.m 1SD p»lg.
'Analytical uncertainty K Iwchnlvf«f uwjal kmrwn tmmwinw whtrh at Include* pnftelon ot the wmuifinrnl [iiocmn
REFERENCE STANDARD
Type Expiration Eate
NTRM1685 07-10-97
Cylinder Number
ALM050886
Concentration
248 ppm NO in Nj
INSTRUMENTATION
Instxuxnen^ModeVSerial J>
NO: Horlba/CLA220/57088S)81('
Last Date Calibrated
12-29-95
Analytical Principle
Cheniiluniinescenl
ANALYZER READINGS 02462 Tl-0.2625
KZ-0.2469 7J-0.0000 T2-O36I0
ZMMXHO T3 "0.2611 R3-0.2473
A«(.Cmc irfCwlCyt 262ppm
Date: 01-04-96 Rcspnrar Units: Vote.
Zl<00000 R1-OJ0M TI-0.KS46
R2--OJI8S Z2-C.0005 T7-OJ6M
23-00000 T3-OJ660 10=0^092
Avg. Cchk. of Cuat Cyt 262 ppm
Concert Ira Uoo-A* 8**Cx2+Dx3+ Ex*
»-a99995
NTRM1685
Constants:
A-1.4SUK*00
B-J.0499E+02
C-O.OOOOE+OO
EX)i*»Of.»00
K-O.OOOOR»00
ft
-------
Air Produc*--- and Chemicals, Inc.
P.O. BOX 35X_
H.D. #1
IAMAQUA, PA 18252
ArrW 3"/l Wc
to.
Ah. LuJU^
Certificate of Analysis - EPA Protocol Gas Standard Page 1 of 1
i
PERFORMED ACCORDING TO EPA TRACEABILITY PR6tOCOL FOR ASSAY AND CERTIFICATION OF GASEOUS CALIBRATION STANDARDS (PROCEDURE #G1)
:ustomer: Order No: 148-013358-01
APCI- CP Batch No: 255-83657
CLYDE RORABAUGH Notes;
FREEPORT RD, ROUTE 26 N02-
-------
'• Xf - . -%-flflt!r-*
' \* - '
. ¦ ,"-'*A \
•"•¦ ""Isi
•W,
(215) ?S5^et *£AfeJ
' " P^%S^ "
*'.• £.575 WilHam:
. ^Pittsburgh, PA 15238
i k :a
^ANALYTICAL INFORMATION^^;
, >?*" . Purchase Order 713; J
-•j»'^"v / Scott Project # O1-759S2|0|
P.O. Box^l^^vr?'-;'r»:.-. %••<&»¦
Plmn8teadvdle) PA 18949^10 ,Vv
• •• ¦•:•¦¦¦^¦•#88s§& ^-:'r
v..,
>v
J
ton was performed
tyre #G1, Section Nui
Number; AAU482£)
JPiwsare 2000psi£fj
> CYLINDER
X toEPMT*
otAssmf &%Cer
. 02^'
Sk-Datfe?
Doneate ''-v.1; '
tmonoxide
LGac Nitrogen
Certified Concentration , a
- ,u4 :&k* • *-i .- ¦!»>$
doal
Certified Concentratioii ;a .^&g&fonalvtteal Once
- *»• ^smsix —- NlSTTttKeabteai
V£
.. .o -T«:r.• „%5\v.;/, r%-*sr-jac^s
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¦ CMtomer :: •
cornmLANALrric^-'-'i':
CJO OPTIMAL TEOtXOWQlES
S?S WILLIAMPITT WAf 1 '
PITTSBURGH. PA 15238 •'
ANALYTICAL INFORMATION
1894941310 PHONE: (215) 766-8861 FAX:fll5)HMf
?Attt#L»b6ratory .
Inc. -
414t£stitM Read
PA 18949
Thti tmtfifattm w pwfarmtd wanjltj to SPA fawatoyftatoBifjWjtoy W CmUfleirnan of Gaxou Otilbnmtm AnfWc O/; &jp/«»4ir?5
llCertifl cation Dates
..^CyMiider PmiBre+ \ferl855PSIG
'MANALYZED CYtlWPER . *§«»»
Carbon M
Nitrogen
Carbon Monoxide
Concentration
jJS !*?>-.
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* Analytical aeatraey U iniiiuMtfuaothvfrmtnortot&eu which aiieait tncludm pncbtan of ttm mtaammmt prodott. *'r*
REFERENCE STANDARD V *
! Type/Sample No. >rj^lExplration DateV- Qrilnder Number
NTRKH679 ' *
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Analyst
-------
Scott Specialty Gases, Inc.
1290 COMBERMERE STREET. TROY, Ml 48083
(810)589-2950 FAX :(810) 589-2134
CERTIFICATE OF ANALYSIS: EPA PROTOCOL GAS
Customer
CAE INSTRUMENT RENTAL.
246 WOODWORK LANE
PALATINE. IL 60067
Assay Laboratory
Scott Specialty Gases, bic
1290 Combermere •
Troy, MI 48083
Purchase Order: 13985-71500
Scott Project #: 585106
ANALYTICAL INFORMATION
This certification was performed according to EPA Traceability Protocol For Assay and Certification of Caseous
Calibration Standards: Procedure Gl; September. 1993.
^Cylinder Number : ALM031I86
. ' Cylinder Pressure + : 1900 psig
Certificate Date: 9/1/95
Previous Certificate Date: None
Expiration Date: 9/1/98
Y ANAI.V7.Rn CYLINDER
"Components
Carbon Monoxide
Certified Concentration
279-2 ppm
Balance Gas: Nitrogen
^•"i +Oo no! use when cylinder pressure is below 1 JO psig.
I?,'Analytical accuracy is inclusive of usual known error sources which at kaa include precision of the
Analytical Uncertainty*
±1% NIST Directly Traceable
Type
: ntrm i68i
Expiration Date
4/21/96
^instrumentation
Instrument/Model/Serial H
CO: Bcckman/864/102528
Cylinder Number
ALM-024826
Last Date Calibrated
8/10/95
Concentration
966.0 ppm Carbon Monoxide in Nitrogen
Analytical Principle
Non-Dispersive Infrared
ANALYZER READINGS (Z~Ztro Ga» R-Referaee Gas T-T«st Gaa r-Coirdaliou Coefficient)
Components
Carbon Monoxide
First Triad Analysis
Data: 8/75/95 Ratpon** Units: PPM
Z1=0.00 R1-100.00 T1-33 00
R2= 100.00 22*0.00 T2=33.00
Z3-000 T3-33 00 R3MOO.OO
Avg Cone, aI Cust Cyl 280 1 ppm
Second Triad Analysis
Dtfa: W1S95 Response Unta PPM
ZI*).
-------
Air Product* and Ch**ical«, Inc.
P.O. BOX 351
R.D. #1
TAMAQUA, PA 18252 W
Certificate of Analysis - EPA Protocol Gas Slindard " * 1 of 1
PERFORMED ACCORD DIG TO EPA TRACEABILITT PROTOCOL FOR ASSAY AND CERTIFICATION OF r.ASKQUS CAIIRRRTIOW STAMPARDS {PROCSKniE #C1)
¦ —order Ros 255-OS615»-ol
wUltOMf. ire
AIR PRODUCTS 6 CHEMICALS Batch Bo: - ,
«7XM ORRIS Hotel! . , ^_ u csiai liifAftiT
FREE PORT RD ROUT* 5R -^Cyliadw Hot SO»114474BAL
CRKIGHTON PA 15030
certification Data: 11/13/94
Expiration Data: 11/08/94
! iit-ai instrueeetation *•**••*»••••<
••• Certified Concentration *•» ~•»»»•••• Reference standards ~•**»*»*» *«»•»••••*
_ . " -t Serial Laat Measurement
Certified Standard Instrument
. » Number calibration prtncipii
Component Concentration Cylinder / Number Concentration Hake/Moofi 5775x052—10/14/94 GC-TlS
CARBOH MONOXIDE 594 ±1.47 PPM SC911353SBAL CMIS 507.2000 PPM Hewlett T4C!kar 2518 / /
balance Gas: Nitrogen
* Standard should not be used below ISO psig
D
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7)
n
n
i
lU^JuuJLk/tkAMM^ p Approved By: ,*¦
chael Wagner®"/ ' Eeo Roubik ' 1
nalyat:
-------
Scott Specialty Gases, Inc.
1290 COMBERMERE STREET, TROY, Ml 43083
(810) 589-2950 FAX:(810) 589-2134
CERTIFICATE OF ANALYSIS: EPA PROTOCOL GAS
Customer
CAE INSTRUMENT RENTAL
246 WOODWORK LANE
PALATINE, IL 60067
Assay Laboratory
Scott Specialty Gases, Inc
1290 Coiubdineie
Troy, MI 43083
Purchase Order: 15612-71500
Scott Project #: 501873
ANALYTICAL INFORMATION
This certification was performed according to EPA Tr»ceability Protocol For Assay and Certification of Gaseous
Calibration Standards; Procedure Gl; September, 1993.
Cylinder Number: ALM05I293
Cylinder Pressure + : 1900 psig
Certificate Date: 9/20/96
Previous Certificate Date: None
Expiration Date: 9/20/99
ANALYZED CYLINDER
Compongnta
Carbon Monoxide
Certified Concentration
1515 ppm
Analytical Uncertainty*
±1% NIST Directly Traceable
' Balance Gas: Nitrogen
/~Do not use when cylinder pressure is bdow 150 prig.
'Analytical accuracy is iwdimvc of mual known .00
72*112.70
R2>14&00
z>aoo
T2-11270
ConHMtt:
AMJ.188W4000
Z3=0.00
T3»112.70
Rl-145.00
ZJKL00
T3-112.70
R3-14&00
e-asrssseooo
c-aot«8ao6eo
Aa^ Coe el C*at Cyt 1515 ppm
A*a Cone, si Curt. CyMSISppm
DXLOOOS313S3
Muooaoooooo
Special Notes
Mail
[Thr^tvtrm
-------
n
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¦V61.41 EASTON ROAD, P.O. BOX 310, PLUMSTEADV1LLE, PA 189490310
(215)766-8861 FAX (215) 766-0320
"^CERTIFICATE OF ANALYSIS*. EPA PROTOCOL GAS
** i OprttaalTechnologies Ijk
f 575 William Pitt Way
Aeaay Laboratory
• •'-* '
¦ f ' .'*
**¦- ¦ <
¦ *
Inc.
6141 Eastoft-Road;
RO.BoxMO;^ ,
Plumsteadtfille, PA 18949-0310
Purchase Order 532512 *
Scott Project # 01-71905-001
••'.f, P*? s>.
ANALYTICAL information
ThiiBjitifiaitum was performed according to EPA TraceabSitif Protocol For Assay fir Certification of Caseous Calibration Standards;
1 PtSakure UG1, Section Number 3.0.4; Septetru~ 1oa*
Certification"Dale 10-05-95 Expiration Date
Previons Certification Dates None
ure UG1, Section Number 3.0.4; September, 3993.
Number ALM032640,;
Pressure 2000 psig+ „;/
V-'- •"5:
10-05-97
XYZED CYLINDER
menta " " ' *
r.\;
Gas.Nitrogen
• s'
v
¦" v'J. ': ^Certified Concentration
¦- / 24.4 ppm J6 * "tf" ¦
•y. - «¦'
' . j v»*
Analytical Uncertainty*^?*^'.'* M '/ %
±1% NISTl*aceaMeV3^ if'"'
" ' ¦¦
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. I7»i««ti^i 111 m . t"Val£L •«-* •
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11-15-97 > vCLM005278
•< •••
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Mq&VSetial # '^Lart Date Calibrated
¦ ¦ „ %¦ vlO-21^95 »vi\
FID ' , 1CV ¦'
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ANALYZER READINGS (Z-Saaffe^ i^ftiifii^^SasvTWfaa G« o'l-OHrcUtkm CocfHckmt)
.^¦" ••¦'- - . -V
>1' t .>- -- .
Dale 1IMK-95 \> Xe^ionM Unils; AmL1
Zt-SOOOOO TIV2M3M,
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-------
it. jpcticiny uascs, inc.
shipped 1290 COMBERMERE STREET
From: TROY MI 4 8083
Phone: 810-589-2950 Fax; 810-589-2134
CERTIFICATE OF ANALYSIS
CAE INSTRUMENT RENTAL PROJECT #: 05-94608-003
PO#: 14897-71500
24 6 WOODWORK LANE ITEM #: 05023451 2AL
DATE: 3/28/96
PALATINE IL 60067
CYLINDER #: ALM030236 ANALYTICAL ACCURACY: +/-1%
PILL PRESSURE: 2050PSIA
BLEND TYPE : ACUBLEND MASTER GAS
REQUESTED GAS ANALYSIS
COMPONENT CONC MOLES (MOLES)
PROPANE 85. PPM 85.89 PPM
NITROGEN BALANCE BALANCE
ACUBLEND MASTER GAS
d kPd- I ~bh>l
ANALYST : Au &'(2,
PLUMSTEAUVIII kf.NNyVLVANIA .• TROY MICHIGAN. HOUSTON TEXAS ' OURHAM NORTH CAJU.HINA
SOUTH PLAlNFirI D, NEW J6RS£V • FREMONT CALIFORNIA ' WAKEFIELD. MASSACHUSE1 '!> ' LONGMONT COLO'^VO
-------
Scott Specialty Gases
8141 EASTON ROAD, P.O. BOX 31Q.PLUMSTEADVILLE, PA iee49&)0 (215)7e&S861 FAX; {215)7850320
•bjj. • • .'4'.b ¦ '-LV1'
& ....
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CiRTIRCATE OF ANALYSIS: EPAPROTOfcOL GAS
** *¦>»* s*-" r„ <¦" J
:'ir;
Cttshnner ?
Optimal Technologies Inc
575 William Pitt Way
Pittsburgh, PA 15238
f
¦ .+•¦*
ANALYTICAL INFORMATION
Assay Laboiatdiy' •>
Scott Specially Gases, Inc
6141 Easton Road
P.O. Box 310
Plumsteadville, PA 18949-0310
iS
Purchase Order 532512
Scott Project # 01-171905-002
.
1 #GI, Serffcit
r Number. . ALM04584&..U:- r--' • . ,
t^anR. '2000!:#Iiwl^.OflMiTOiDifcti • '-None-'- "
Gas: Nitrogen
.... r" —
•:. " • :••• mm?
U 104)2-95 S Expiration
•_4,rSK 7o*.
Certified Concentration
not ok when cylind»t b len Own 150)^g.
nnoeminty ni
REFERENCE STANDARD
r; %: - Expiration Date
r ..
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^ANALYZER READINGS
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Z3-000000 T3^011fl^RS-wl
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OPTIMAL TECHNOLOGIES, INC.
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OPTIMAL TECHNOLOGIES, INC.
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OPTIMAL TECHNOLOGIES, INC.
SOURCE TESTING INSTRUMENT CALIBRATION RECORD
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OPTIMAL TECHNOLOGIES, INC.
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OPTIMAL TECHNOLOGIES, INC.
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OPTIMAL TECHNOLOGIES, INC. C 0
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OPTIMAL TECHNOLOGIES, INC.
SOURCE TESTING INSTRUMENT CALIBRATION RECORD
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OPTIMAL TECHNOLOGIES, INC.
SOURCE TESTING INSTRUMENT CALIBRATION RECORD
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SOURCE TESTING INSTRUMENT CALIBRATION RECORD
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Dimensions
M)A WMA
>n— *—
,»• -V*
(> < )
L - J
NOA-305A analyzer dimensions Unii mm
I
Jl. fl
V3 --
. {1 .
m
-i
: Specifications
licmilnniiiii'^t'iici?
Plinciple: Alum-pli<
Ml< -tl li '< I
Measuiituf tJHMjc iimi lutin/vou 1(1/
•>!,() Id '.(III III ppm ul NO. >>l lllill/llllI'VMl/MHI/
I <)()! I'." 111 | >1 >¦" W)»
Repcatabilily: I ili.m • 1% ul hill •;> .ilf
Zero iliift-I «•¦ •'. ilt.in 1 I i i ppni/ ' '»(
Span dtill: I •••;•; limn ' :»% nl lull •;>:.ilo ! • !i C
Linearity: HHlet lli.in ' nl lull r,t:;ilt>
Response: I <"•" lli.in I 11 m it lit ? loi ilt mi I lime phi': HtJ% ul
llllill JIMlllltil
Sampling rate: ^P/iuin
Recorder output:• • • IV lit; (Nui insiil.iicil)
(Standard Accessories
Description
Eloctrlcnl powor cable
Electrical signal cable
Converter cable
Fluoro-iubbcr tube
Fluoro-rubber tube
Sofl vinyl tube
Q'ly
1
1
1
1
2
— -
Remarks
Connects the main body
to the converter
Connects the ozone
deactivator
Connects the main body
to the converter
Exhausts the drain
NOj-NO converter dimensions Unit; mm
";Vy; -.'V'&i
Ambient conditions: •> ? / <
Power requirements. A( luny lluV, IHiV. I ^OV. 17/V.
Jl IV /Vlt IV. iii I 1 lu':,) ;t. .Mil<'i«:il •>(! 11/oi fiO 11/
Alioiil VA hi p'uvt'f ¦ « ii I- i implKin
Dimension*: and woiyht
Mnfi.W.fl "inil^""ly ii.'ii '.I Piitintti. I .'to kg
JO? NO r.ottvmUttT~Tr%^V'! ,'HI" IMlHmm 4 0 ki)
Sample Gas Conditions^
ii i i[i'IiImi1 —Cn 11 inn ppui Nl I t piim
(;()• H, won:. *;o. in ppm IM) If! wi%
r;o «.(it i ppm ni i inn ppm
c.-u.i. ih.c.ie Not < ..ui,ni..-.i
Noli- Hi' *;iih' i<» •.("» ilv il>>' lit«• vnli.it|i- mil lnn|n.
tOmm OD
Fluo»o-«ubiw II)
12mm OD
Soft vinyl tuhf. ?inin II).
iOnwn OD
l!»f?sc Hr*ttts »ro nv.iitoMc* n*
toq*ltlK?' with tlw ninln lio»Iy
Wl*m» ptacitMf m» okIci fm i
tllCH JKIll fMlllllMM'".
P/N
Q'ty
Remarks
01710424
i
SOOg
638 65232
1
300g
630-02514
1
1 box
630 02148
1
630 00705-02
1
200me
631 41200-04
1
1 m
631 41200-06
1
1m
630 00315-07
1
2m
a *<*1 rir»nn« mi otclnr lor tills it©!.
Mir.tttttitlioM jibfiiW1! k?l MS femiw
SH1MADZU
IIIIU1I cgtMMini MnHUMH aiiunf iMtm
1 M Hi'iMVrlwi I limn*- Oiifrall lin ll*|0 101 Mnw PIW* 811 llVH SMI I J. 8ll3U7»9 5'*>
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ol Smqapoie
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