USS CLAIRTON WORKS
CLAIRTON, PENNSYLVANIA
Report on
COMPLIANCE DEMONSTRATION
NO. 13, 14, 15 BATTERY
PUSHING EMISSIONS CONTROL
DECEMBER 1993
Prepared By: Chester Environmental
3000 Tech Center Drive
Monroeville, Pennsylvania 15146
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TABLE OF CONTENTS
Page
EXECUTIVE SUMMARY iii
1.0 INTRODUCTION 1
2.0 METHODOLOGIES 2
3.0 RESULTS 5
LIST OF TABLES
Table 1 Particulate Matter Emissions Data
Day 1: 10-19-93 7
Table 2 Particulate Matter Emissions Data
Day 2: 10-20-93 8
Table 3 Particulate Matter Emissions Data
Day 3: 10-21-93 9
Table 4 Particulate Matter Emissions Data
Summary of Days 1,2, and 3 10
Table 5 Visible Emissions Data Summary 11
APPENDICES
APPENDIX A TEST PROTOCOL, FIELD DATA SHEETS, CALIBRATION
RESULTS
APPENDIX B PLANT OPERATIONAL DATA
APPENDIX C GRAVIMETRIC AND ANALYTICAL RESULTS, EMISSIONS
CALCULATIONS
USS Gail-ton Works
300261-01 12/93
CHESTER
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EXECUTIVE SUMMARY
A demonstration of the pushing emissions control system for Batteries 13, 14, and 15
operated at USS Clairton Works was conducted on October 19, 20, and 21, 1993. The
purpose of the test program was to determine (1) the particulate matter emissions rate in
the exhaust of the baghouse, (2) the opacity of the plumes of the baghouse exhaust, (3) the
opacity of the plume which resulted from the pushing of the coke into the hot car, and (4)
the opacity of the plume which resulted from the travelling of the hot car to the quenching
station. Emissions testing was conducted only when coke was pushed from an oven in
Battery 13, 14, or 15.
The results of the testing showed an average particulate matter emissions rate of 0.46
pounds per hour, while the allowable emissions rate is 4.81 pounds per hour. The
maximum plume opacity observed from the baghouse stacks during the test program was 5
percent. Over the three day test program, 182 pushing events (each event includes a
pushing and travelling operation) were observed. A maximum plume opacity during the
pushing operation greater than or equal to 20 percent was observed 12 times. A maximum
plume opacity during the travelling operation greater than 10 percent was observed 12
times. Both opacities for the pushing event were greater than their specified reference
values 9 times.
USS Clairton Works
300261-01 12/93
-iii-
SO* CHESTER
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1.0 INTRODUCTION
As required by Paragraph V.A. (5)(f) of the amended Mon Valley Consent Decree, a
demonstration of the pushing emissions control system for Batteries 13, 14, and 15
operated at USS Clairton Works was conducted on October 19, 20, and 21, 1993. A
baghouse controls the emissions which result from the pushing operations from the ovens
of Batteries 13, 14, and 15. The purpose of the test program was to determine (1) the
particulate matter emissions rate in the exhaust of the baghouse, (2) the opacity of the
plumes of the baghouse exhaust, (3) the opacity of the plume which resulted from the
pushing of the coke into the hot car, and (4) the opacity of the plume which resulted from
the travelling of the hot car to the quenching station. Emissions testing was conducted only
when coke was pushed from an oven in Battery 13,14, or 15.
The field work activities were completed by Chester Environmental. All test procedures
were witnessed by a representative from the Allegheny County Health Department -
Division of Air Quality (DAQ).
USS Clairton Worts
300261-01 12/93
-1-
CHESTER
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2.0 METHODOLOGIES
A test protocol was prepared by Chester Environmental and submitted to DAQ prior to
the execution of the test program. A copy of the test protocol can be found in Appendix A.
Specific methodologies employed in the test program are outlined below.
The baghouse exhausts through four stacks; the emissions from each of these 36 inch
diameter stacks were sampled simultaneously. A total of three test runs were completed
on each of the four baghouse stacks with one series of tests completed on each of the three
days of testing. Testing was performed only during periods of normal plant operation.
Each traverse for each stack included 12 traverse points as calculated from EPA Method 1
(40 CFR 60 Appendix A). For each stack, sampling was conducted along a total of five
traverses, or 60 traverse points, with each push sampled for the required one minute at one
traverse point. Sampling was conducted on each stack through two sampling ports which
are separated by 90 degrees in the same horizontal plane. Three traverses were travelled
through one port, while the remaining two traverses were travelled through the other port.
In accordance with EPA Method 2, exhaust gas velocities and volumetric flow rates were
measured using a calibrated S type pitot tube. Positive and negative pitot lines were leak-
checked at the beginning and end of each test run. Gas velocity differential pressures along
with stack gas temperatures were recorded at each sampling point.
Gas concentrations of carbon dioxide (CO2), oxygen (O2), and nitrogen (N2, by difference)
were measured using Fyrite apparatus as specified by EPA Method 3. Gas concentrations
were used to obtain molecular weight of the process gas on a dry basis.
Percent moisture content, by volume, of the exhaust gas was measured from the weight
gain of the four sample train impingers in accordance with EPA Method 4.
Particulate matter sampling was performed in accordance with EPA Method 5, the
Amended Installation Permit for Nos. 13, 14, and 15 Batteries, and Sections 139.11 and
139.12 of the Pennsylvania Department of Environmental Resources (PA DER) Source
Testing Manual (Revision Number 1, January 1983) with the exception that the DER
USS Onirton Works
300261-01 12/93
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XtfL CHESTER
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requirement of sampling 50 cubic feet of exhaust gas was replaced with the requirement of
sampling the emissions from 60 pushes. The emissions from each push were sampled for
one minute. Thus, a total of 60 minutes of sampling was completed.
Clean up of the sampling trains included separate water and acetone rinses of both the
front-half and back-half components of the sample trains, as per Section 139.12 of the PA
DER particulate matter test method. The water soluble and water insoluble portions of
the front-half of the sampling train were determined as a total; that is, the water rinse was
not filtered to determine soluble and insoluble portions. Front-half acetone and water
rinses were evaporated to dryness, desiccated, and weighed to a constant weight. The
water soluble and water insoluble portions of the back-half were determined separately in
accordance with Section 139.12 of the PA DER Source Testing Manual. The back-half
water rinses and first three impinger solutions were combined and then filtered under
suction through a preweighed 0.22 micrometer membrane filter. The filter used to capture
the insoluble material was dried, desiccated, and weighed to a constant weight. After
filtration, the soluble back-half water was extracted with chloroform and ethyl ether. The
extracts were evaporated to dryness, desiccated, and weighed to a constant weight. The
filtrate, or remaining water from the extraction process, was then evaporated to dryness,
desiccated, and weighed to a constant weight. The filtrate extract was then be solubilized
with 100 raL distilled deionized water and submitted for sulfate analysis via ion
chromatography. Back-half acetone rinses were evaporated to dryness, desiccated, and
weighed to a constant weight. Sample train filters were desiccated for 24 hours, and
particulate matter weight was determined gravimetrically. Rinse residue weights and filter
weights were measured to the nearest 0.1 mg. One acetone blank and one deionized
distilled water blank were prepared in the same manner as the test sample rinses. The
blank residue weights were subtracted from the test sample residue weights. After blank
correction, front-half water and acetone rinse residue weights, sample train filter weights,
and back-half water insoluble filter weights were used to determine total particulate matter
catch.
All plume opacity measurements were performed in accordance with EPA Method 9 and
Section F of Chapter 18 of the DAQ Source Testing Manual. During the pushing
operation, the maximum plume opacity and length of time (in seconds) when the plume
opacity was greater than or equal to 20 percent were recorded. During the travelling
USS CUirton Worki
300261-01 12/93
-3-
CHESTER
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operation, the maximum plume opacity and length of time (in seconds) when the plume
opacity was greater than 10 percent were recorded. Visible emissions from the baghouse
stacks were recorded for one minute for each push in which emissions testing was
conducted.
USS daitton Wort*
300261-01 12/93
CHESTER
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3.0 RESULTS
The particulate matter emissions test results have been summarized in Tables 1 through 4.
The total particulate matter emissions rate for each day of testing was obtained by
summing the emissions rates from each stack. The three day average particulate matter
emissions rate is 2.79 pounds per hour of pushing (lb/hr pushing). Since emissions do not
occur continuously, the mass emission rate has to be adjusted for the number of pushes
which occurred during the testing periods. Since there were, on average, 9.85 pushes of
coke per hour, and each push was sampled for one minute, the actual emission rate (based
on a continuous operation) is equal to the following:
2.79 lb x 1 hr pushing x 1 min pushing x 9.85 pushes = 0.46 lb/hr
hr pushing 60 min pushing 1 push hr
The allowable particulate matter emissions rate is equal to the lowest allowable emission
rate standard (LAER) of 0.040 pounds per ton of coke pushed. Since there were on
average 12.20 tons of coke per oven, and on average 9.85 ovens were pushed per hour, the
particulate matter emissions rate is equal to (0.040 lbs / ton coke pushed) x (12.20 tons
coke pushed / oven) x (9.85 ovens pushed / hour), or 4.81 lb/hr. Thus, the average
particulate matter emissions rate determined in the test program is less than the allowable
emissions rate.
Tables 1 through 3 also list other pertinent stack and sampling parameters including the
exhaust gas flow rate in units of actual cubic feet per minute (acfm), standard cubic feet per
minute (scfm), and dry standard cubic feet per minute (dscfm), moisture content of the
exhaust gas, exhaust gas temperature, gas volume sampled for each test (dscf), and the
isokinetics value for each test. The isokinetics value is equal to the ratio of the average
linear gas velocity sampled through the probe nozzle to the average exhaust gas velocity.
An isokinetics value between 90 percent and 110 percent is considered acceptable. All
sample volumes were greater than 30 dscf per test. All isokinetics values were within the
acceptable range.
The plume opacity data has been summarized in Table 5. The maximum plume opacity
observed from the baghouse stacks during the test program was 5 percent. Over the three
day test program, 182 pushing events (each event includes a pushing and travelling
USSCIiirton Worta
300261-01 12/93
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CHESTER
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operation) were observed. A maximum plume opacity during the pushing operation
greater than or equal to 20 percent was observed 12 times. A maximum plume opacity
during the travelling operation greater than 10 percent was observed 12 times. Both
opacities for the pushing event were greater than their specified reference values 9 times.
A pushing performance or travel performance of 100 percent was registered if the
maximum plume opacity observed during the pushing or travelling operation was less than
20 percent or less than or equal to 10 percent, respectively, A pushing performance or
travel performance of 0 percent was registered if the maximum plume opacity was greater
than or equal to 20 percent or greater than 10 percent, respectively. The average pushing
performance for test program was 93.4 percent, while the average travel performance was
also 93.4 percent. During the pushing operation, the plume opacity was greater than or
equal to 20 percent for an average of 0.5 seconds. During the travelling operation, the
plume opacity was greater than 10 percent for an average of 0.8 seconds.
All testing was performed during periods of normal plant operation. Copies of the field
data sheets can be found in Appendix A Copies of the plant operational data for each day
of the test program for Batteries 13,14, and 15 can be found in Appendix B.
All sampling equipment was calibrated and operated in accordance with EPA Methods 1
through 5. Copies of the pre-test calibration results, post-test calibration results, and
results of an audit of the control boxes conducted with a critical orifice provided by DAQ
can be found in Appendix A.
The analytical results and emissions calculations for each test can be found in Appendix C.
USS ctairtoo Worti
300261-01 12/93
-6-
ACHESTER
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USS CLAIRTON WORKS
CLAIRTON, PA
TABLE 1
BATTERIES 13,14, AND 15
PUSHING EMISSIONS CONTROL SYSTEM
PARTICULATE MATTER EMISSIONS DATA
DAY 1
TEST DATE: 10-19-93
TEST TIME: 0905 TO 1520
Stack Number
2-1
2-2
2-3
2-4
Test Number
CLR-2-l-l
CLR-2-2-1
CLR-2-3-1
CLR-2-4-1
Miss Emission Rate
and Concentration
Particulate Matter
(lbAir pushing)
0.42
0.84
1.00
1.64
(gr/dscf)
0.0017
0.0036
0.0046
0.0078
Stack Conditions
Flow Rate
(acfm)
31900
31000
28700
27400
(scfin)
28700
27700
25900
25000
(dscftn)
28100
27200
25400
24500
Temperature
CF)
118
122
117
111
Moisture Content
<#)
2.0
1.9
2.0
1.9
Samolina Conditions
Sampling Time
(minutes)
60
60
60
60
Sample Volume
(dscf)
45.872
46.779
37.506
35.590
Isokinetics
(*)
97.fi
100.9
95.3
91.6
USS Clairtan Works
300261-0! 12/93
Xjfiu CHESTER
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USS CLAIRTON WORKS
CLAIRTON, PA
TABLE 2
BATTERIES 13, 1-4, AND 15
PUSHING EMISSIONS CONTROL SYSTEM
PARTICULATE MATTER EMISSIONS DATA
DAY 2
TEST DATE: 10-20-93
TEST TIME: 0810 TO 1413
Suck Number 2-1 2-2 2-3 2-4 Total
Teat Number CLR-2-1-2 CLR-2-2-2 CLR-2-3-2 CLR-2-4-2
Mass Emission Rate
and Concentration
Particulate Matter
(Ib/hr pushing)
0.31
0.48
0.66
0.65
(gr/dscf)
0.0013
0.0021
0.0030
0.0031
Stack Conditions
Flow Rate
(acftn)
31900
31100
28700
27400
(scfm)
28800
27700
25900
25100
(dscfm)
28100
27100
25300
24500
Temperature
(°F)
116
124
116
108
Moisture Content
(*)
2.4
2.3
2.3
2.3
Samolinfi Conditions
Sampling Time
(minutes)
60
60
60
60
Sample Volume
(dscf)
46.164
47.030
37.003
37.384
Isokinetics
(*)
98,3
101.9
94.3
96.2
USS CUirton Works
-8-
300261-01 12/93
Sfyu CHESTER
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USS CLAIRTON WORKS
CLAIRTOK, PA
TABLE 3
BATTERIES 13, 14, AND 15
PUSHING EMISSIONS CONTROL SYSTEM
PARTICULATE MATTER EMISSIONS DATA
DAY 3
TEST DATE: 10-21-93
TEST TIME: 0758 TO 1412
Stack Number 2-1 2-2 2-3 2-4 Total
Test Number CLR-2-1-3 CLR-2-2-3 CLR-2-3-3 CLR-2-4-3
Mass Emission Rate
and Concentration
Particulate Matter
(lb/hr pushing)
0.37
0.47
0.72
0-80
(gr/dscf)
0.0015
0.0021
0.0033
0.0044
Stack Conditions
Flow Rate
(acfrn)
32100
30700
28900
23900
(scfm)
28600
27100
25700
21600
(dscfro)
28000
26500
25100
21100
Temperature
(°F)
121
126
121
112
Moisture Content
(*)
2.2
2.2
2.3
2.2
Sampling Conditions
Sampling Time
(minutes)
60
60
60
60
Sample Volume
(dscf)
47.083
44.371
36.389
33.059
Isokinetics
(%)
100.7
98.1
93.5
98.8
USS CLaiiton World
-9-
300161-01 12/93
CHESTER
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USS CLARTON WORKS
CLAIRTON, PA
TABLE 4
BATTERIES 13, 14, AND 15
PUSHING EMISSIONS CONTROL SYSTEM
PARTICULATE MATTER EMISSIONS DATA
SUMMARY OF DAYS 1, 2, AND 3
Particulate
Matter
Emissions
Day Test Date (lb/hr pushing)
1 10-19-93 3.90
2 10-20-93 2.10
3 10-21-93 2.36
Average 2.79
USS Claiitoa Workj
10-
300261-01 12/93
MkU CHESTER
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USS CLA1KTON WORKS
CLAIRTON, PA
TABLES
13, 14, AND 15 BATTERY PUSHING EMISSIONS CONTROL
VISIBLE EMISSIONS DATA SUMMARY
Bughouse Sticks
Observation Number of Greatest
Date Observations Opacity (%)
10-19-93 1440 5
10-20-93 1344 0
10-21-93 1496 0
Pushing Operation
Number of Average
Observations Pushing Time with
Observation Number of with Opacity Performance Opacity
Date Observations >=20% (%) > 20% (sec)
10-19-93
10-20-93
10-21-93
60
60
62
95.0
91.7
93.5
0.3
0.9
0.3
Average
93.4
0.5
Travelling Operation
Number of Average
Observations Travelling Time with
Observation Number of with Opacity Performance Opacity
Date Observations >10% (%) >10% (sec)
10-19-93 60 5 91.7 0.6
10-20-93 60 5 91.7 1.5
10-21-93 62 2 96.8 0.4
Average 93.4 0.8
USS Cliifton Work*
-11-
Afc CHESTER
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COMPLIANCE DEMONSTRATION
NO. 13. 14, 15 BATTERY
PUSHING ^MISSIONS CONTROL
USS CLAIRTON WORKS
CLAIRTON, PENNSYLVANIA
APPENDIX A
TEST PROTOCOL, FIELD DATA SHEETS, CALIBRATION
-------
TEST PROTOCOL
COMPLIANCE DEMONSTRATION
NOS. 13, 14, 15 BATTERY PEC
USS CLAIRTON WORKS
CLAIRTON, PA
As required by the amended Mon Valley Consent Decree (Paragraph V.A.(5)(f))» a
compliance demonstration will be conducted on the baghouse which controls the pushing
emissions from Batteries 13, 14, and 15 operated at USS Clairton Works. The purposes of
this testing are to (1) determine the particulate matter emission rates and concentrations from
the exhaust stacks of the baghouse, (2) compare the measured particulate matter emissions rate
with the allowable particulate matter emissions rate, (3) determine the presence of visible
emissions from the baghouse stacks, and (4) measure the opacity of the plumes which result
from the pushing of the coke into the hot car and during the travelling of the hot car to the
quenching station. The three day test program will be performed during periods of normal
plant production and operation.
Particulate matter sampling will be performed in accordance with EPA Stationary Source
Sampling Methods 1 through 5, the Amended Installation Permit for Nos. 13, 14, and 15
Batteries, requirements set forth in Chapter 18, Section F of the Allegheny County Health
Department Bureau of Air Quality (BAQ) Source Testing Manual, and Sections 139.11 and
139.12 of the Pennsylvania Department of Environmental Resources (PA DER) Source Testing
Manual (Revision Number 1, January 1983) with the exception that the PA DER requirement
of 50 dry standard cubic feet sample volume of exhaust gas will be replaced with the
requirement of sampling the emissions from 60 pushes. The emissions from each push will be
sampled for 1 minute. Thus, a total of 60 minutes of sampling will be completed. A total of
three test runs (one test run per day) will be performed for each of the 4 stacks of the baghouse
with all stacks being tested simultaneously.
The baghouse exhausts through four individual stacks. All of the stacks measure 36 inches
internal diameter. Each diametral traverse for the stack will include 12 traverse points as
calculated by EPA Stationary Source Sampling Method I. Sampling will conducted along a
total of 5 traverses, or 60 traverse points, with each push sampled for the required 1 minute at
one traverse point. Sampling will be conducted through 2 sampling ports which are separated
USS Clairton Works W3
1
A6L CHESTER
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by 90 degrees in the same horizontal plane. Three traverses will be performed through one
port, while the remaining two traverses will be performed through the other port.
In accordance with EPA Method 2, velocities and volumetric flow rates of the exhaust gas will
be determined using a calibrated S type pitot tube. Positive and negative pitot lines will be
leak-checked at the beginning and end of each test run. Gas velocity differential pressures
along with stack gas temperatures will be recorded at each sampling point. Static pressure of
the exhaust gas stream will be measured with the same pitot tube.
During each test, gas concentrations of carbon dioxide (CO2), oxygen (O2), and nitrogen (N2,
by difference), will be determined with the use of a Bacharach "Fyrite" apparatus as specified
by EPA Method 3. Gas concentrations will be used to obtain molecular weight of the exhaust
gas on a dry basis.
Percent moisture content, by volume, of the exhaust gas will determined by measuring the
weight gain of the four sample train impingers in accordance with EPA Method 4.
As specified by EPA Method 5, each sample train will be assembled as required by the
method, leak-checked on site at the beginning and end of each test run, and operated such that
isokinetic conditions are maintained. Clean up of the sampling train will include a water rinse
followed by an acetone rinse of both the front-half and back-half components of the sample
train, as per Section 139.12 of the PA DER particulate matter test methods. The water soluble
and water insoluble portions of the front-half of the sampling train will be determined as a
total; that is, the water rinse will not be filtered to determine soluble and insoluble portions.
Front-half acetone and water rinses will be evaporated to dryness, desiccated, and weighed to a
constant weight. The water soluble and water insoluble portions of the back-half will be
determined separately in accordance with Section 139.12 of the PA DER Source Testing
Manual. The back-half water rinses and first three impinger solutions will be combined and
then filtered under suction through a preweighed 0.22 micrometer membrane filter. The filter
used to capture the insoluble material will be dried, desiccated, and weighed to a constant
weight. After filtration, the soluble back-half water will be extracted with chloroform and
ethyl ether. The extracts will be evaporated to dryness, desiccated, and weighed to a constant
weight. The filtrate, or remaining water from the extraction process, will then evaporated to
dryness, desiccated, and weighed to a constant weight. The filtrate extract will then be
USS CUiitoD Workj 9/93
2
Afo CHESTER
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solubilized with 100 mL distilled deionized water and submitted for sulfate analysis via ion
chromatography. Back-half acetone rinses will be evaporated to dryness, desiccated, and
weighed to a constant weight. Sample train filters will be desiccated for 24 hours, and
particulate matter weight will be determined gravimetrically. Rinse residue weights and filter
weights will be measured to the nearest 0.1 mg. One acetone blank and one deionized distilled
water blank will be prepared in the same manner as the test sample rinses. The blank residue
weights will be subtracted from the test sample residue weights. After blank correction, front-
half water and acetone rinse residue weights, sample train filter weights, and back-half water
insoluble filter weights will be used to determine total particulate matter catch.
All visible emissions determinations from the baghouse exhausts stacks will be performed in
accordance with EPA Stationary Source Sampling Method 9 and BAQ Method 18F. Visible
emissions will be recorded for the duration of each of the sixty oven pushes. All plume
opacity measurements will also be performed in accordance with EPA Method 9 and BAQ
Method 18F. During the pushing operation, the maximum plume opacity and length of time
(in seconds) when the plume opacity is greater than or equal to 20 percent will be recorded.
During the travelling operation, the maximum plume opacity and length of time (in seconds)
when the plume opacity is greater than 10 percent will be recorded.
A report summarizing the compliance test program will be submitted within 60 days following
completion of the field work. The report will describe test methodologies utilized and present
a textual and tabular summary of the emissions results and related sampling information.
Copies of operational data will be included in the report to verify that all testing was
performed during periods of normal plant operation. Also incorporated into the report will be
copies of the pre-test calibration results, post-test calibration results, the results of an audit
conducted with a critical orifice provided by the BAQ, field data sheets for the particulate
matter sampling and visible emissions determinations, emissions calculation sheets, and
analytical results for each test.
USS Clairtoo Works 9/93
3
/& CHESTER
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STACK SAMPLING DATA SHEET
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(incliea)
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Meter Reading
(del)
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(in. 1120)
Orifice a II
Meter Temperature
Vacuum
(in. lit)
Stack
Temp.
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Probe
Temp.
(•F) *-
tmpmfcr
Temp.
CF)
Hot Do>
Temp.
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CornmeaU
Required
(in. 1120)
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(in. 1120)
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(•F)
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CF)
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.B' £>
fr7
<32.T~H b'
i,4
l,(o3
4/
(tfCj
3 o
//?
LM
i<>
i.ift
L>!
•P..Q
VJ
7.*-
h-Vl
U/
3-0
//?
,
«?.y
.~4VV- 2-U>
1. o
{.It*
L?3-
6?^-
O
// V
/, o
.<34, <1 /1
1 • 1
I.Z-&
/¦ 20
(e 4
kW
3v O
W
v5"J?.<,S24
\
>
/
I,*7V
) (
_j!
3"! 6 ,
1 lt»3
)
Estimates:
v.
MW- 2B, &
%H20« J_
Impinjer
No.
Impinger
Contents
Final
Initwi
Difference
1.
(0CW- ^i.A/6
R.&
2.
|O0*«L #i.O
^3J.&
.537,-7
3.
Gufhi
¦i(39
*¦?
4.
(^S(r-0
7?
i.
«.
7.
1.
SYSTEM LEAK CHECK
After
Vacuum
(in. If j)
j*'LQwA
DGM R«te
(cfni)
Positive
Ncgalsve
Before
aL
A Her
cp *C
oM—
OA5
C02
t
02
ao->"
t\, i
; /fjk CHESTER
CO
\a
N2
7?o"
-------
CLIENT^ UJW.K5
TEST UNIT B-/t
$7T\CJC- 2-[
STACK SAMPLING DATA SHGET p.6<^ of ¥<£
TEST DATE /&- ft- ?3 ORIFICE CORRECTION ( a. 11®) j 6 7 3 HOT/COLD BOX NO. 8
TEST NO.
PROJECT NO. JC02A/-0
TEST CREW
CL&.-2.-| - f
NOZZLE (SIZE,#) o lAO'
STATIC PRESSURE e? < ft "X O
METER CORRECTION (Y) o
PROBE NO. s~ - ^
CALIBRATION DATE FILTER NO. //
Meter Reading
(Ocl)
Pilot iP
(in. II20)
Orifice All
Meter Temperature
Vecoum
(in. Hg>
SUek
Temp.
CD
Probe
Temp.
CF)
Impinjer
Temp.
(*F)
Hot Box
Temp.
CF)
CornmenLi
Required
(in. 1120)
Actual
(in. >120)
In
CF)
Out
CF)
)c O
if
/'/
/.Z.&
//s
/v2$""b
<6i5
-w-So
_i_ min./point
iM
^ i
1, <
l.zv
!.
U<
3.0
H.i
/' o
),/L>
/ / //^
U> Ci?
*3 < &
m
c-Y
i< 2-
i MO
i .HD
L>7
(pL0
s.-r
\t9>
?cO
S3£i.\"?
3'<*
hi
nfr
2.7- O
1-7
I9f>
kp>
loQ
3<$
tit
2?. C
l<7
htft
tj'O
ur>
7'. 7
ST41.29-3.
J., i
aWs1
i*e>
H'D
U2>
I
n 4>
S~Y3> ioT-
2C\
4o
}<3
V
i
i.S-iO
i
W)
t
'
-------
Ckujtkn Ucv(<5
TEST UNIT 13 -/5- fc-ifeW
PROJECT NO. q7/
STACK SAMPLING DATA SHEET P«ge3 of 5"
TEST DATE (o - f?-?J ORIFICE CORRECTION (A HQ) HOT/COLD BOX NO. 5*
Tec. TEST NO.
METER CORRECTION (Y) o . 2- PROBE NO. _s~—*/
NOZZLE (SIZE,#) O' IW1
CTlTir* DOCCCIIDD 1 A" ri
CALIBRATION DATE 5'-l^jrr3 FILTER NO. /{07
TEST CREW
PITOT CORRECTION O-i
STACK DIA.
BAROMETRIC PRESSURE
PORT DIRECTION
CONTROL BOX NO. V
PORT SIZE
Trweiw
Time
Dry On
Pilot *P
Orifice * II
Melet Temperature
Vacuum
Slack
Probe
Impmger
Hot Box
Comraenta
Point
(inches)
Meier Reading
(<1<0
(in. I120)
Requited
(in. I[20)
Actual
(in. 1120)
In
(*P)
Out
<•!=)
(in. U|)
Temp.
<*F)
Temp.
(*F)
Temp.
(*F)
Temp.
(•F)
lb. O
. 2, I
1.<0
-b-Zo
n \
O
4-D
11 L?
&
-?/
t? 9'
V'£?
//£
2 %L
fT47,boi
1,1
3..2.(o
Z.-2-C>
7/
~?o
V-/0
//£>
2.7.0
i.n
2-oi-
2- >0 1~
1 /
lo
-5>/T
M*
2-7. 2-
¦ bf
hi?}
7/
7 /
3 €
//&
IJ--S
^o-io3
l<£"
ioe
\n¥?
K
-7 O
lit?
9.o
<£>«£bc>
113
\-&
—>2
7 3-
3 ^
>?-o
~L~
/'V3
b¥3
73
120
^ V
£)£3>.o"VZ
I O
i.W
73
7 3
3 .£7
If®
/.<=>
I ¦ 0
111 °t
Wl^
7 V
73,
-O
111
S&.X'A 1
*
<¦ V
I
rf^9;
)
> (
1 l£j.3
>
Estimates:
J
v_
~
MW- Z.g/8
SI 120-X
SYSTEM
LEAK CHECK
PITOT LEAK CHECK
1 infringer
Impingcr
Vacuum
DOM Rale
Positive
Negative
No.
ConleaU
Final
Initial
Difference
{in. Ilg)
(cfm)
Before
1.
Before
After
2.
After
OAS
\
2
3.
C02
4.
02
5.
<2*
CO
«.
CHESTER
N2
7.
ENVIIKINMCNIM
».
-------
CLIENT USS CJcla^\ bJoJ^
TEST UNIT 13 - 7?
PROJECT NO. ggj2X/ c,/
Z-Y
STACK SAMPLING DATA SHEET
TEST DATE fO-ft-fS ORIFICE CORRECTION ( a H@) /, 673
TEST NO. f
NOZZLE (SIZE,#) O. I <\ o"
STATIC PRESSURE {¦ O
METER CORRECTION (Y) O .WZ-
CALIBRATION DATE S
Page of -5""
HOT/COLD BOX NO. 8
PROBE NO. .ST--/
FILTER NO. //O?
TEST CREW
PITOT CORRECTION
o -iW
*7
STACK DIA. 36
PORT DIRECTION SowrV\
CONTROL BOX NO.
PORT SIZE y ¦/
TwfilK
Point
(inchei)
Time
Dry On
Mclcr Reacting
(dcf>
Pilot aP
(in. H20)
OriflCO All
Meier Temperature
Vacuum
C»."«)
Slack
Temp.
<*F)
Probe
Temp.
(•F)
Impttf(er
Temp.
(#F)
Hot Box
Temp.
<*F)
Comment*
Required
(ill. 1120)
Actual
(in. 1120)
In
¦("Is)
Out
CF)
3£©
CZA M
n H
13
M'D
izo
ji- rain./point
*3 C ,
554>vl,o
z, I
3-SO
7*v
n 2.
f
31. 7
1' 0
lift
-73
H-d
v23
2U
{.
2.. tZ
-2-.il-
7V
7V
^, 6
I 2-3
7 J. 2-
1. if
l.^
7-y
3,r
fl.g
|ii
/.k£l
/<6
7V"
3,
l^
/.°
5-6.3.^0-?-
I'M
1
-71
lift
\
/ >»
(
L(*33-
) <
l.q3>
6
7V^
) <¦
12-1 ¦?>
)
Estimates:
MW= 8
*H20-
SVSTEM LEAK CHECK
PITOT LEAK CHECK
linpinger Irnplnger
Vac 111 itn
(<«• »*)
DOM Rate
(cf'»)
Poiilrra
Ncgitive
No. Contents Find Initial Difference
Bcfoce
I.
Before
After
2.
Aflcr
OAS 1 2
3.
C02
4.
Xjjfc CHESTER
ENVVlflNMCNlAL
02
5.
CO
6.
N2
7.
t.
-------
S77KX-
STACK. SAMPLING DATA SHEET P»g. S~of jT
CLIENT LfeS Cla HOT/COLD BOX NO. g
TEST UNIT 13 - H Ic-ftcy 7eX- TEST NO. Ct-f-2-t-l METER CORRECTION (Y) O.ffyZ PROBE NO. if
PROJECT NO. 3lx2&t-OJ ' NOZZLE (SIZE,#) o, iq 0 P1TOT CORRECTION 0.&? STACK DIA. %77
BAROMETRIC PRESSURE 3if.j'C PORT DIRECTION wr A CONTROL BOX NO. PORT SIZE Y"
Traverse
Poirt
(inclKt)
Thu«
Diy Gil
Mclct KeaiJin^
(del)
Pilot aP
(in. IIZO)
Orifice A H
Meier T«npcr«ture
Vacuum
(in. Ilg)
Stack
Temp.
(•F)
Piofee
Temp.
(*F)
Impingcr
Temp.
CF>
Hot Box
Temp.
(•F)
Coitimcnd
Required
(in. 1120}
Actual
(in. 1120)
tn
(*F)
Out
(*F>
(.0
s63/=W0
1,3
f '^3
f-O
n9>
7 6?
3 ^
/; 7
-2-5D
<"6^
min. /point
ifiW.l 11
''-f
i.*G
h-7ft
7#
~7Ce
//ff
*/• 3
\n$
}
79>
n
3 O
//7
1'^
\.19>
7«
~?(o
//7
n,o3C>
\.->€>
78
110
5"6 7,#2.5"
' 'W
)*(*(?
!- C?(&
7g
~7(i>
3/
/,
77
"75"
u&
i-7. o
Sic/}. ^"2-4
1-1
¦%'OV
¦%'OT^
77
7 if
V/W
•vt
4-o
3/.?
SlUXft
%>\
"L,fO
"7S>
7>V
*4-o
//.<>
V
,
$72.0
T-.l^
iao
~L<1d
"7C?
7o
^ (
. w.
//8°
?-
ci4 ,
) <
r
) <
-)
Esiiniales:
tfJki
—(
1'%
MW« -X&. 8
Lb
*H20- jt
SYSTEM LEAK CHECK
PITOT LEAK CHECK
1 mpingcr linpfager
Vacimm
(in. Ilt)
DOM Rule
(cfrn)
Positive
Negative
No. Content! Final Initial Difference
Before
I.
Before
After
2.
A Her
~ AS 1 2
3.
COl
«.
CHESTER
ENVimjNMfNfAt
02
J.
CO
6.
HI
7.
1.
-------
same. 2.-2_
CLIENT k1£ Oou^kA IMtofe
TEST UNIT |vVxt^UTg-
PROJECT NO. ?eoa/-o 7f
STACK SAMPLING DATA SHEET P.ge / of jT
TEST DATE >-d- ORinCE CORRECTION (t H&)/, S~ ? 2- HOT/COLD BOX NO.
TEST NO. CcJ—Z-Z.-7
METER CORRECTION (Y) / g/sr(
PROBE NO. S~ - ?
FILTER NO. ///7
STACK DIA. 7k
NOZZLE (SIZE.f) 0, /
CALIBRATION DATE J
P1T0T CORRECTION o"^/
TEST CREW
STATIC PRESSURE
Traver ic
Point
(iltclics)
Time
Dry Ou
Meter Reading
(del)
Pilot 4 P
(in. H20)
Orifice aH
Meter Tcmpermlure
Vacuum
(in. Hg)
Stack
Temp.
<*F)
Probe
Temp.
CF)
Irapinger
Temp.
CF)
Hot Bo*
Terap.
CF)
Comments
Required
(in. 1120)
Actual
(in. H20)
In
(•F)
Out
<*F)
?T,o
3^7. 34T
L 7
2.IG
2- lb
H
21. Z
36L10I
bfr\
3 AO
!i bl
2./6>
la
H,9
h°
a. 8
3(£. ISV
{,<¦
/,£(
iH
HiT
12&
9,tp
36 3. CO/
j. 4
hUl,
/l 1
m
£
H,0
t9.o
ZLZ.^OCj
1,2
tAQ
13$
lC?
60
~
/-o
JGL.o'M
0. KO
1 %
X, S3
/oo
~3CC. I2t>
(
) I'U
)
72,17
a.s
(
lH,93
-
>V.
V
J
Estimates:
<
(ol ^
\
MW- ZB. 2>
*H20= rL
SYSTEM LEAK CHECK
Vacuum
(in. Hg)
DOM Rate
(cfra)
Before >
Wt
- OO?
After
CfliO—
-vr!
Poaitive
Negative
Before
& PC.
After
o K
0 IC
Impinge!
Mo.
Impinge*
Contentj
Find
Initial
Difference
GAS
CHESTER
tNVinONMENfAL
C02
02
O-o^i
t
CO
— r
>
NZ
^¦-3
1.
~&vX. M,c
KHZ. 1
2.
'-/sirs
3 .H
3.
H(o2n
\.o
~.
Zl.d'&eSL
%A
5.
¦ J
6.
¦iii!
-
7.
r
8.
V
! RfV
-------
CLIENT USS CJlaiiw iJznjtf
TEST UNIT /7-/f
PROJECT NO. 50O2h/-£r
T£C
577kJC~ Z.-^
STACK SAMPLING DATA SHEET P.gc ?_ of 5~
TEST DATE /P-/7-73 ORIFICE CORRECTION ( a H@) /¦ *- HOT/COLD BOX NO, £
TEST NO. C^-Z.-2T^|
METER CORRECTION (Y) PROBE NO. f-3
NOZZLE (SIZE,#) O,
'^q "ti—
o.30JLo
CALIBRATION DATE
2l1zH
D.fiV
FILTER NO. ,Ul
TEST CREW
BAROMETRIC PRESSURE 2*1
STATIC PRESSURE
PITOT CORRECTION
STACK DIA. 36
PORT DIRECTION
CONTROL BOX NO.
PORT SIZE
! i!
in
Time
Dry Gtu
Meter Reading
(dcf)
Phd a P
(in. H20)
Orifice iH
Meter Temperature
Vacuum
fid. Hg)
Suck
Temp.
CF)
Probe
Temp.
CF)
(rapinger
Temp.
CF)
Hot Box
Temp.
CF)
CommeoU
Required
{in. H20r
Actual
(in. 1120)
Jo
(•F)
Out
(*F)
f.o
3U.12&
??£>
.?£
-11
1 K
65?
?.n
/0£>
~ z5b
3, O
1° &
V?
301.1L 1
/, 1 £>
/. JO.
1. 3A
to
70
3,S~
~(oV
/..V
3(Sn.LlS
/.JO
/.
HO
!,(oO
/<
io
y,o
IZb
/'.7- *
311.
f,Ln
hi
t,
-------
CLIENT OSJ CLaM^ MtrrJS.
TEST UNIT [J-IS
PROJECT NO.3asz(?!-»/
S77KX 2.-2—
STACK SAMPLING DATA SHEET PigcJ of £~
TEST DATE /0-l?-*?5 ORIFICE CORRECTION (aH@) t.S^Z- HOT/COLD BOX NO. £
if
METER CORRECTION (Y)~7TbtS'i PROBE NO.
TEST NO. ClZ - 2,-i.
NOZZLE (SIZE,#) 6,/q 2/ ,
STATIC PRESSUREp , O
7fjEp
CALIBRATION DATE
PITOT CORRECTION
FILTER NO. ~{IT
STACK PI A -3£ Y
TEST CREW
T raverae
Point
(inches)
Time
Dry Gas
Mdtr Reading
(dcO
Pitct iP
(in. H20)
Orifice a H
Meter Temperature
Vacuum
(in. Hg>
Stick
Temp.
CF)
Probe
Temp.
(•F)
Impinger
Tcnp.
(•F)
Hot Box
Temp.
CF)
ComnmU
Required
L (in. H20)
Actual
(in. H20)
In
fF)
Out
(*F)
3T.0
3-iC.W)
0.7,1
s-V
-7 a
Z&1
3.C*
13
h;
73.^
as. 1
1.6**.
(A 7
i f?&
«o
Estimates:
mw«
-------
CLIENT pa Oculist
i>i Ldb*.\
STACK 2--Z-
STACK SAMPLING DATA SHEET *
TEST DATE /0-/9-?3 ORIFICE CORRECTION ( t. H®) A5?2_ HOTVCOLD BOX NO, £,
Page V of S
TEST UNIT U-yg"
PROJECT NO" Z/ScV
TEST CREW
TEST NO. CJ-fi--—¦(
METER CORRECTION (Y) /. o/S < PROBE NO. 5--3
NOZZLE (SIZE,#) Ot fA c,
STATIC PRESSURE
CALIBRATION DATE
0.&4
FILTER NO. Htt
rt.qO-
PITOT CORRECTION
STACK DIA.
Traverse
Point
(inches)
Time
Dry Gst
Meter Reading
(*0
Pile* IP
(in. H20)
Orifioc aH
Meter Temperature
Vocuum
(in. Hg)
Stack
Temp.
CF)
Probe
Temp.
(*F)
Impingcr
Temp.
CF)
Hot Box
Temp.
CF)
Comments
Required
(in. H20)
Actual
(in. 1120)
In
(•F)
Out
(*F)
7H
y,jr
~25Z>
£>
^25Z>
-i min./point
ryu
3ZL. UJ-Pv
/,?r
2,?-0
W
74
y.,r
izL
»
31.7
3&-7. 313
/rlT
2.X.L
2.^1.
SrA
76
/<3k
tf.L
•3frSr.;w/Sr
LlO
X21
£.2,1
fa
i?o
/, %o
2 JO
ZIO
76
v,. 1
/, 30
!,sr\
7*"
^ A
i?n
9. 0 . ,
W
3<=t / , (. 3 S
7.
/, S~f
f,rt
£r%-
7^
3,
/.CO
sri
£r /
12?
396r. frZj
b?, p.
n.£>
I3fS
/W 7
Uno)
(s
)
Estimates:
MW- 29. ^
SH20-
SYSTEM LEAK CHECK
P1TOT LEAK CHECK
Vacuum
(in. Hg)
DGM Rute
(cfni)
Before
After
Positive
Negative
Before
After
Impinger
No.
Impingcr
Contents
OAS
-------
CLIENT tl&Jckrf t&nM*
t-of
TEST UNIT \Z-ti ^.-jbu/TeC- TEST NO. 2,^-T
<.77K-£- Z-—"2-
STACK SAMPLING DATA SHEET
\
TEST DATE /u-/"? -13 ORIFICE CORRECTION (aH@V,
MY
P»ge ,^~of -3T
HOT/COLD BOX NO.
METER CORRECTION (Y) /. cyj
PROBE NO. y-.?
PROJECT NO. 3ooi(J -of
NOZZLE (SIZE,#) a
•f?3, ,
. °>Q %.0
CALIBRATION DATE 7"J
FITOT CORRECTION p/8?
FILTER NO. /Hi
STACK DIA.3C, ^
TEST CREW
STATIC PRESSURE
Tnveiie
Point
(mcbea)
Time
Dry G*»
Meter Reading
la
CF)
Out
(•F)
f.O
f.OO
i,i3
uB
w
* - /
IX3
¦—25c>
ji min./point
¦?<"/
a^S^ASr
I. OO
/, /sr
!,}<*
fr?
Sri
"•?. '/
1X3
V-3
I.30
iff**-
h $"X-
fe^
*1
vj'
' z^r"
fcV
397, 3^
tH0
l,(,1
/ >m
r/
fcle
U.&
huo
/. ir^r
/t tirk~
*-*
S7
H. I
/2-C?
t%Z-
a??, 73
I.St
%H20- J-
SYSTEM LEAK CHECK
Vacuum
{in. Hg)
DOM Rate
(cfm)
Before
£.6
:oo9
After
CHESTER
CNVinONMENTAL
PITOT LEAX CHECK /5~
Positive
Negative
Before
After
&{rJ-
-------
>73c*- 2. -3
STACK SAMPLING DATA SHEET
CLIENT (X; t/MfS
TEST UNIT b-IS ^
PROJECT NO. ^wlLt-Otf
Page / of 5"
TEST DATE lb-
TEST NO. cd./i - 2-3-/
NOZZLE (SIZE,*) Cy/g3*~
ORIFICE CORRECTION ( a H@) A *>/ HOT/COLD BOX NO-
METE R CORRECTION {Y)Q-7d>~
PROBE NO. 5"- I
FILTER NO. I/Q^
CALIBRATION DATE 3--/ ?-
TEST CREW
BAROMETRIC PRESSURE Z.9. Vi~
STATIC PRESSURE /.o'j/.Q
PITOT CORRECTION
STACK DIA. 3^ 7
PORT SIZE ?rr~
PORT DIRECTION
CONTROL BOX NO.
T raverec
point
(inches)
Time
Dry Gil
Meier Reading
(
?>
_i- min./point
l&.ozz
/.
/•
/ bG
63
Z-.S"
//3
31.7
#7. Kb
I-Kn
<•?<=>
To
3. 0
//A
/?.(.
1 ?
i-7-G
1. 7fe>
~H
<^r
3. G
"8
Xl-0
w
/V6
/Vfc
77
(o^r
z. c
7.12.
hi
/ 3f-
t.3?
?-/
&&
2. O
//?
ji-8
K«O.Z?o
l.z-
7/
^.O
y/ff
1L\. /C/D
(. J,
f.V*
t,z7-
6>
2.. C>
//£
t,V
76/.0I3
J.2-
f.z-T-
fr?
z.o
«8
43
(¦ 2-
t.^7-
r-5
6P,
2-.0
ut
0^0
l.o
1. oG
f. 0b
7>/
G0
I. &
loj
/-o
on
0.93'
V
TO
2. 2
io&
Estimates:
MW« <2_B. g
%H20= J-
SYSTEM LEAK CHECK
Vicuum
(in. Hg)
DOM Rite
(cfm)
Beforc
T O
After
~f.o
O.O to
PITOT LEAK CHECK /5~£rc-
V,
CHESTER
ENVIRONMENTAL
Positive
Negative
Before
O^
O/i
After
GAS I 2
C02
O
02
20,£~
CO
O
N2
.7757.
[mpinger
No.
Impinger
Content!
Fiul
Initial
Difference
1.
/- /to
¥(>7.7
7.?
2.
IOW. ^OT,
.535,3
y.
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TEST DATE /0 -ft-*?3 ORIFICE CORRECTION < & H<&) / fo/ HOT/COLD BOX NO. 2-
TtX, TEST NO. Cc£ - 2,-3-f
~T. „
METER CORRECTION (Y) Q.TO32,
CALIBRATION DATE 5^/7-f 3
TEST UNIT /7- /g~ gr
c-tfc~y
PROBE NO. 5--
FILTER NO. //Q 7-
X
PROJECT NO. jQOa^Ao/
NOZZLE (SIZE,#) £>,
STATIC PRESSURE /. o "U^iD
TEST CREW
P1T0T CORRECTION o.
STACK DIA. 3C "
Traverse
Point
(inchet)
Time
Dry Gm*
Meter Reading
(*0
Pitot *P
{ia. H20)
Orifice iH
Meter Temperature
Vacuum
(in. Hg)
Suck
Temp.
(#F)
Probe
Temp.
CF)
Impiager
Tecnp.
CF)
Hot Bo*
Terap.
CF)
Comment*
Required
(in. H20)
Actual
(in. H20)
In
CF)
Out
CF)
1 O
0.0
o.eV
ro.&T
76
?o
/,iT
/o
7^
2.0
///
Y.3
^5'
1. 0
/. ok
/ o6>
72.
r^-
Z-C>
/A5
L,i
/./
1,1?"
7^
7^
2.0
/2o
9-o
U*Mf\
/./
<7
7^
7f
2. C
/'?
(2.2
1L1. Ooo
1.3
1.31
/.3S
74?
7/
-2.5"
//?
i-3.2-
:?„7< c^T-
13
A7
*H20- -f
SYSTEM LEAK CHECK PITOT LEAK CHECK
GAS
CHESTER
ENV1HUNMEKTAL
Before
Positive
C02
CO
02
N2
Before
After
Vacuum
(in. Hg)
Jmpingcr Irmpioger
No. Con tent i Filial Initial Difference
1.
2.
3.
4.
S.
6.
7.
1
-------
2-J
STACK SAMPLING DATA SHEET
CLIENT OSS UfoJCS
TEST UNIT \j-fa#**, 7FC
PROJECT N0.3co
TEST CREW
TEST DATE /(>- /
AS'
/. G/
/, «,/
¦so
3- 0
//8
^7-0
-?rt
/.v
/£/
AS?
<3/
75-
2. S
1/8
»2-
msk?
/.3
aV
-?.S~
\2-t
^3
1.3
/Vo
/.Vo
78
}Zxi
??8.^
0 ft
ofif
0-??-
So
77-
/'8
/.»
0 B
o, %
**s
7t>
/, g
//6>
Estimates:
MW=2g. 8
*H20= jL
SYSTEM
LEAK CHECK
P1T0T LEAK CHECK
Impinger
Impinger
V acuum
DOM Rite
Positive
Negative
No.
Contents
Final
Initial
Dirr«c*icc
(in. Ilg)
(cfra)
Before
1.
Before
A Her
2.
After
OAS
I
2
3.
C02
~.
02
S.
CO
s.
CHESTER
N2
7.
ENVIRONMENTAL
8.
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TEST UNIT (?- /5" U ^ PSST.
PROJECTNO. 3gst.it-eft
TEST DATE /o-
TEST NO.
(, Yt>
£r
(Z^
<4>8
/-¦2.5b
_i rain./point
«. t
Tdo.SVl
f.'S
t 6/
'¦
3, cj
(zsz.
31.7
7&L2Slo
(.<
/.(J
r.<>/
3. O
Z2-2-
27-C
i.i
l.bl
/&(
8(
7?
^.8
/^C
27- o
T8L.UH-
iS
(¦U
(.(=,(
S2-
3.o
/zz.
2-1 £.
783, ^
t< 3
Llf\f
13
(cfm)
Before
I.
Before
After
2.
After
CAS
1
2
3.
C02
4.
02
5.
CO
6.
CHESTER
N2
7.
ENVmONMENIAL
!.
-------
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STACK SAMPLING DATA SHEET P.gc of «j"~
CLIENT 5 Ctuxriy TEST DATE /O-ff- J J ORIFICE CORRECTION ( A HOT/COLD BOX NO. 2-
TEST UNIT \3- 7T rcc. TEST NO. 2.-3-/ METER CORRECTION (Y) O.PROBE NO. S~ -1
PROJECT NO. JaJiO/" o4 NOZZLE (SIZE,#) /ft}' CALIBRATION DATE FILTER NO. f/olh
TEST CREW STATIC PRESSURE ho" ll o PITOT CORRECTION o. >44 STACK DIA. 70 ^
BAROMETRIC PRESSURE 27.^-5" PORT DIRECTION ^ CONTROL BOX NO. 5 PORT SIZE */" ~
Traverae
Point
(inches)
Time
Dry Gu
Meter Reading
(
Probe
Temp,
CP)
Impinger
Temp.
CF)
Hot Box
T«nip.
(*F)
Comment!
Required
(in. H20)
Actual
(in. H20)
In
<*F)
Owt
(Is)
to
^?o 7.£?/2-
M-
Wh
Az&
8/
z.z-
H7-
— 2-iTO
_i min./point
2-i
700.228
/. *-
/. 2-8
eV
&(
£.£-
H. 3
7ys.86<
/.2S
/.20
&y
8c
Z-. T-
H5-
(.4
7&7&c2>
U7
83
8«
21. 2.
/'&
%o
7?a |2&
f'l
/./¦?-
/./^
tiV
a. 2-
l*-l
IZ-Ji
m?37-
(. >
UH
/.o?
81
2- O
tn
?3. 2-
7H.32S5
(.3
/.37
/• 3^7
7-?
7k
J.o
It 2-
3'. -7
/.<•
\,1z-
t.yz.
J- 5"
//3
33.,t>
79V. //7
A 5"
I. b/
/. fc»/
7<°
7. o
//3
7N. P//o
Z' -
f.7*-
I.7Z-
76
J o
1/3
7pf~
ftpL-
-/Wo
, -
^"117
rfcf
i?
Estimates:
WdAi
A3
mw= ze. 8
._
*H20-
SYSTEM LEAK CHECK
PITOT LEAK CHECK
Irapinger lmping«r
Vacuum
(in. Hg)
DOMRitc
(cfra)
Positive
Negative
No. ContuiU Fiiul InilUI -Difference
Before
1.
Before
After
1.
!
After
GAS 1 2
3,
C02
4.
Zjfifc CHESTER
ENVinUNMENIAL
02
5.
CO
6.
N2
7.
».
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TEST UNIT (5-i€ fckuxj
PROJECT NO. l - &g_
STACK SAMPLING
TEST DATE 10-t*?-^3
DATA SHEET
ORIFICE CORRECTION ( a H@) /¦ 802-
Page / of 5^
HOT/COLD BOX NO. V
rir<
METER CORRECTION (Y)
?.&
//t?
2^- L
/• 7
> *it,
/¦?L*
1/
7 r>
//Z
i7.r>
/v?.
/-3
t-7 /
/.?/
?e^
no
^ o
//£>
21.i-
/•O/
/-rv7
/•-3?
7/
-7tk
3-0
ii- a
/
75s
no
V o
no
/•!>9
3
%~o
it
jfo
///
/-ty> ?f7.f
1
-
Estimates:
I
MW= 2-g.. 8
JGH20- J_
.
Vacuum
-------
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CLIENT (J>S (JCuJckA UhjJ&
TEST UNIT l?- /r /SrflW FSC-
PROJECT NO. /-
Hot Box
Temp.
CFJ
Con menu
Requited
(in. H20)
Actual
(in. H20)
In
(*F)
Out
(*F>
ni hf
/- /
1
/'
7»
,rr.<
//O
A^2^t>
.yo
Fo
75;
J-J
///
JOo ¦ #7$
ill
**
7V
A.O
/fO
Z9.U
/.y
V
7/
/..Jf
// O
31.7
\H
t.uj
1-1,1
fa
7o
//^\
(6t AJf
t'C>
/.r?
/.f7
r?-
?/
7 r
il'h
35".o
1013.30
hi*
/•*«
K'o
7y
7-^
/Of
Estimates:
MW=Z-«.g
%H20=
SYSTEM LEAK CHECK
PITOT LEAK CHECK
lrapingtr Impinger
Vacuum
(in. Jig)
DOM Rale
(cfm)
Poiitive
Negative
No. Contend Final Initial Difference
Before
I.
Before
Alter
2.
After
GAS 1 2
3.
C02
4.
CHESTER
ENVI HON MENTAL
02
S.
CO
6.
N2
7.
8.
-------
CLIENT USf'Ciu^tl Ujcn-^y
TEST UNIT |3wr fc-dfccy f€C~
PROIECT NO. 3COiZt -Of
Jnfak- 2 V
STACK SAMPLING DATA SHEET
TEST DATE /tw?-?J ORIFICE CORRECTION ( a H@)/,&C>2-
TEST NO.
Page 3 of^~
HOT/COLD BOX NO-jjf Y"
PROBE NO. 5--5
g, FILTER NO. //g b
METER CORRECTION (Y)
NOZZLE (SlZE.iT)
CALIBRATION DATE
&E
STACK DIA. 3C y
TEST CREW
STATIC PRESSURE
PITOT CORRECTION o
Tfaverae
Point
(inchca)
Tirae
Dry Gu
Meter Reading
(dcO
Pilot iP
(in. H20)
Orifice A H
Meter T emperato re
Vacuum
(in. Hg)
Stack
Temp.
CF)
Probe
Tamp.
(•p)
¦mpiagcr
Tenip.
(*F>
Hot Box
Temp.
CF)
Conmenta
Required
(in. H20)
Actual
(in. H20)
In
CF)
Out
CF)
/.£
rTf
t.rf
7 f
XQ
'W5b
>
no
>.-?o
Si
n K
r.o
J
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f-t#
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gr
Zo
70
/ft
2?, t-i
-itfi
f.-x
/¦Y3v
I.H'X
xr
STc
/. .0
/'£
H.c>
J6?. «v
t.iC
t. if
rst
v. a
//^
f.o
170. Si I
f.C
it£
ITS'
s.&
I/O
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TEST UNIT 13- /5"
TEST DATE /o~
TEST NO. gi-2-Vw
STACK SAMPLING DATA SHEET
ORIFICE CORRECTION ( a H@) /, BOZ-
P»gc of
HOT/COLD BOX NO, zz
METER CORRECTION (Y) O 3b'7 PROBE NO. 5~'S"
CALIBRATION DATE FILTER NO. //pj-j,
PROJECT NO. 3007.f, I —at
NOZZLE (SIZE,D Q, / ftS
STATIC PRESSURE j PITOT CORRECTION oT&7
TEST CREW
STACK PI A.
Traverse
Point
(inches)
Time
Dry Oma
Meter Reading
(
AO
//S
2?-L
/. 3.
(<4c
/ Vo
fo
/*. ~*f
//V
i?.o
i.3,
t.HC
/¦vn
yo
6
«¥
2-7, 2-
yjf.o(*c
/¦/
/ 3 f
/.3&
Jfo
£ O
//S
12. S
nf. 7 Id
/.n(,
J.C3&?
ro
x.o
ft-/
9.o
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o.r'J
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b-i
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r>T
<3.9/
&&¦/
n
v-sT
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J/
/¦ n
• /f
//
* /
h 5>
/, O
m. Yd/
wf
Mir
irf
f/
' 1
///
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Estimates:
MW= &
*H20- ^
SYSTEM LEAK CHECK
PITOT LEAK CHECK
Vacuum
(in- Hg)
DGM Rate
(cfra)
Befoic
After
Positive
Negative
Before
After
Impinger
No.
Impingcr
Content ¦
GAS
CHESTER
ENVIRON MENTAL
C02
02
CO
N2
Find
Initial
Difference
1.
2.
3.
4.
S.
6.
7.
S.
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STACK SAMPLING DATA SHEET Page 6~ of £~
TEST DATE /o ORIFICE CORRECTION ( a HQ) /. &Q2- HOT/COLD BOX NO. ^
METER CORRECTION (Y)
CALIBRATION DATE fTVg|gSF"
TEST UNIT )7-/T
PROiECT NQ.3flp^<:/ -Q)
TEST NO.
NOZZLE (SIZE.*) o -
PROBE NO. S--T
FILTER NO. //6 B
V,Q PITOT CORRECTION Q.&f
TEST CREW
STATIC PRESSURE
BAROMETRIC PRESSURE PORT DIRECTION
STACK D1A. "
CONTROL BOX NO.
PORT SIZE Y"
Traverse
Point
(incites)
Time
Dry Gtt
Meter Reading
(del)
Pitot A P
(in. H20)
Orifice tH
Meter Temperature
Vacuum
(in. Hg)
Suck
Temp.
CF)
Probe
Temp.
CF)
Irnpinger
Tcn^i.
CF)
Hot Box
TepfP-
' (-F)
Comment*
Required
(in. H20)
Actual
(in. H20)
In
CP)
Out
CF)
{> O
*'?
/.#6
/o(„
/?
if 3.
jf.o
//£»
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nlu-rK
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l.lf
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no
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nitto
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f- .r
t-if
ff
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f.(tS
if
77
/f.r)
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f, - 8o°
ie* 1,r
P
~Bhk-4~
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Estimates:
1.2-
MW- 20. B
*H20= JL
SYSTEM LEAK CHECK
PITOT LEAK CHECK
Impinges Impinge*
Vacuum
(in. Hg)
DGM Rate
(cfm)
Positive
Negative
No. Contend Final Initial Difference
Before
i.
Before
After
2.
After
OAS 1 2
3.
CO!
4.
MlU CHESTER
ENVHIONMENTAL
02
5.
CO
6.
N2
7.
J.
-------
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A 15
B 16
A 17
B 18
A19
B 20
A.21
B 22
A 23
B 24
A 25
B 26
A 27
B28
A29
B 30
A 31
A 1
B 2
3
B 4
A 5
B 5
A 7
B 8
A 9
B 10
A 11
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A 13
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A 15
7.14 IX
713 3.S
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B 16 /13_
A 17 /15_
B 18 /13_
A 19 /15_
B 20 /13
A 21 /15~
B 22 /13__
A 23 /1S_
B 24 /13
A 25 /15~
B 26 /13_
A 27 /15~
B 28 713
A 29 /15
B30 713~
A 31 /15_
A,2./14_
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A 4 /14_
B 4 yi5__
A 6 /14_
B 6 /15_
A 8 /14_
B 8 /15_
A 10 /14
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A12 714
B12 /15
B 26 /1S_
A 28 /14_
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A 30 714~
B 30 /15
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A 12 /13_
B 11 /14_
A14 713
B 13 /14_
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B 14/15 •
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B 18 /15
A 20 /14
B 20 n 5 .
A 22 /14
B 22 /15
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A 26 /13_
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A 28/13
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A 30:713
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B 13 713~
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B 7 715 - 33-
A 9 /14. 3&
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A13 714 frg>/
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B 29/14
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B 15 /15
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A 25 714 67
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A 17 /15
B 1 /14
A 18 /15
A 3 /13 •*!
B 18 /13
A 4 /13
B 19 /13
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A 19 /15
B 3 /14
A 20 /15
A 5 /13
B 20 /13
A 6 /13
B 21 /13
B 6/14 5W
A 21 /15
B 5 114
A 22/15
n
A 7 /13 SS
B 22 /13
A 8 /13
B 23 /13
B 8 /14 1JL,
A 23 /15
B 7 /14
A 24 /15
•A 9 tr»^
B 24 /13
A 10 /13
B 25 /13
B 10 /14 ^7
A 25 /15
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a 26 ns
A 11 /13
B 26 /13
A 12 /13
B 27 /13
B 12 /14 H
A 27 /15
B 11 /14
A28 f\5 .
A 13 /13 Wo
B 28 /13
A 14 /13
B 29/13
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A 29 /1S
B13 /14
A 30 /15
A 15 /13 V*
B 30 /13
A 16 /13
A 1 /14
B 16 /14 «<3
A 31 /15
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B 1 /15
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A,2 /14
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B 18 /14 A 20 /13
A 5 /14 X
B 20 /14 */ 7
B 4 /15
l'B '19 /14
B 5 /15 g
A21 /13 y-e
A 6 /14
$A22 /13
A 7 /14 y
'"S"
B 22 /14
A 27 /13 TV
A 12 /14
A28/13
A13 /14 &
b 28 /14 yr
B 12 /15
B 27/14
B 13 /15 It
A29 /13 rc
. A14 /14 ' • >¦
. A 30 713
A 15 /14
i"
F
B30 /14 s~?
B 14 /15
B 29 /14
B 15 /15 fl
A 31 /13 .9*
A16 /14
B 1 /13
A 17 /14 (f
A 1 /15 $*}
B 16 /1S
. A 2 /15
B 17 /15 /5
B 2 /13
A 18 /14 ¦
B 3 /13
A 19 714 /t
A 3 /15
B 18 /15
A 4 /15
819 715 n
B 4 /13
A 20 /14
B 5 /13
A 21 /14 /a.
/
A 5 /15
B 20 /15
A 6 /15
8 21 715
B 6 /13
A 22/14
B 7 /13
A 23 /14 ue
A 7 /15
B 22/15
A 8 /15
8 23 715 ?Lf
. ja B 8 /13
A 24 /14
B 9 /13
A 25 /14 i-V
W A 9 /15
B 24 /15
aio ns
B 25 /15 x3
B 10 /13
A 26 /14
B 11 /13
A 27 /14
A 11 /15
B 26 /15
A 12 /15
B 27 715 X<
B 12 /13
A 28 /14
B 13 /13
A 29 /14 Jt
A 13 /15
B 28 /15 „
A 14 /15
A 31 !\4 It
B 14 /13
A 30 /14
B 15 /13
B 79 /IS
A 15 /15 .
B 30 /15
A 16 /15
-------
CLIENT U$5 C
STACK SAMPLING DATA SHEET P«ge / of
TEST PATE l(^70xflS ORIFICE CORRECTION ( a H®) hi, 73 HOT/COLD BOX NO. ft
PROBE NO. 5"—4
FILTER NO. i llO
STACK DIA. % '
TEST UNIT R."
PROJECT NO. "^xj2fa l-
O
TEST NO. Cl£-2.-I-2~
NOZZLE (SIZE,#) O, l ^ O'
STATIC PRESSURE /. Q% Q~
METER CORRECTION (Y) ort?'?-
CALIBRATION DATE <-- /?- ? 3
PITOT CORRECTION q/bV
TEST CREW
CONTROL BOX NO. ^
BAROMETRIC PRESSURE 2-^, Lf0 PORT DIRECTION .SoM.-r W
PORT SIZE
Tr«ver»c
Point
(inckei)
Time
Dry Gat
Meier Reading
(dc<)
Pilot h P
(in. H20)
Orifice A H
Meter Temperature
Vacuum
(in. H*)
Slack
Temp.
<*F)
Probe
Temp.
(*F)
Inipinger
Terap.
C*F)
Hot Box
Temp.
(*F)
Com menta
Requited
(in. H20)
Actual
(in. H20)
Id
(•F)
Out
(•F)
3f-0
t?
nv Llt>
a. O
^..37
wj.
6^
u€
—25D
<£&
^zSb
_i min./point
1
?-<
}/i>
31?"
£7t>, tMit,
-2-<0
-2.. 3 7
£-37
S"
T^.Lp
£77, 3»
1-1,
a.© i
I
fo-5.
*/'©
/
-
12,^
s-79. &3V
i
l«if?
, | .7#
\tvl
#< 5""
ltl9>
£>-*>
I/O.
-
6./
SVi. 4/?>
1
i.o<^
/j? c>
l/<
V,3
gdZ.hZ
A 7©
(o~?
fc>5"
4't>
w
i-L*
/¦&<"
lo (&
3'<
//3
L *
£>&3. ho2-
1,1
l.3o
(•Jo
(o~7
.i.n
//3
/
1/ 6^5^
¦ J
)
/
1»4-a
;
Estimates:
L
MW=Zg B
»H20=i
SYSTEM LEAK CHECK
PITOT LEAK CHECK /5^
Impinger Impbigcr
nee
Vacuum
(in- Hg)
DGM Rate
(cfm)
Positive
Negative
No. Conlenti Final loitiil Diffcrc
Before
fR
® K
].
CtLatC' O
4S?,fr
SfbA
J3.3
>
Before
r~
>c>e>3-
After
eyf*-
2.
tCty^L t>jC ftn
Sl6»l
oX
GAS 1 2
3.
Mi.?.
C02
+.
£,43."'?
«.0
SfyA CHESTER
EWlRCWMfNTAL
02
1o><
K f*-
5.
CO
r
6.
-fsW. -
7-3.c?
-------
CLIENT kXS Cl
STACK SAMPLING DATA SHEET P.ge 2, of <=?
TEST DATE ORIFICE CORRECTION ( a H®) |,(g-?2> HOT/COLD BOX NO.
TEST UNIT |3 -if feifcy tFX- TEST NO. C-ul- 2 2.
a
NOZZLE (SIZE,#) p. t <\"qT
METER CORRECTION (Y) g>,q<)<2- PROBE NO. 6~~V
O-'rW
PROJECT NO3OQUit
CALIBRATION DATE
FILTER NO. 11 1 O
TEST CREW
STATIC PRESSURE
PITOT CORRECTION
STACK DIA. 3C y
Trivene
?OMt
(¦BChtf)
Time
Dry Gu
Meier Reading
(def)
Pitot iP
(in. H20)
Orifice aH
Meter Temperature
Vacuum
(m- Hg)
Suck
Tenp.
(*F)
Probe
Temp.
CF)
Impcnger
Temp.
(*F)
HotBot
Temp.
(*F)
Comments
Required
(in. H20)
Actuil
(in. H20)
In
CP)
Chit
(•F)
f. o
£&t.23Pi
| ¦ 3-
i MX
H2-
•2>-Q
i < "2-
¦
—
•£. min./point
^.
. ~?l
~?o
_ x
3- >
/f£
491
i'i
J'OS
A9
3^ 5"
//&
&?.9*> 7
1
J.
7/
-7 £>
//4>
27. i
>
-1 - p
\n9)
J' 7g>
7,2
-?o
//lo
2-7 o
'
a-D i
3- o \
->,a
11
ftf
27 b
^lo.ZSL
2-o
2 v?
2-3^7
*10
v-r
."1
?».*
r2.0
,2.3-7
£>•37
"7^
A no
.iH
•3- 1
*72-
no
.it 3
s<\b. 035
.^,r>
52.37
^•3"7
-7.X
no
v->
//V
},ull
c
1-^cO
t
) <
Estimates:
MW= Z?& . £
%H20- 1
SYSTEM LEAK CHECK
PITOT LEAK CHECK
Vacuum
(in. Hg)
DOM Rale
(cfm)
Before
After
Positive
Negative
Before
After
GAS I 2
CHESTER
EMV
-------
CLIENT UZS C Uulhn LcW^i
STTkJC. Z--(
STACK SAMPLING DATA SHEET
TEST DATE ( 0-2.0-73
ORIFICE CORRECTION ( a H<&) \,h~]2>
Page 3 of S
HOT/COLD BOX NO.
METER CORRECTION (Y) aPROBE NO.
TEST UNIT
13 Siikt* F-ge,-
PROJECTNO. '
TEST NO. CUZ~ i-t-Z-
NOZZLE (SIZE,#) 0,1^0
STATIC PRESSURE I . O
CALIBRATION DATE
-33
q-SY
FILTER NO. t
¦W-
TEST CREW
PITOT CORRECTION
STACK DIA. 3,
T raver*
Fotirt
(inchcft)
Tirn«
Dry Gas
Meter Reading
(
3-32
•7^2-
"?£>
//3
~vlST>
\>c\o
1
17-
"7 £>
V-o
//<"
<2-8
^99o¥o
/ w
\.L<
!•/,<
T3.
"I <£>
3^
//2>
%o
SW.l*7
l w
i.L<
)»kS
11-
-? i
!?
/'*"
(.M
' w
I'L,^
!<(*,*
nir
no
/ lr>
<-°\ 0
\,c\o
ii,
n o
nS~4
75L
lo
Z..O
//^
/. o
)
'ln.&
) ^
|l 3-3
>
Estimates:
MW=2-0, 8
>
*H20= rL
SYSTEM LEAK CHECK
PITOT LEAK CHECK
Vacuum
(in. Hg)
DOM Pate
(cfm)
Before
After
Poiitive
Negative
Before
After
Impinger
No.
Impinger
CoDtenU
GAS
CHESTER
tNVinONMENTAL
C02
02
CO
N2
Final
loitiftl
Difference
1.
2.
3.
A.
5.
6.
7.
S.
-------
S7tej<- 2.-/
STACK SAMPLING DATA SHEET
CLIENT Qfj CkuMvrl U&vte
TEST UNIT 13-/5' Sttiduf ft*.
PROJECT NO. 30C54/-0//
TEST CREW
TEST DATE tO-Lu -?J
ORIFICE CORRECTION ( a H@) I
METER CORRECTION (Y) p iz_ PROBE NO.
P«ge yot
HOT/COLD BOX NO. P)
TEST NO. CL{Z~2--/-j
NOZZLE (SIZE,#) O.I^O"
STATIC PRESSURE \ ¦
CALIBRATION DATE
pTW
¦ ». FILTER NO. Q ,n IP
PfTOT CORRECTION
STACK D1A. "
T ravtrw
Poult
(incites)
Time
Dry On
Meter Reeding
(del)
Pitot «P
(in. H20)
Orifice A H
Meter Temperature
Vftcwtm
(in. Hg)
S^cic
Temp,
(*F)
Probe
Temp.
(*F>
I raping* r
Temp.
rn
Hot Box
Temp.
(*F)
CoraraenU
Required
(in. H20)
Actual
(in. H20)
In
(*F>
Out
<*F)
7£~. O
c>3.<4k 1
... ^
a
10-
-7 0
M-S
1 11<
— 2.S.D
.i rain./point
33. L>
6*/..% 2
• oi -O
1
1 n.1
13-
-7 c>
1.H
a.Stf
73>
72-
im
2?-0
/„£>£»-&/
-?(*
3-o
1 z /
6,/
/ffioo^/3
1.-2-
H3
1 -43
m
3 0
1^
f.3
isionrt
1.2-
i.43
\M3
72
3< O
/l^
Coll .^00
f. 1
J,3 t
\^i
70
77
3.0
JZ-0
/,o
.
6 '5-o ~7 "3
/, £>
>,(9
h/9
"7 g.
76.
0
//£
kta.*733
S
<
\.l&>
)
C1
1
(j4»3
)
)
Estimates:
v_
MW= zff, 8
A
*H20«=_£
SYSTEM LEAK CHECK P1TOT LEAK CHECK
Before
Alter
C02
CO
02
N2
Before
After
Vacuo m
('"¦ Hg)
DOM Rile
(cfm)
Impingcr Impinger
No. Content* Final Initial Difference
1.
2.
J.
4.
5,
6.
7.
9.
-------
CLIENT
test unit a-ik fctk**
— ,-61
2.-/
STACK SAMPLING DATA SHEET P.ge .^Tof 5~
THST DATE /o- T.Q-13 ORIFICE CORRECTION ( a H®) |. (g>7 3 HOT/COLD BOX NO. gg
TEST NO. £UJ£-2W-Z_
NOZZLE (SIZE,#) O. i <\ f)
STATIC PRESSURE \ . P*Z
METER CORRECTION (Y) o, q i X- PROBE NO.
PROJECT NO. 3>qpz£/-
CAL1BRATION DATE ^r,- v &, - s 3 FILTER NO. mo
TEST CREW
P1TOT CORRECTION
STACK DIA. 3g
77-
Trimie
Point
(inches)
Time
Dry Gu
Meter Reading
Pitt* A P
(in. K20)
Orifice &H
Meter Temperature
Vacuum
(in. H|>
Steele
Temp.
<*F)
Probe
Temp.
(*F)
Impinger
Temp.
TO
Hot Box
Tenp.
(*F)
Commeaijt
Required
. 1,0
I'fl
"77
r3 -o
~-2SO
/V'ZJfZ?
JL mm./point
*Y
ia\3.
M
1.3(
I <3 |
7?
77
3- O
Y->
G>/*/'Ootf
!. 1—
1-W3
I.
H'<
l£~U
31.?
/¦&
5a4
75"
73
V-jT
12/
33. L
&
£0
? 3?"
7-3^
7^
)ZO
KO
a.o
5-37
7<
73
ill
L>.?2. 1 I 4
A'foV
:
MW=1?. 9
%H20«J_
SYSTEM LEAK CHECK
PITOT LEAK CHECK
Vacuum
(in. Hg)
DGM Rale
(c/m)
Bcfoic
After
Poiitive
Negative
Before
After
Impinger
No.
Impingcr
Content*
Final
Initial
Difference
GAS
CHESTER
ENVIRONMENTAL
C02
02
CO
N2
1.
2.
3.
4.
S.
6.
7.
8.
-------
CLIENT UfS CJouXiuy
TEST UNIT \3~lf
crl
&wu.y V&
v*
yrfejc- z--~z— ;
STACK SAMPLING DATA SHEEi^.^,; J Page I of 5~~
TEST DATE /o-uiiJ ORIFICE COIufcctlON ( AHH
Meter Temperature
Vacuum
Cm- Hg)
Suck
Temp.
CF)
Probe
Temp.
C°F)
Intpinger
Teoip.
CF)
Hal Box
Temp.
CF)
Cofflmenu
Required
(in. H20)
Actud
(in. H20)
In
CF)
Out
(*F)
3f,o
HoSllMS-
X°
Q.XL
2,Z>
Ti
lo
57 O
/^5~
o
2,c*
1H
L S"
CO.
/a 3
mo. C2^
trio
/,(.!
IrU
76>
H/^>
/A3
£ftO
¦ A*?
' I, HO
/Ml
!,k 1
76>
<-/, y
)Xi
6,y
&
/ ,(&(&
It
12-
V.3
Hf 2,1ft 3
t,HO
/s
CHESTER
ENVM«JNMtNIAL
Positive
Negative
Before
<3 l«C
CJ /<
After
C>[\
OAS 1 Z
C02
O
02
CO
o
Ni
Impiager
No.
Impinger
Contenti
Final
laitial
DiiTerence
1.
(CO^n^ n
f?>
4.
6,bo,0
j.'oS/±2^
R.R
S.
6.
-Mi-
Zl.lq
7.
}
8.
u
r
-------
f>7^
TEST NO. Z-
"NOZZLE (SIZE,#) O.
METER CORRECTION (Y) l,&/(T/ PROBE NO. iT-3
CALIBRATION DATE
STATIC PRESSURE /, Q« 4/ X) PITOT CORRECTION
1-^3 FILTER NO.//o y
STACK DIA. 3i>
TEST CREW
TuvetK
Point
(inches)
Time
Dry Gm
Meier Reading
(dcO
Pto* * P
(in. H20)
Orifice t H
Meter Temperature
Vacuum
(in. Hg)
Stack
Temp.
CF)
Probe
Temp.
(*F)
Imptnger
Tamp.
CF)
HotBot
Temp.
CF)
Comment!
Required
(in. H20)
Actual
(in. H20)
In
CF)
Out
CF)
{.V
tf / i~. do/
,?r
I.IO
/,/o
7 Sr
72-
z.o
~lsto
i- min./point
i'V
>4tb.
hoO
/,n*
/> /C?
Ko
7 H-
3, A
;?-3
43
1/L 30
f.as-
•
to
7^
7-^
/53
o-V
/,
X2.
7 v
.57 <9
¦ IZH
2J.2,
yt,r/£,
h?o
2. of
pzL
7 V
r.r
124
11.0
HIO .37^
h&o
i.c4/
Xoer
w
74
ir;r~
fry
21.1*
-?./*"
P. \f
S3
7 V
/7Lf
}<•*
9~
2.32-
Sr^>
"7V
t£3
3i?<°
c/;u.
J.VO
5.JP-
2. 32-
f! 3
7^
12-1
WM.67?
/. S(A
(/.
1i) \
y/.o
73,4
Estimates:
MW-1-& 8
%mo- 'X-
SVSTEM LEAK CHECK
FITOT LEAK CHECK
Vacuum
(in. Hg)
DOM Rale
(cfra)
Before
After
Poiitive
Negitive
Before
After
OAS 1
2
Impiager
No.
Impingcr
Content!
CHESTER
ENVIRONMENTAL
C02
02
CO
N2
Pinal
Initial
Difference
I.
2.
3.
4.
s J.
V 6.
1.
-------
CLIENT QTi dJa^hy^
TEST UNIT 13 -if faree-
PROJECTNO. ¦$X)2&,/~Q >
S7feK 2-2—
STACK SAMPLING DATA SHEET
TEST DATE /o-jg-g? ORIFICE CORRECTION ( a
TEST NO. C4jg.-2.-z-21-
Page 3 of 5
/,S72- HOT/COLD BOX NO. 6>-r s?>
TEST CREW
STATIC PRESSURE
PITOT CORRECTION
STACK DIA.^t
Traverse
Point
(inches)
Time
Dry Qm
Meter Renfing
(del)
Pilot aP
(in. H20)
0 rifice a H
Meter Temperature
Vacuum
(in. Kg)
Suck
Temp.
CF)
Probe
Temp.
CF)
Impinger
Temp.
(•F)
Hot Bon
Temp,
CF]
ComDient*
Required
(in. 1120)
Actual
(in. H20)
In
CF)
Out
(*F)
3T.o
/r?^
-7.2!
3. 2/
74
ID.1
*-•2-50
. L,
Htft -*
,3, /.r
2. 1 s
?r
C
/P-3
to Sr.
ft tC
/,
7.r
.C. fr
/23
il.t*
^ sr
/,.ro
f,ir
/, 75*
*V
7^
173
A. 8
lltf.oyc,
f,2S~
'/, yr
//V5
W
zr
•J.o
ill
*7/ D
Hbo.yni
/.3&
i.ri
/, j7
XS"
7^
H<1
ms 11 £3 ^
/.20
t Ho
l.qo
!r V
?
1^ yc
I /,Yc
s>^
75~
H,o
J A3
ys3tc,ti
" //^
j?4/
7^
3,
SV
?r
' X.I
&3
i3H.
7.
-------
5?7)c/<- 2,-2_
STACK SAMPLING DATA SHEET
CLIENT \)f,i Clcu^yv tOfrMs
TEST UNIT tf -nT bk-tkx^ ?^J
TEST DATE
ORIFICE CORRECTION ( a H@) f ,g~J2.
Pige of ,5~~
HOT/COLD BOX NO. (o-L
hoi
TEST NO. CU*-~ i-2^- Z-
NOZZLE (SIZE,#) Q, /q~5C
METER CORRECTION (Y) / , &r>Tt
CALIBRATION DATE 1 - - ?J3
PROBE NO. T-3
PROJ ECTNO. JuoiM
STATIC PRESSURE /, & #? £> PITOT CORRECTION
1
o£>r
FILTER NO.
TEST CREW
STACK DIA. 54
Tr»v««e
Point
(iscbe.)
Time
Dry On
Meter Reading
(dcO
Pitot aP
(in. H20)
Orifice aH
Meter Temperature
Vacuum
(in. HD
Stack
Temp.
CF)
Probe
Tamp.
(*F)
Iropinger
Temp.
CF)
Hat Box
Temp.
<*F)
Com menu
Required
(in. H20)
Artua]
(in. H20)
In
(*F)
but
CF)
?£>" O
' I.O
2..? 7
a.n
W
76
£./*>
<68
jt- min./point
33, b
i«5", /e>c(
/, 8
0 IO
2 IO
*.«T
76
A" pL
K(T. 9£ 1
XO
0. 33
p. 33
Sr5"
7C?
L,o
45fS"6
>< fr
bo
V, 7
{2-T
ct. o
hr>
f ib 3*
hSX
kO
4,7
/££>
wl.oor
I / 3
/r
/, f?-
/
/.a?
t.lft
9 O
?
j>y
,2P0
Hfo
3.tf
t.
w3. 113
.80
M
M
90
kO
Xo
'7.^34'
(A
Lb") (
7 )
n*. -7)
(
>
^ 1
V
/
Estimates;
MW= 2-& ©
*H20-rL
SYSTEM LEAK CHECK PITOT LEAK CHECK
GAS
CHESTER
EWOTONMENTAl
Before
After
Negative
C02
CO
Before
After
Vacuum
(in- Hg)
DGM Rate
fcfnQ
Impingcr Impinger
No. Content* Final Initial Difference
1.
2.
3.
4.
5.
6.
7.
A
-------
CLIENT U$S t-6
TEST NO. C^Z— 2-2.- 3-
NOZZLE (SIZE,#) O, 19^
$2
METER CORRECTION (Y) /, g iCi£^ PROBE NO. JT-3
PROJECT NO. 3UJ2^/-
CALIBRATiON PATE 9 -^-^3
3a£
FILTER NO. //
min./point
z/
yuu.s&n
, kO
,
/A.r
1,90
/, V/
i< y/
3,?
/aV
9, O
Wi. QtH
t.HO
!,{,£-
k3>
Vr7
W, ikG>
/r 'YO
A 6 s'
/,Cs~
" ftt
RZL
V,7
/3,
-------
CLIENTQ5S CltuJm UklU
TEST UNIT |?-y«rfW£w P^-
PROJECT NO. JaJZU'^i
TEST CREW V
STAc.2-3
STACK SAMPLING DATA SHEET
TEST DATE /0-xo-7J ORIFICE CORRECTION (&H®) /•
P»ge /
METER CQRRECTION (Y) 0.7b3"Z-
CALIBRATION DATE 5~-f7~23
of 5"
HOT/OOLD BOX NO.
PROBE NO. SV
FILTER NO. y/6^?
TEST NO. 2.-3-2.
NOZZLE (SIZE,#) Q.I&3 :
STATIC PRESSURE
PITOT CORRECTION
STACK DIA3&
Ttiwic
Point
(inches)
Time
Dry Gu
Meier Reading
(del)
Pilot A P
(in. H20)
Orifice aH
Meier Temperitiire
Vacuum
(in. Hg)
Stack
Temp.
(*F)
Si*-
Impiagcr
Terif.
(~F)
Hot Box
Temp,
<*F)
Comment*
Required
.°€o
/V
/,V&
-?2-
6~~o
J- mio./point
31k
/V
aV8
*2-
57o
i/(c
3'. 7
/,£"
/^>
/5B
4,8
£T7o
US'
296
A 6
(bri
?2L
//£
r7.0
#8,9/6
aV
f.H9
£8
<< o
///
13. T-
!<3
b 3?-
(,r^
^3
49
^0
///
00.00^
hi
//6>
A/6
1*1
Ko
///.
*). 0
to. 67^8
/.2-
Ml-
A z.?
76^
9b
6TO
i/4
gw.300
(.3
A3?
rfc>
4:0
IP
gy/.^2o
(.3
(
/.32
Co
//c
6bZ,5tf?
A'
(tile
r?
7/
y.o
/
/q«.
8cs:74o
'
Estimites:
MW= Z-4?' &
*H20-J2
SYSTEM LEAK CHECK
PITOT LEAK CHECK
(?>&•<-
Impinger Impinges
Vtcuum
(in. Hg)
DGM Rate
(efm)
Positive
Negative
No. Content* Foul inilkl Difference
Before
ok.
o/C
I.
fQ^rC >3Wr£o
JVI/
10,1
l/'
Before
iT.O
After
Ot^
2.
/Ca^o ~fcr;4o
*#»•/
U
After
-------
CLIENT \j£S Cloven lAJPiJCS
TEST UNIT Q-nZ Kclku;
STAcXO ^
STACK SAMPLING
TEST DATE {0-Zc.-7J
-2
DATA SHEET P«ge 2 of 5~
ORIFICE CORRECTION ( a H&) (. 73*/ HOT/COLD BOX NO. V
PROIECT NO. 3oo-ict
iCuy
TEST NO. Ci-K-l-J—'2-
NOZZLE (SIZE,#) O. I Qf*~
METER CORRECTION (Y)
offbTZ- PROBE NO. S~-/
7 7~?3 FILTER NO. ffO(o
/¦Q
CALIBRATION DATE S"
"PTTOT CORRECTION Q. 8 V
TEST CREW
BAROMETRIC PRESSURE £c).
STATIC PRESSURE
M
PORT DIRECTION SjjgZ
O
STACK DIA. 36"
CONTROL BOX NO.
PORT SIZE Yr/
T rtvertc
Point
(uiclka)
Time
Dry Gea
Meter Reading
(del)
Pitot iP
(in. H20)
Orifice A H
Meter Temperature
Vacuum
(in. Hg)
Stack
Temp.
(*F>
Probe
Temp.
<*F>
Inpnfer
Temp.
CF)
Hot Box
Temp.
(•F)
Comment*
Required
(in. H20)
Actual
(in. H2fl)
In
(•F)
Out
CF)
f. O
m.&o
l(
M7
i.fr
??
7^-
///
-VZ50
<68
<~Z5X>
d- min /pouit
-i,y
8/f3Cf?
(¦(
(.D
/.Go
&o
1. o
//5"
A7.o
flfc/Sb
/
l.U
/• <£>/
76
7-o
//<£>
2-9. b
&0.9W
{,(*
f.#-
-6o
-7S~
7.5"
//V
aft.sBf
If
L&3
(.83
8cj
9.o
A5"
-? J L
3l0j"/2^
(-€
/<(*!
h^of
s/
76
//?
3
-------
yrMK z--?>
STACK SAMPLING DATA SHEET
CLIENT ClaJt+bA IQciP TEST DATE
ORIFICE CORRECTION ( a H(2>) /. ?JV
P«ge3 oQ'
HOT/COLD BOX NO. V
PROBE NO. 5"V
FILTER NO. ;/C
/./
/. 57
/5?
^2.
7.o
//of
vl^D
<<=>ld
mm./point
33 O
W.i'co
//• <3
(3?-
82-
//S~
3'.7-
8(3, Z^£T
AiT
f.U
/.6?f
02-
^5"
//£
ZCI.L
013.9(7-
hiy
1>1Z*
A?3-
6"3
79
HfT
2-7 o
/-S7
§3
7?
//
BO
fro
//•?"
8# ttf
O
1-36
/Jo
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0D
So
/o?
v.j
8# 83 &
(¦Ho
/.yo
<3/
{».0
/£>?
V
A2-
(<3o
t,3o
SY
80
Co-o
t<&-
AO
/
-------
CLIENT Q$S { QJmkt
$7%c/c- z-3
STACK SAMPLING DATA SHEET
TEST DATE /O-2^-93
Pige Y °f S~
H@) /¦ £?.
CF)
Hot Box
Temp.
(*F)
Coninieata
Requited
(in- H20)
Actual
(in. H20)
I*
(•F>
Out
("F)
2T-0
A5/
/
_i min. /point
311
320,432-
AY
AS7
A 57
&y
8/
7fT
//7"
3\.%
82.1. (32-
aY
/,£"/
A 57
85"
7r
/20
Ifj.isP
8x1. e.io
/,/
AT/
A57
0^
//?
¦J.-? o
&22.^TO
/,o
K°&
8
S2-
<1,8
{J?
(Mo
AVb
ez
7^
(2-T-
*}.
-------
client LX< LOeruU
TEST UNIT 13- If tjitbff
SVh-K
STACK SAMPLING
TEST DATE /o-2 ox/J
Z.-3
DATA SHEET P»gp £> of jT*
ORIFICE CORRECTION ( a H<8) /, HOT/COLD BOX NO. */
-3/
TEST NO.
.
METER CORRECTION (Y) o f}&32~-
CALIBRATION DATE 5'-/7^93
PROBE NO. iT~{
PROJECT NO. ^OOZC/
NOZZLE (SIZE/)
STATIC PRESSURE
FILTER NO. KQfo
STACK DIA.^6''
PORT SIZE -r v
TEST CREW
PITOT CORRECTION o.
PORT DIRECTION hJtaf-
CONTROL BOX NO.
Travcrae
Point
(inches)
Time
Dry On
Meter Reading
(dcO
Pilot iP
(in. K20)
Orifice »H
Meter Temperature
Vacuum
(in. Hi)
Slack
Terap.
(#F)
Probe
Temp.
(*F)
Impinger
Temp.
CF)
Hat Box
Temp.
CF)
CoinmenU
Required
(in. H20)
Actual
(in. H20)
In
rv
Out
CF)
&
8z?.3%>
f.o
AO#
£To
//3
~ J- VXi
JL— min. /point
2.~(
82&,ccc>
ft o
/.ce
S"3
5To
/'?
Z2-
ui
t.z£\
S>2-
<7^
O'i
Qfi, *0°
f./
/7f?
/./?>
£?£>
&2-
S.O
/2?>
9tf.no
(.*-
/,*r
/^t
ir?°
83I.G83
'•2
fH o
/¦*/o
¦&Z-
?.o
12-2—
z1.il
83*^333
A 5/
S6"
/*3
31.1
255 .o2^-
/<&z-
8V
&/
/ZJ
823. 713
/.£
/. 62-
/< A2-
*65"
Bl
9. c>
M.u
83/. 30=?
J.3
Mo
&/
V-o
/ 2Z—
WZ.Cftf
1ST
K-Lo
t\ ~Jh%f
(
=•/18
'
\.~Ht
r
/ytHAs
def
M TJv
fc> 1
vm.
Estimates:
*/Uk
i-3
MW= 28- 6
%H2o- ;L
SYSTEM LEAK CHECK
PITOT LEAK CHECK
Vacuum
(in- Hg)
DOM Rate
(cfm)
Before
After
Positive
Negalivo
Before
After
Irnpinger
No.
Impinger
Content*
Final
Initial
Difference
GAS
CHESTER
tNVIRONMENTAL
CQ2
02
CO
N2
2.
3.
+.
5.
6.
7.
8.
-------
ST^K 2-—r
client usy UlmJZs
TEST UNIT Q'/y /"fc-gl
STACK SAMPLING DATA SHEET
TEST DATE /O-Zo *?.*, ORIFICE CORRECTION (t. H@) i.
P»ge / of
HOT/COLD BOX NO. fl
PROBE NO. 5~- 5"
FILTER NO. ~[/cTk^
TEST NO. ~Z-
"NOZZLE (S1ZEJQ Q' f8^~
METER CORRECTION (Y) Q,Vfc
CALIBRATION DATE
PROJECTNO.
TEST CREW
STATIC PRESSURi
7#
STACK DIA. 3t>
Tr*ret*e
Point
(inch**)
TiHK!
Dry Oms
Meter Reading
(del)
Pllo* tP
{in. H20)
Orifice i K '
Meier Temperature
Vacuwnt
(w. Hg)
Steele
Temp.
(*F)
Probe
Temp.
(*F)
Iropiijer
Temp.
(•F)
Hot Box
Tenip.
(•F)
Couunenti
Required
(in. H20)
Actual
(in. H20)
In
(•F)
Out
(•F)
IS-O
/&> /5/
O <7
l.oi
7^
-70
3- "5"
t/n
^150
^^6
^SO
jl min./point
3ZL
9
If
/. ?r
,.*r
7O
no
y.o
/of
X7-
/P7-
/ /
/.?-7
i? 7
7/
70
¥ If;
f/n
tf-b
^7.^/
/ /
/•¦a 7
t.%. 7
n f
v.o
iff
x 7>o
•
/.jo
7%
7o
/o?
27. z-
/JP9-2/0
/ '
/al?
7/
LeJ
vo
/c?
'2.«
/fc.fCdc
<5-?
AOJ"
7Y
*?o
f»Y
tf.o
(10 . *>/
/. <5
htO?
Cf)
/s>f
/ ^
/.V7-
J.Y&
go
70
v,r
/ 0 O
jti. v?-y
.
Hstimites:
MW=^S.°
%H20=JL
SYSTEM LEAK CHECK
P1TOT LEAK CHECK /5~^c^
Vacuum
DOM Rate
/
Ptakive
Negative
(in- Hg)
(cfm)
Before
0/?
^AT
Before
otfrt/'
After
"X
o«r
After
0. OS /
OAS
I
2
C02
0
02
?o.r
CO
u
CHESTER
N2
79. CP. a
m.f
iCfiJ
9.^
2.
£r>
SZfc-ql-
yw/
2.1
3.
yy-r.6-
0-(
4.
C]>r//l^£eJ?
js/. ?
5.
6.
isHs
7.
C"
8.
-------
5TfyUC-
CLIENT (JSS QeukU L&M.
TEST UNIT (3~/ST gzfib^u/ P^-
PROiECT NO. 3Ltg^ I -u1
STACK SAMPLING DATA SHEET Page ^ of S~
TEST DATE jp^ z» <}b ORIFICE CORRECTION ( a H<3) / HOT/COLD BOX NO. ^
TEST NO.
"NOZZLE (SIZE,#) O-/gj?
METER CORRECTION (Y) 0 .Z> PITOT CORRECTION oTs/ STACK DIA.
TEST CREW
Tr«v«»o
Point
(inches)
Time
Dry G«
Meter Reading
(B
"7 min. /point
>4
/ -r
,.?7
t.nn
/n
<3
/co
Y3
tit ?sr
/ /
/.u.
?/
£*¦0
}c/
/
r c-
7^
/-.O
<¦->£
9.0
/ ?>
iif
/ y/
&o
/TO
jh*i
tu8
t.l!
/9f
Xa
*71
f.a
13.2-
/17.M9
t.S2>
*?y
j? ©
/oQ>
Ll-O
/9f- tin
'•i
!<*i
r*
/ /'"l
2"v-6
[iff-
/.3
/'7(r
/.*7£»
f*
-r.jf
///
y7
f.O
/.r7
rv
7?
ZeXyiiO
hbH
f-vf
xi
/} o
3&i. £>/<
f /
Est i males.•
MW=2©k3
*H20- i-
SYSTEM LEAK CHECK
"Vacuum
{in. Hg)
DGM Rate
(cfni)
Bcfote
After
£ftA CHESTER
ENV1RONMFN1AI
PITOT LEAK CHECK
Impinger
Iropiager
Positive
Negative
No.
Contents
Final
Initial
Difference
Before
1.
After
Z.
OAS
I
2
3.
C02
4.
02
J.
CO
6.
N2
7.
8.
-------
CLIENT Ljy Ckudan Lkrote
TEST UNIT fey flgC,
PROJECT NO.:icCait-of
S7fe/C 2-^f
STACK SAMPLING DATA SHEET P«ge3 ofS~
TEST DATE ,g- Zo-~?3 ORIFICE CORRECTION (a H@) Aft?#. HOT/COLD BOX NO. £
TEST NO. - 2 -•/- "2-
NOZZLE (SIZE,#) Q. /ICS "
METER CORRECTION (Y)
l?
¦ao3-O07
f-fa
/.r-j
/.IP?
pi
fo
ion
Tfl.i,
/¦d
/ 77
;/">7 j
, ^
To
6,-0
/oU
?7 o
/ •/
7<=)
T.o
/«7
211
/.y.5
TiR
/•«
rTf
J.o
to 7
sutf.7?/
/¦o
/./<7
/./
fTo
y.o
t*f
3b7 • ??/
f /
!.3>
/,3>
fa
Fo
/o 7
2.4
¦ao^.y/69
I. o
I'-Hjo
i.ao
&>
7
/
^o-5.^7X"
Estimates:
MW= ^6.8
*H20- Jl-
SYSTEM LEAK CHECK
PITOT LEAK CHECK
Vacuum
(in. Hg)
DGM Rate
(cfra)
Before
After
Poaitive
Negative
Before
After
Impinger
No.
Impinger
Contenu
OAS
CHESTER
€NVIRONM6NTAt
C02
02
CO
N2
Final
Initial
Difference
1.
2.
3.
4.
5..
6.
7.
8.
-------
CLIENT OSS (Jkudvt (Anfc
TEST UNIT
PROJECT NO. lojkj-6/
?7#ciC 2--V
STACK SAMPLING DATA SHEET
TEST DATE /C>-2^'fS ORIFICE CORRECTION ( A H@)
TEST NO. CCjt--.Z-V-Z- r
NOZZLE (SIZE,#) 0,/gJ*"
Ptge^ of 6
/fr#, HOT/COLD BOX NO. ^
METER CORRECTION (Y)
o-y^/f
PROBE NO.
fsr-.-r
CALIBRATION DATE
, "4t Q PITOT CORRECTION
FILTER NO.
TEST CREW
STATIC PRESSURE
-/ 9
31,1
" i-
t. JjM
j.1
5U03*
?.o9-
5T7
to
-7. O
//<->
f
HZ-ofo
if
/.¦?r
/¦if
r?
r.r
///
Z-7-o
(oO
tO
til
r,1
fTZ
5.o
}t"^>
43
Hit,.
/¦/f
A/X
ti
y.o
//{
ii
SL/6..75/
/. I
(.10
Jo
m
fti7 ¦
Q.&
o It*
o.?fo
90
W
foS"
J3U*?. <*/C
Estimates:
MW-Z-8-S
56H20-J,
SYSTEM LEAK CHECK
PITOT LEAK CHECK
Irnpiager Impuigcr
Vacuum
(iA. llg)
DGM Rate
(cfm)
Pontiv©
Negative
No. Conleiiti Pinal Initial Difference
Before
].
Before
After
2.
After
OAS 1 2
3.
C02
4.
MfU CHESTER
yjnr CNVinONMeNTM.
02
5.
CO
6.
N2
7.
8.
-------
CLIENT U£S Clgjjhn Ltty^
TEST UNIT
" — oh 1-6/
477k^ 2-y
STACK SAMPLING DATA SHEET Page 5~of
TEST DATE id'2-0-93 ORIFICE CORRECTION (6II®) / fC^ HOT/COLD BOX NO. pt
PROJECT NO. yjoZC,
TEST NO. - 2--V- 2- ,/
METER CORRECTION (Y) „. 9^,7
PROBE NO.
FILTER NO. /Jc<5
NOZZLE (SIZE,I)
"• / fit,
CALIBRATION DATE
£L
TEST CREW
r^i
STATIC PRESSURE ^ 'a.&,Vro PITOT CORRECTION O
STACK DIA. 74
T reverse
Point
(inches)
Time
Dry Ou
Meier Reading
(dcO
Pkot i P
(in. II20)
Orifice aH
Meter Temperature
Vscuure
(in. Hg)
Stack
Temp.
(*F)
Probe
Temp.
CF)
Improper
Temp.
CF)
Hot Box
Temp.
CF)
Comments
Required
L (in- H20)
Actual
(in. H20)
la
(•F)
Out
CF)
L 0
a/£
_i min./point
Z.V
9-i $.-70 £
I.O
i.ai
Y-.r
«,3
/>3k
f.'iJS
>.*5"
9/
Jr<
j*. 0
/o4/
l'Y
' /. 0
1,1
/./<=?
/y
y.5*
//o
9.v>
- t o.
/.•V3
/y
//
I.7.0
I-J3
f
$V
1.10
<=>*
-7.0
li2\
337o
aja^TTs'
/ V
t.&o
1 ¦LrC'
fd
H-
Ajj
swio'
hot
A 'CO
M*U
16 "
On
(T&,
«*¦ '8°^
TMrh
sY*\Lv
rtof
s, p\*
(Vfc
r\\JL>
Estimates:
Aims
12-
MW=^8 6
%H20-jl
SYSTEM LEAK CHECK PITOT LEAK CHECK
GAS
CHESTER
Bc/ore
After
Pojitivc
CO
02
N2
Before
DGM Rale
M">)
C02
lmpingcr Impuigcr
No. Contents FinxJ Initial Difference
t.
2.
3.
4.
5.
«.
7.
t
-------
t
t>*-rT
r.»
1
.4*57
/J3
7-StT
i-'.Jl ....
4-^i7
H
£>o?
' &k
i?r30
/3
/Y
g'/O
*//
1 (**¦
/W
/¦¦"*
•^y
fi-ft
/*""
JO-oto
: Vir
/3
/o-/*
/jr
/&.-/7
^7
/3-ssl
/d03
,20
A-**
./*-
/£»*.*}
/r-j?
/0-'3£~
3
Jj-zr
/O'fO
U.JS5
ptfC I 3-y-=r*
lo 1-3.1 1*3,
)pl© -4:40
($7-- c^*> fx^Ucf
U- 3*3'"*^ ^
C^/esJ
SatT
*
3)
&ro( (0
fj
32-
A -*7
/r
3>
35-J&
S3
/e-\£T7
5V
A-a9
/s~
// "*¦"
S"
-------
client (Jsi Uaictvn
TEST UNIT IZ-/S- T'gO
57flcfc. 2-/
STACK SAMPLING DATA SHEET P.ge / oi^T
TEST DATE /Q-^a/^?3 ORIFICE CORRECTION ( a HQ) /. U?3> HOT/COLD BOX NO. Q
¦ZT7&U.I
~zMl
TEST NO. 3
NOZZLE (SIZE,#) O, \
5? 'S
U^%
—'iSD
'vZfb
i- min. /point
33L,
<£>33. Y53
a. i
i ¦<>
nn
-?®
-77
3,<
/2.1
%=h
k
¦
£-7>c\
77
*77-
7^
"7*3
17- S
133
/..«r
(. 7°l
/27. 75t
I'M
I'/sl
1 > Lr~7
~>7
77
[lie
*?.o
'rTlfc
1.4
/• (/7
1-1/1
^>.n
1^-7
/, 5.
),W
2>o
~7C}
lCL(?
<3
(&3o'05Z
¦ /• /
)-37-
¦ l-3>
9>\
feO
3 c?
12-b
o?. V
h3o, 73.<
/' '
I <3 "2-
Z-3-2-
-a/
7-n
C3/.V3/
I.O
\ao
1 . 2-0
: 7Q
*)Z3
(p3X ioB
4l'
£
--— —¦
/ -i i nit
^
t
—A
(b< I • 1 uw
t-foSL
)
)
(
I2?T3
Esltmiles:
V
s
*H20-^t
Vacuum
(in. Hg)
DOM Rote
(cfm)
Before
.c
j no A
After
( K
oK.
After
a> k~
C?&
OAS
COi
—-¦
02
VAL
CO
/
N2
-n4
No.
Content*
Final
Initial
Difference
i.
iQOm£~ !?[£> /L O
lo,T
2.
/¦ $&**£ HtO
.<31,2.
2.2-
3.
LMo.<
<0,3 ,
4.
^7^-7
<,ne>
8.?
5.
6.
ZLTf .
7.
>
S.
-------
5T&CK z-(
CLIENT C7 lO&l&
TEST UNIT (3- /*y SaifOo/ T&L-
DDftlCPT MO / j . -n / '
STACK SAMPLING DATA SHEET Ptge 2- of 5~
TEST DATE >Q~Z/-V3 ORIFICE CORRECTION (i H®) /, £,-?J HOT/COLD BOX NO. Q>
TEST NO. CM*-3
NOZZLE (SIZE,#) O. I^Q''
METER CORRECTION (Y) 0,9^2-
CALIBRATION DATE
PROBE NO. S~-V
PROJECT NO. 3cpUal-Vl
ST ATJC PRESSURE PITOT CORRECTION 5 &
FILTER NO.
WS-
TEST CREW
STACK DIA.
Tiiverie
Point
(mcbca)
Time
Dry Q«
Meter Reading
(dcf)
Pitot A P
(in. H20)
Orifice aH
Meter Temperature
Vacuum
<». H*)
Stack
Temp.
CF)
Prob©
Ttrnp.
(*F)
Iniplflger
Temp.
(~F)
Hot Box
Temp.
CF)
Cora meaU
Required
(in. H20)
Actual
(in. H20)
In
CF)
Out
CF)
f.v
673^.10%
f (, P
M°1
fcl '
3^
l?-l>
jL min./point
*4
tp32> • ~75z>
"/,/
f i Z 1
1.31
0/
So
¦So
If7?
4.1
&33. HfoO
// /
P3J
1.3!
2/
7?
/7-V
(*34. Ii 7
11 1—
iJjs
i
3' f.
> 'iC»
Jo
)'Y
} •(s>0>
/¦ bCo
"7?
77
3,0
/zy
{*8
/artfiT. <*ic
/, 7?
h 7
i.lo
h?a
7#
7^
3 O
In2*?
zf°
L31. afrE
/ ' Cj>
hfo
A 9£>
-7^
"7 Co
x,o
z%L
6*38, /S1
I'ft
^?./V
7*>
7G-
3'(o?-
Z'b-Z.
- 7ff
77
/^Z
1
C?8.3;
' ¦
/23*3
>
Estimates:
~~
~~
MW=Z-&>.
-------
CLIENT KJSS Cio^Ul OOiP'tS
TEST UNIT ['£-(3-rt&
PROJECT NO. looxj-o/f
<5T$CKz--[
STACK SAMPLING DATA SHEET
TEST DATE IO^t-73 ORIFICE CORRECTION ( *H@) /,L?3
TEST NO. OJI-- 2W-3
NOZZLE (SIZE,#) O-
Ptgc3 of 5"
HOT/COLD BOX NO. ^
METER CORRECTION (Y) PROBE NO. S~-f
CALIBRATION DATE
STATIC PRESSURE ; , Qc PITOT CORRECTION O
FILTER NO. 111
TEST CREW
STACK DIA. 3fc
T riverM
Point
(incHet)
Time
Dry Qu
Mck* Retduig
(dcO
Pitot h P
(in. H20)
Orifice aH
Mdcr Tempeiature
Vacuum
(in. Hg)
Suck
Temp.
(*F)
Probe
Temp.
CF)
Inpinger
Temp.
CF)
Hot Bon
Temp.
(*F)
Comnenti
Required
(in. H20)
Actual
(m. H20)
In
CP)
Out
(*F)
~)£d
ML&tX
1 1^
"2-<(0 1
-79
7 7
4t
2 L>(
79
7?
V'Ci)
/23
(*<#.14 i
l.-zO
^^
77
"7/9
V,a
236
• Cc(3
I-ft
Xii
2,ft/
7?
3^
f
2fiO
6 VS~> 1
1' ii?
llo
MO
P.>n
79
3.o
zr-3~
CrV&.'MoO
hG>
tlo
h *70
tp> 1
3^
ft-.S
(oil
t'V
I.CC,
/-CrCo
9>o
3^
/>3>
8 1
&o
3¦ 0
("2*4
(&9. 5-3<
' I, 7~
'-VJ
#2-
??o
3'0
*4
w ,
^To.27.5-
' / , J
/ '3 1
'¦$/
8/
&o
3-0
/*3
/. »
1 < '~>
l.i^
m9
77
7V
ill
\
fa-/. MX
[77.1
)
Ct*0
r
J
•~o
>
Estimates:
mw- ^8. Q
%H20-
SYSTEM LEAK CHECK
PITOT LEAK CHECK
V«ciwm
(in- "J)
DGM Ra(e
(cfn>)
Before
After
Poi'rtive
Negative
Before
After
Impinger
No.
Impinger
Coolcfltl
GAS
CHESTER
ENV«0NMCN1AL
C01
02
CO
N2
Find
Initial
Difference
1.
2.
3.
.
4.
5.
6.
7.
S.
-------
CLIENT U>S C<6-Jckn Um-fc
TEST UNIT 17 vr fcj&cy F&C-
PROJECT NO. loOZX.t- W_
ST&it- 2-(
STACK SAMPLING DATA SHEET
TEST DATE { ORIFICE CORRECTION ( &H@)
TEST NO. Cz^-2.-/-J
NOZZLE (SIZE.#) O/ffoT
p«ge -y1 of 5"
HOT/COLD BOX NO.
METER CORRECTION (Y)^ 0,79/^ PROBE NO. j5~-V
CALIBRATION DATE
STATIC PRESSURE nC>'' (h.O P1TOT CORRECTION
3
o -ey ~
FILTER NO.
TEST CREW
STACK DIA. jfc,
Travero
Point
(inckca)
Time
Dry Gat
Meter Reading
(
2-30
"7 5"
7^>
^5D
jZ- mtn. /point
yi.t
6&.^l
¦ "2—
2-6^
X&2-
7y
7^
V, n
//^
1^-2-
2->6^
- 73
7/
i ,
H'O
//5"
23-1-
z
^•6)
^-?>8
~73
7/
3,
2^»7.
- ! i Ce>
}.4o
72-
7 (
7>.o
//<
l^R
6>5"7.olC
i.r
1,78
// 7^
7 2-
no
3.0
//s-
^7.=lol4
J
|. LfCy
7P.
no
3 o
if (p
//S-
h 1ft
/.7g
7/
b°}
3-C
//,<
f-s
/¦ 1&
A 7^
"7 /
no
3' O
//,<
0?,V
!• (j?Q?
, "7 3-
7
//V
1.3
r<<
7a
7/
3-o
//3
s
(
/, £
)
r 5.0 1s!
7/,/*
>
'l1*1
)
Estimates:
y
MW- 2g, g>
-
*H20= _2-
SYSTEM LEAK CHECK
PITOT LEAK CHECK
Vicuun
(in. Hg)
DOM R»to
(cfm)
Before
After
Positive
Negative
Before
Alter
tmpinger
No.
Impinger
Contents
OAS
-------
575fc< 2--1
client q:j, ckuJcbi LOuz.te
TEST UNIT n-K&tbUvTt
PROJECT NO- 3cQ^b/~jL>!
STACK SAMPLING DATA SHEET
TEST DATE tO-V-?7 ORIFICE CORRECTION ( a HQ) /. L?J
METER CORRECTION (Y) O ,77/2.- PROBE NOT
Page 6~ of S~
HOT/COLD BOX NO. Q
TEST NO. 2.-(-3
NOZZLE (SIZE,#) Q'I?i7
CALIBRATION DATE
STATIC PRESSURE | . PITOT «)RRECTION qT&T
FILTER NO. 11) 2.
TEST CREW
STACK DIA. 3C."
Tr*w«e
Point
(inch*)
Time
Dry du
Meter Reading
(def)
Pilot A P
(in. H20)
Orifice aH
Meter Teraperaturc
Vacuum
(in. Hg)
Suck
Tenp.
(*F)
Probe
Temp.
<#F)
[lapipgcr
T«p.
(*F)
Hot Box
Temp.
(•F)
Comment!
Required
(in. H20)
Actvtl
(in. H20)
In
(•F>
Out
(*F)
ho
hi
It (a (*>
/'£»&
-73
7/
2>.o
^zro
jJ. min./point
b>(*2ATl
/W.
1 • (l>L?
}.(»<*
"73
3,
1}^
(s>C?2>/2l>3
i .<
1.1£
\.7
73
7.2-
S.O
\\Le
b
r
!-L
t
/.*9
7^
73
3.0
ti$
ft-S
1, IS
).7&
¦7^
7-/
3-D
23.2-
1 • G
).99
h*<>
~>S~
-7 V
^ O
ill
z?>°
C,6>7. fp>0
t.A
"7
75T2
3.<
lie
&.(*
2,o
3.3 (*
3-3Q
7S~
7V
3\
2,7-
> UZ-
¦
7<
H
/, %r
J?, is-
a./s-
nn
f#7
Zl.O
4s-7. 7S-P-
/ ,C>o
/, S-9
/.
2f&>
Hto
(3$-
VIT-
m'
'/,s-o
/,77
/'? 7,
frC>
j>,9
I Iff'
(z-8
^r=t. 34^
j^o
/,(,r
h 6 5"
9£y
srG
3,JL
/29
Vo
OP?
t,3a>
J'S~3
/,5-J
Z-G
if, A
!P$
\
qu>, inL
(.OX
//V?
/W7
9V
kC?
.3, /
fffl
•-
H(A. rzf
/s/o
/,3o
/,Z&
9o~
K7
i
j.*/
,4o
on I
o. 7/
x.rN
0 (o&
o. 11
£>, 7/
qQ
5.o
/a.%
\
r
W3, 364
1,12.0
£,
!.o3)
9?, 3
m.i
Estimates:
^ /
t— "*)
MW-2&B
V
*1120-2,
Vacuum
(i». no
DOM Roe
(clin)
DtTore
-tfj?
'Oef
After
*?i£
<»/
CHESTER
tNVUKINMFNMl
Poiilive
Negative
Dtfote
afi.
e> K
After
OAS 1 2
C02
02
3,0. 'i
V\\
CO
N2
'?H,5
No.
Content*
Find
Initial
Difference
1.
/qw 4
4.
(t>M O
At,
3.
6.
-MJ1 -
2t\ 80
7.
A
t.
-------
STfle-X- 2'^~
STACK SAMPLING DATA SHEET
P»ge 2- of
CLIENT U$S CIcLucjon lOoifcS
TEST UNIT 13' fed
PROJECT NO. IXDUj-ck
TEST DATE /o-*S-J3
TEST NO. 1-3
ORIFICE CORRECTION ( a H©) HOT/COLD BOX NO. (n
METER CORRECTION (Y) PROBE NO. 5^3
NOZZLE (SIZE,#) o/
~Z5T»
jf_ m in./point
<&3. 123
.La
O, l!
&. -7/
2.0
I^Sr
ven,
! ,oo
his-
/r/r
9/
frST"
2.
ijjt
L.i
iLr.M
' L£o
A Hi
/,
Lk,f.1L2>
hW
US'
' /,£/"
Sr*?
.7, 4
/*?7
It
*,SL
H.o
vltO
Htti. e>v)
/.ko
?.X1
3 U
/,9o
2.X>-
2.2a
HH
1 27
31L
Hlc.
-------
STACK SAMPLING DATA SHEET
CLIENTQ$i Cjftxc4*l MnKf TEST DATE/o-ZA-T?
Pigcg of S~
ORIFICE CORRECTION ( a HHOT/COLD BOX NO. (g
TEST UNIT (3-/
Probe
Temp.
CF)
lnpSo|er
Temp.
(•F)
Hot Box
Temp.
CP)
Comment a
Required
(in. 1120)
Actual
On. >120)
In
CF)
Out
(*p)
3$: o
WX, 2>I^
Q.O
Q.m
90
?£¦
• b .O
/SL7
xt»S
_3- nun./point
Ji4
nn.iK,
2,6
2.-51
2.3
inc.
It lb
CH
!<^l
£2.
3. <2
t*l
*
J.4
W. W
-b°
.9
in.H
Estimates:
MW= 2-9, S
*H20= JL
SYSTEM LEAK CHECK
PITOT leak check
liapingcr Impingcr
Vacuum
(in. Ilg)
DOM Rue
(cftn)
Positive
Negntlvo
No. Content! Find Initial Difference
Before
1.
flcfuro
After
2.
After
OAS 1 2
3.
C02
4.
/Zfr CHESTER
C NV( K )NM( N1AL
o2
5.
CO
6.
N2
7.
1.
-------
client OH UcuJdton DmiS
TEST UNIT /3- /
CALIBRATION DATE
7-t-?3 FILTER NO. tff\
TEST CREW
STATIC PRESSURE / fj
P1T0T CORRECTION b-gV
STACK DIA.X/
Trunin
rw
(hclw)
Time
Dijr Gas
Meier Reading
(ifcf)
Pilot *P
(m. II20J
Orifice All
Mrter Temperature
Vac aura
(». Hg)
Stock
Temp.
CF)
Probe
Temp.
(*F)
ImpMger
Temp.
(*F)
Hot Boi
Temp.
(•F)
Com rnenU
Retired
(ML 1120)
Actual
(in. 1120)
In
CF)
Out
CF)
frv
v*/, l*5>
P. 1
2.76
,r.2-
t*7
~ZSTb
^8
^•LSX>
JL min./poiirt
3iL,
wt.Sss'
p, o
Z 3 3
J?>33
$~,o
IXI
31,4-
^3, HHH
P., 2.1
-7/
H, %
w'/.i/l
/,
2, /o
zH
Hi 7
f^-S
Hbf. /
- A 7
un
/<¦
£3
H,Z\
taH
ZXZ-
«#r. 9PJ
h L
u%t
//^
X 3
74?
hA
/¦2 V
ti8
73/
/, l<
" //
/£?
l.o
v&7,
i, £3
/,£3
7£
3,9
'/^T
u
V^rgT.
l.H
Ad3
,/^3
7C
/£J
_12_
ho
ys^, o3
W. £7/
I,lo
f.fO
7(p
'1
(
/*5~/gr
) fi.
%)
^3.3
T). 3k
l2HtO
Eilimitos:
MW= 2^?,
%H20=j2-
SYSTEM LEAK CHECK
PITOT LEAK CHECK
Vacuum
(ill. Ilg)
DOM Rale
(cfrn)
Befcjcc
After
Positive
Negative
Before
Aftor
Inpingcr
No.
Impinfcr
Contents
OAS
CHESTER
(NVUKINMENTAl
C02
Ol
CO
N2
Final
Initial
Difference
1.
2.
J.
4.
5.
6.
7.
1.
-------
CLIENT Lhixkn (XJir<& TEST DATE
TEST UNIT (?- /
TEST NO. Cqt-i-i -3
NOZZLE (SIZE,*) o, I'll7
METER CORRECTION (Y) /-o/g? PROBE NO. b'-J
CALIBRATION DATE
FILTER NO.
VP-
TEST CREW
STATIC PRESSURE
D PITOT CORRECTION
STACK DIA. 3
.2, f
JZ- rain./point
z hO
U8*
77
H,l
jM
H9C.
/. £,<*
Ji.il
3J7
&7
7^
LLfr
497.1U
t~q<
2.24
£7
ytr"
t? V
i
7i. L
UQk <7.2
2. OO
2,3 tr
3l.3
-------
CLIENT \JSi CkuJck*}
TEST UNIT tScrfUf ?a£ TEST NO.
STACK SAMPLING DATA SHEET P«g> / ol5~
TEST DATE /0-2y-?J ORIFICE CORRECTION ( & HQ)/HOT/COLD BOX NO.^/
METER CORRECTION (Y) q^Sj^
PROBE NO. 6'V
FILTER NO. /C?5"/
STACK DIA.3fr"
CALIBRATION DATE
NOZZLE (SIZE,#)
STATIC PRESSURE {,-2-*4^,_Q
O' W
TEST CREW
PITOT CORRECTION
' 'tlv J Itv/I C
DAROMETR1C PRESSURE 2-{ PORT DIRECTION CONTROL BOX NO.
PORT SIZE ^Pr
Tr*v*r«e
(i«che»)
Time
Diy Om
Meter Reading
(*=0
Pkol aP
(in. 1120)
Orifice *11
Meter TemperMure
Vacuum
(«. "«)
Sud
Temp.
CF)
Probe
Temp*
<*F)
lmpio|cr
Temp.
(*F)
ffot Bon
Temp.
<*F)
Comments
Required
(in. 1120)
Adi»i
(in. 1120)
In
(•F)
Out
(*F)
5^.o
936
l<3
(M(
/V/
6^
85"
£r,o
(3&~
*60
"7. min./point
35 fc
8^>.ooo
(S
/. 6/
/Y?/
85~
/X=t
7^.7
/-S~o
/,£
/,5o
«£>"?-
C^S~
}23>
2.1.o
838- cfio
u(
UQ
(.(8
7^
87-
4TO
fz.
/.Vo
88
(yC>
(2$~
l2-ft
S3
(<7$
!
)?-?>
V.J
9tL &S
(<2-
\<2f\
u?
7^
<57
(?cO
/Z4.
,
&u?so>
(' &
L^6
/.«=€>
SB
*3*0
!< O
V+2-9/8
/'O
[•Ob
Ace>
y#
5
V3o,f
J.
WZ.'i
vW-/
"0,2-
4.
^iiluyfctU-
C*8o.Z
<0?O,~}
S.
6.
7.
>
t.
u
-------
CLIENTS
TEST UNIT ()-ff fiz^
PROJECT NO. ->u02o/-Jf
5^^: 2~-3
STACK SAMPLING DATA SHEET p»gP Z- of 5"
TEST DATE /Q-Zt-ll ORIFICE CORRECTION ( a II®) /, HOT/COLD POX NO. V
TEST NO. C+,
NOZZLE (SIZE,if) 0//^
METER CORRECTION (Y) O H&T-
PROBE NO. jTV
STATIC PRESSURE 1,2
CALIBRATION DATE
5~-g??3
Pit"
FILTER NO.
TEST CREW
1
P1TOT CORRECTION
STACK X*K.3(,
DAROMETR1C PRESSURE £=>. 2-<
PORT DIRECTION
Jii
CONTROL BOX NO.
PORT SIZE Y*~
Traverse
Time
Dry Oh
Pilot *P
Orifice aH
Meter Temperature
Vacuum
Slack
Probe
[mpingef
Hot Bo*
Comments
Point
{inches)
Meier Reading
c*o
(in. 1120)
Required
(in. 1120)
Actual
(in. 1120)
In
(~F)
Out
(•p)
(in. lift)
Temp.
CF)
Temp.
(*F)
Temp.
(•F)
Temp.
(•F>
t< °
f< o
/•o8
C0
lo
5TO
CZo
**ZSb
^48
/^250
min. /point
hi
l.o
|.o8
/«o8
%
5"rO
!*-<
3
mm,
M
f.l?
(,(1
88
5^5"
(22-
1.3
AVo
/.Yo
&e>
%o
/2.V
1,0
l?>
tMo
/s/0
6&
sy
l.o
(*3
/£¦&
fyjb' Ot°l
I<3
A3?
f.39
ft*
86"
?,o
/20
'2-3.2.
uib, ids>i>
/¦*-
u%
LP??
&h
0*/
/2»3
m.-xz-
/<3
aT?
87
~7 o
I.IoO
l.ioO
IZ3
31.7
m<*38
A k
\JI
I-?/
no.o
f23
f
¦K.t-
/¦U
«¦?(
Sl
lo.o
1 23
3 f.o
15"
t.t-o
/. loO
Sl
ft!
9fO
/23
\
r%C> f)2o
i
j
j
Eiti miles:
MW= z<£.8
%H20= 1
SYSTEM
I.EAK CHECK
PITOT LEAK CHECK
Impinger
Impinger
Vacuum
DCM Role
Positive
Negative
No.
Contents
Final
In it ill
Difference
(in. Kg)
(cfm)
Before
1.
Before
After
2.
After
OAS
1
2
3.
C02
4.
02
5.
CO
6.
CHESTER
N2
7.
bNVMONMtHIM.
ft.
-------
CLIENT V^5 C4(xW^~
3/^kJL z-3
STACK SAMPLING DATA SHEET P.gej of ^
TEST DATE ; V -2/-93 ORIFICE CORRECTION ( a H@)/, HOT/COLD POX NO.
TEST NO. ^^-.z -3-1
TEST UNIT
fc-
METER CORRECTION (Y) O ^&3Z- PROBE NO7~T^I
%
PROJECT NO. ICQlGt-Of'
NOZZLE (SIZE,#) G,{&V
CALIBRATION DATE
5-W
o8r
fr
FILTER NO. /057
STACK DIA.
TEST CREW
BAROMETRIC PRESSURE
xT
STATIC PRESSURE
PORT DIRECTION
//2>'
£
PITOT CORRECTION
CONTROL BOX NO.
PORT SIZE V'
Tmvkk
Tim
Dry Clai
Pkot A P
OrHke Alt
Mriet Temperature
Vacuum
Slack
Probe
Impinger
Hot Box
Commcnti
Point
(inches)
Mdcr Heeding
(del)
(in. II20)
Required
Cm. 1120)
Aetna!
(in. »I20>
In
(•F)
Out
(#F)
(in- Hj)
Temp.
(*F)
Temp.
CF)
Temp.
TO
Temp.
CF)
3f,o
&50.B2O
/•<
/.4t>
(
86
8^
9.0
Iho
t-s
t.bV
LtoO
S3
S'O
23,Z-
as1/368
/3
(,3°!
/.r?
8C>
83
?.£T
/-*/
tt-b
9ss, 02y
l-*~
/^3
9,°
865",^
1.3
/.37
83
?.s~
/25~
U
S5fe.262.
1.2-
/«z0
Sfc
&3
7-o
/^V
(i&
?5C
83
c?.&
/£/
,
jA
/¦o
A ^
l.o?-
83
r.
-------
CUENT CkuM*f W&M
mes
^rrr
-y/^kjL 2^3
STACK SAMPLING DATA SHEET
TEST DATE ORIFICE CORRECTION ( a 11®) L
P»ge ^ of jT
HOT/COLD BOX NO. V'
TEST UNIT a -ft
TEST NO. C^Ut - -z-3-3
NOZZLE (SIZE/) O. (fcV
METER CORRECTION (Y) PROBE NO. 5~-/
PROJECT NO. 3co//J.
/.t'io
' 3^
CALIBRATION DATE FILTER NO. /£>,5Y
PtTOT CORRECTION O'ZiY sTArif niA -j/
TEST CREW
DAROMETR1C PRESSURE^'
STATIC PRESSURE
STACK DlA.3fc-
id_
PORT DIRECTION
CONTROL BOX NO.
Temp.
<*F)
Temp.
CF>
Temp.
(-P)
Temp.
rr)
/V
AS©
t<5£>
Bo
?.o
//5~
.i min
/point
7JC
is
(<(oD
/.£o
¦eo
n
/a 5"
//5"
111
&$7,9#-
/• Co
VK
\^(
06
// o
2S?.t
Sko.kz-^"
/.if
l
•&e>
/0<5"
//6
3b»(.3(o
/.v
t.^o
(.££>
7?
/&o
//7
232-
(.2-
/.z-5
1.Z&
8^
71
8.o
//£
tz&
&*¦¦*»
M?
7-?
%
7-o
/(-?¦
9,o
&£.tz4
f.77
/,7?
/V
7?
9
43
/.6b
i.^o
79
7k
/O. o
HO
3A
u
i.*?
76?
7.5~
///
t.o
?&.yz4
/,2-
/.z-9
go
lb
7-5"
///
9Uc,^L
Estimates;
mw-z^S. 8
xiuo-J-
SYSTEM
LEAK CHECK
PITOT LEAK CHECK
lntpi»ger
Irnpiitgec
Vacuum
DOM R«le
Positive
Negative
No.
Contents
Fine]
Initial
Difference
(in. lift)
(elm)
Bcfon
1.
Before
After
2.
Afler
GAS
1
2
3.
C02
4.
02
5.
-------
CLIENT \JS>i CIcuxLa UdcnkS
TEST
PROJECT NO. ¦ba^Zofr
S7MJ^ 2--3
STACK SAMPLING DATA SI1GET
TEST DATE 10-U-173 ORIFICE CORRECTION ( a 11®) /, 7-j/
P«ge 5~~of
TEST NO. Cttf-- 2.-1-1
NOZZLE (SIZE,*) O
HOT/COLD BOX NO
IE
/tee-
METER CORRECTION (Y) 0i.T&j. PROBE NO. jp7
CALIBRATION DATE
STATIC PRESSURE /, P1TOT CORRECTION
6'W
FILTER NO.
753?
TEST CREW
BAROM ETRIC PRESSURE 21,
STACK DIA
~1Z
~~w
M
PORT DIRECTION
CONTROL BOX NO.
PORT SIZE
Ttavene
Point
(incliel)
Time
Dry Ou
Meter fludinj
(del)
Pilot i. P
tin. II20)
Orifice <11
Meier Temperature
Vacuum
(in. Hg>
Stack
Temp.
(•F)
Probe
Torap.
CF)
linpinger
Temp.
CF)
Hal Box
Temp.
CF)
Comment*
Required
(in. 1120)
Actual
(in. 1120)
In
¦CP)
Ou(
(*F)
f,o
/,3
I'll
f.3e(
8o
fco
l|"2_
vJ-^ZP
«.&
^z-5zi>
_i min./point
z.i
!• 2-
/<*?
/.t«7
0O
7?
7°
//31
H-3
(3
A 3^
/3C/
So
85"
US
a>a^
1-3
/.r?
/,39
So
77
9o
ifT-
t.o
l3(?8.65B
f'3
/¦3T
/..?
-------
CUENT»JSj CkccjlfI
TEST UNIT
j)JECTNO. fcgZ^/-
STTk-K-
STACK SAMPLING DATA SHEET
TEST DATE ORIFICE CORRECTION (t H@) A ££>2-
TEST NO.
NOZZLE (SIZE,#) Q.ti$Zrr
METER CORRECTION {¥) P <%?T
CALIBRATION DATE
Pig« / of
HOT/COLD BOX NO. ^
o-&/
PROBE NO.
FILTER NO.
r -n»i
STATIC PRESSURE ^
PITOT CORRECTION
R1C PRESSURE ?&.&} PORT DIRECTION /,)tSr
STACK DIA. 3b
PORT SIZE 4*
CONTROL BOX NO.
[Ltrmtu
I Time
DtyGu
Meter Reading
(del)
Pilot *P,
(in 1120)
Orifice iH
Meter Temperature
Vacuum
('w. h*>
SUck
Temp.
(•F)
Probe
Temp.
(•F)
Tmpiager
Temp.
CF>
Hot Box
Temp.
{•F)
Coittntettfa
1* Point
1 (incites)
Required
(in. 1120)
Actual
(ia. 1120)
In
CP)
Out
CP)
(U?r-o
aaL>lto
/.
Fa
*7
y.o
--25D
4. min. /point
jpz
*.-x7 43D
(.Co
/So
1 tts
a#
fix
i
/7
A6>3
') .(*•*)
*>c
*i.o
'ft-?. 4
/ y
/¦T>
(W
/ o
i.n
tl 1
I
A C
*:>3.V77
a. &
oW
fiC
/To
/o^
^. Ti°
—
Estim»les:
—
MW=2a 8
5H120-J.
SYSTEM LEAK CHECK
PJTOT LEAK CHECK
;
Vtciiuin
(in. Ilj)
DOM Kite
(cfin)
Before
yJTO
f oo^
After
So
f'. o^y
sz.
L
r&ri
Difference
7?*'!
l~
(j&o.J fr>f> j?
^6
oO
<63
-------
377k-£->2W
CLIENT^ Oqa^-1
STACK SAMPLING DATA SHEET
TEST DATE fO-2/-V ORIFICE CORRECTION ( a H®)/, &P2-
Page^S- of 5^
HOT/COLD BOX NO. £2,
TEST UNIT |3-//r ;_
^PROJECT NO. TcDi&j-ol
?&-
TEST NO. <^z- J.-V-3
NOZZLE (SIZE,#)
STATIC PRESSURE j n (J#> q
METER CORRECTION (Y) 0^6/*?
CALIBRATION DATE
"P1TOT CORRECTION O'W
PROBE NO.
F1LTER NO. ///y
i/ '/
TEST CREW
JZ2
STACK P1A.16V/
Traverse
Point
(incite*)
Tirte
Dry 0««
Meter Reading
(del)
Pilot dp
(in. >120)
Orifice All
Mc|cr Temperature
Vacuum
(in. Jig)
Slack
Temp.
<*F)
Probe
Temp.
CF)
Impirtger
Temp.
(¦F)
Hot Box
Temp,
CF)
Comment*
Required
(in. 1120)
Actual
(in. 1120)
In
(•F)
Out
(•F)
/'•
W9.k>7
O &
oaV
o.3.i
??
j£>0
>V25EP
<6©
jZ- min./point
>.;V
n. 3.
o.'2-Y
O .A/
£9.
a ¦ r
/OO
A3V
. or
o-7 f
o.?r
"7<^*~
/. o
¦ /V?
1 . o
/.n
JFV
?y
3. O
^mt
1.1
/.•3/
i-13l
/y
7iT
r
/o6>
IZ--S
<1
A-?0
i.?n
*v
=5 j"
t/O
2-?.1
<¦ o
A/9
/./i
-? ¦
ro
v.o
V-
//5
3/.
¦ iHl
/•3
/„-T3
J.-rt
jfc>
f.o
//c,
35k
i.S
A?Cf
/•76»
/O
V..T
ft*/
^,vo . 3S5
/. 5
f ¦ 7C»
>.76?
Fn
V-5
' ' r
11$
\
¦&11 'IZo
Hslimates:
MW= 2-&S
XH20=
SYSTEM LEAK CHECK
PITOT LEAK CHECK
Vacuum
(ill. Hg)
DOM Rate
(cfra)
Bcfuce
After
Positive
Negative
Before
Alter
Impioger
No.
Impingec
Contents
OAS
CHESTER
tNVBH1NM(NTAL
C02
02
CO
N2
FjmI
luilMii
DifTciMM
1.
2.
3.
4.
S.
6.
7.
1.
-------
CLIENT U& Ufrdt-i
TEST UNfrjf ' & fee
PROJECT NO. ?chlbl-olf
5VTfrdt- 2,-4
STACK SAMPLING DATA SHEET
TEST DATE /q-34>-^7 ORIFICE CORRECTION ( t.
METER CORRECTION (Y) £>,9k«?
CALIBRATION DATE
Pago^r oft?
HOT/COLD BOX NO.
PROBE NO. 5~~g~
FILTER NO.
TEST NO.
NOZZLE (SIZE,*) Q,fb^
STATIC PRESSURE + g.C, V?_ <> PITOT CORRECTION U'3Y
TEST CREW
nf)
STACK DIA. ~bL
Tri*MM
Point
(indict)
Time
Dry Gai
Meter Reading
(Jcl)
Pkot *P
("mi. II20)
Orifkc A H
Mtlti Temperature
Vacuum
Cm. Hg)
St»ck
Temp.
(•F)
Probe
Tejnp,
(•P)
lnpHter
Temp.
<'F)
Hoi Box.
Temp.
Cry
Comment!
Required
(in. 1120)
Actual
(in. H20)
la
c*p)
Out
(*F)
an-ttO
1.5
/. 7C»
tf
ri
*3
f/S
~»P£>
min./poinl
n.(o
tM
f.
if &
1*.-o
&44r.74to
!. !
t-Vf
t.tt
9-7
n
-*.s
II T
tiz
S.Sb5
i-o
uxn
>¦>-)
KLr
!Tr>
nt*
• lr?/
1,0
,.m
i-i 7
JFf
fc>
35
t/fci
/. o
t-i-1
til
r.5
fP
3.r>
//7
/S'V
frft* ¦ 19c.
l.C
itl
t.\l
fT5
To
1. Y
//'/
H.J
ml 3oo
o.^
n ¦ 2^0
a¦ 3^0
To
FO
o.5
///"?
1
ad
*V7- c.Ho
o. "3.
«.pLO
o - 3,0
Xo
?o
Cy S*
/rO
* to
o-2
O frO
o
70
r)<^>
if
!
!•/?• //?
Estimates:
MW-= 8
%1120-^t-
SYSTEM LEAK CHECK
PITOT LEAK CHECK
Vac ihiin
DOM Rule
(in. IIS)
(cfni)
Deface
Aflcr
CHESTER
I NVMMMMfNfAL
Poritive
Negative
Before
After
OAS 1 2
C02
02
CO
N2
IinpMger
No.
lmpingcr
Content i
Finil
Initiil
Difference
1.
2.
J.
4.
5.
6.
7.
1.
-------
CLIENT USS
/$ fff-Midy PfeZ-^
1tsOZLi-G>/
STACK SAMPLING DATA SHEET
TEST PATH /Q-Z/-?3 ORIFICE CORRECTION ( l H@) AS02-
METER CORRECTION (Y) O^Wn
CALIBRATION DATE 5~-t 7-*?3
o'c>/
P»g° jVs:
HOT/COLD DOX NO. Z*
TEST UNIT 13-
PROJECTNO. -JisQZLt^&T
TEST NO. ~ t-V-T
NOZZLE (SIZE,#) O- /gf*"
PROBE NO. 5~"3~
FILTER NO.
TEST CREW
_rZ2&
STATIC PRESSURE
£ • £=»
W
PITOT CORRECTION
STACK DlA/%'
BAROMETRIC PRESSURE PORT DIRECTION /y&.V
CONTROL BOX NO.
PORT SIZE ~W
Xb
740t&
S-j-
//?>
min./point
la?
l-o
/./-7
t. 11
fCn
no
^ :5
>f I
3/.-?
AV•!
/-0/7
i* 1
vf
70
3.jT
U5
nt
5Vf. 7-7/9
..3
/ 5C"
1.3°
?fb
•7(7
-7>.0
/CO
*iS ¦ 37'U
Estimates;
—
MW- 39,8
»H20- tX-
SYSTEM
LEAK CHECK
PITOT LEAK CHECK
Impinger Impinger
Vacuum
(i». iig)
DOM Rule
(efm)
Poakive
Negative
No. ConlcnU Pinal Initial Difference
Before
1.
Dcfore
After
2.
After
OAS 1 2
3.
C02
4.
Zfifc CHESTER
INVMKINMtNlJU.
02
5.
CO
6.
N2
7.
1.
-------
CLIENT Clf 5"
HOT/COLD BOX NO. g
TEST UNIT
METER CORRECTION (Y) Q , 76/7
PROBE NO. 5^5"
PROJECT NO.
FILTER NO.
TEST CREW
STACK DIA.
Traverse
Point
(inches)
Time
Dry Gaa
Meter Reading
(del)
Pilot iP
(in. 1120)
Orifice ill
Meier Temperature
Vacuum
(in. (I|)
Stick
Temp.
(•F)
Probe
Temp.
(-F)
Impiftgcr
Temp.
CF)
llot Box
Temp.
C*F)
Commenl*
Retired
(U. 1120)
Actual
(m. 1120)
Id
(•p)
Out
(*F>
Ao
1XTS7&
A.r
a. If
n.f?
7^.
3J
/oO
—'^5t>
<<^B
«^2
3. o
/o5*
5^6 ?/0
/ . r> "f
i o .*5
7 a
3.J
//o
d-9
/- o J"
/. Ovt
Co
7^
///
fl-f)
t.ou!
/.ny
h
3.o
//3*
2Z*-
a.3ir.?.:rG
/- ^
..fil
/•¦%7
5TV
ods
V. r>
1(0
l3<.&
ra.TV
/b
-?&
:*>. 5
//
y.o
,n
3 17-
fr6>o.7£5
131
V <-
/ / ^
37.
AG!. TO/
/ <3
ht<*
/. >£f
-?v
J?-J*
///,3
,?^o
oof
/.£>
I.I&
!>\c
7*^
9- f
/ /Jf
.9^3 oi&
1let
£ibk-
/Wjk,
(&vL
-as
)
°r
('<*, J
A, -//;
Jdh±
kc&Cj
dfcf
/I*
M3
Hslimiiles:
o.L)
MW- 2-&g
r
*H20- 4-
SYSTEM LEAK CHECK
PITOT LEAK CHECK
Vncmnn
(in Hg)
DOM Rule
(efm)
Define
After
Positive
Negative
Before
After
OAS I 2
Impinger
No.
Impinger
CoulcnU
Final
Initial
Difference
CHESTER
tNVffHIttMENlAl
C02
02
CO
N2
1.
2.
3.
4.
5.
6.
7.
S.
-------
CONTROL BOX CALIBRATION
THREE POINT CALIBRATION
BOX # 3 BP 28.9 in. Hg
DATE 07-02-93 OPERATOR RPC
WET TEST METER
DRY TEST METER
METER
ORIFICE
TIME
(min)
TEMP
TW
VOLUME
VM
PRESSURE
PW
TEMP IN
T1
TEMP OUT
TO
TEMPAVG
TA
ORIFICE
PO
VOLUME
VD
COEFFICIENT
Y
COEFFICIENT
aH@
START
HALF
STOP
11.48
7a o
0.000
5.000
28.90
104.0
92.0
98.0
0.50
74.200
79.348
CALCULATION
11.48
538.0
5.013
28.90
558.0
28.94
5.148
1.0086
1.492
START
HALF
STOP
B.43
78.0
0.000
5.000
28.90
108.0
94.0
101.0
1.00
79.700
84.836
CALCULATION
8.43
538.0
5.013
28.90
561.0
28.97
5.136
1.0151
1.601
START
HALF
STOP
12.05
79.0
0.000
10.000
28.90
117.0
98.0
107.5
2.00
96.600
106.880
CALCULATION
12.05
539.0
10.025
28.90
567.5
29.05
10.280
1.0216
1.623
AVERAGE
1.0151
-------
POST TEST
BOX *
DATE
3
10-22-93
BP
OPERATOR
29.20
RPC
In. Hg
WET TEST METER
DRY TEST METER
METER
ORIFICE
TIME
fm1n)
TEMP
TW
VOLUME
VM
PRESSURE
PW
TEMP IN
T1
TEMP OUT
TO
TEMP AVG
TA
ORIFICE
PO
VOLUME
VD
COEFFICIENT
Y
COEFFICIENT
START
HALF
STOP
8.85
75.0
0.000
5.000
29.20
97.0
93.0
95.0
1.00
538.200
543.400
CALCULATION
8.85
53S.0
5.013
23.20
555.0
29.27
5.200
0.9975
1.745
START
HALF
STOP
6.73
75.0
0.000
5.000
29.20
101.0
96.0
96.5
1.00
543.600
548.711
CALCULATION
8.73
535.0
5.013
29.20
558.5
29.27
5.111
1.0212
1.688
START
HALF
STOP
8.80
75.0
0.000
5.000
29.20
103.0
96.0
99.5
1.00
549.100
554.319
CALCULATION
8.80
535.0
5.013
29.20
559.5
29.27
5.219
1.0019
1.712
AVERAGE
1.0069
1.715
DIFFERENCE
o.a%
-------
PRE-TEST MAGNEHELIC CALIBRATION
BOX# 3
DATE 07-02-93
OPERATOR RPC
OlolO* H20 RANGE
010 0.50' 1120 RANGE
MAGNEHELIC
4 P
MANOMETER
MAGNEHELIC
6 P
MANOMETER
0.50
0.50
0.50
0.50
1.00
1.00
0.40
0.40
2.00
2.00
0-30
0.30
4.00
4.00
0.20
0.20
6.00
6.00
0.10
0.10
8.00
8.00
PRE-TEST LEAK CHECK
DATE
07-02-93
OPERATOR
RPC
START
STOP
VOLUME
TIME
LEAK
CF
CF
CF
(mln)
RATE
DRY
73.610
73.795
0.185
10.000
0.004
WET
0.00O
0.230
0 230
PYROMETER CALIBRATION
PRE-TEST PYROMETER CHECK
DATE
04-28-B8
DATE
07-02-93
OPERATOR
AGL
OPERATOR
RPC
VOLTAGE
ARGE
TEMP
VOLTAGE
TARGET
TEMP
INPUT
TEMP READING
INPUT
TEMP
HEADING
fmV)
CD
en
fmV)
I!D
0.18
40
40.0
0.18
40
40.0
0.40
50
50.0
0.40
50
50.0
Q.B4
70
70.0
0.84
70
70.0
1.29
90
90.0
1.29
90
90.0
1.74
110
110.0
1.74
110
110.0
2.66
150
150.0
2.66
150
150.0
3.B2
200
200.0
3.B2
200
201.0
6.09
300
301.0
6.09
300
300.0
8.31
400
400.0
6.31
400
402.0
10.57
500
500.0
10.57
500
502.0
010 5* H20 RANGE
MAGNEHELIC
aH MANQMETEH
4.00
4.00
3.00
3.00
2.00
2.00
1.00
1.00
0.50
-------
POST-TEST MAGNEHELIC CALIBRATION
BOX# 3
DATE 10-22-93
OPERATOR RPC
0 to TO* H20 RANGE
Oto 0.50* H20 RANGE
MAGNEHELIC
A P
MANOMETER
MAGNEHELIC
a P
MANOMETER
0.50
0.50
0.50
0.49
1.00
1.00
0.40
0.40
2.00
2.00
0.30
0.30
4.00
4.00
0.20
0.20
6.00
6.00
0.10
0.10
8.00
6.00
POST-TEST LEAK CHECK
DATE
10-22-93
OPERATOR
RPC
START
STOP
VOLUME
TIME
LEAK
CF
CF
CF
(mln)
RATE
DRY
536.900
537.075
0.175
10.000
0.0002
WET
0.000
0.177
0.177
PYROMETER CALIBRATION
POST-TEST PYROMETER CHECK
DATE
04-28-68
DATE
10-22-93
OPERATOR
AGL
OPERATOR
RPC
VOLTAGE
ARGE
TEMP
VOLTAGE
TARGET
TEMP
INPUT
TEMP READING
INPUT
TEMP
READING
-------
OA ORIFICE AUDIT
ORIFICE BAPC-3 DATE 10-22-93 B.P. 29.20
OPERATOR RPC BOX» 3
RUN
1
2
3
INITIAL CF
513.500
521.000
528.700
FINAL CF
520.643
528.369
536.096
DIFFERENCE
7.343
7.369
7.396
TN
OUT
IN
OUT
IN
OUT
TEMP INITIAL
84
84
94
B9
98
93
TEMP 5 MIN
91
87
95
90
99
94
TEMP 10 MIN
92
87
97
91
99
95
TEMP 15 MIN
94
89
98
93
99
95
TEMP R
TEMP R
TEMP R
TEMP AVQ
88.5
548.5
93.375
553.375
96.5
556.5
TIME (MIN.)
15.00
15.00
15.00
N WATE
IN HG
IN WATER
IN HG
IN WATER
IN HG
ORIFICE
0.70
0.05
0.70
0.05
0.70
005
METER PRESSURE
29.25
29.25
29.25
°F
•c
•F
•c
•F
•c
AMBIENT TEMP.
80.0
26.7
BOO
26.7
80.0
26.7
VACUUM IN HG
19.5
19.5
19.5
DGM CAL Y
1.0151
1.0151
1.0151
STDCF
7.042
7.004
6.990
STt> CUBIC METERS
0.1994
0.1984
-------
CONTROL BOX CALIBRATION
THHEE POINT CALIBRATION
BOX#
DATE
4
05-19-93
BP
OPERATOR
28.75
RPC
In. Hg
WET TEST METER
DRY TEST METER
METER
ORIFICE
TIME
(min)
TEMP
TW
VOLUME
VM
PRESSURE
PW
TEMP IN
Tl
TEMP OUT
TO
TEMP AVG
TA
ORIFICE
PO
VOLUME
VD
COEFFICIENT
Y
COEFFICIENT
START
HALF
STOP
11.55
61.0
0.000
S.000
28.75
72.0
71.0
71.5
0.50
39.000
44.158
CALCULATION
11-55
521.0
5.013
28.75
531.5
28.79
S.158
0.9901
1.495
START
HALF
STOP
B.92
62.0
0.000
5.000
28.75
75.0
74.0
74.5
1.00
44.500
49.650
CALCULATION
8.92
522.0
5.013
28.75
534.5
28.82
5.150
0.9941
1.700
START
HALF
STOP
6.23
63.0
0.000
5.000
28.75
75.0
73.0
74.0
2.00
50.200
55.347
CALCULATION
6.23
523.0
5.013
28.75
534.0
28.90
5.147
0.9893
1.745
AVERAGE
0.9912
-------
POST TEST
BOX#
DATE
4
10-22-93
BP
OPERATOR
29.20
RPC
In. Hg
WET TEST METER
DRY TEST METER
METER
ORIFICE
TIME
(mln)
TEMP
TW
VOLUME
VM
PRESSURE
PW
TEMPtN
Tl
TEMP OUT
TO
T&1P AVG
TA
ORIFICE
PD
VOLUME
VD
COEFFICIENT
Y
COEFFICIENT
START
HALF
STOP
8.70
75.0
0.000
5.000
29.20
81.0
80.0
80.5
1.00
681.200
686.325
CALCULATION
8.70
535.0
5.013
29.20
540.5
29.27
5.125
0.9856
1.732
START
HALF
STOP
8.76
75.0
0.000
5.000
29.20
84.0
83.0
83.5
1.00
686.500
691.660
CALCULATION
8.76
535.0
5.013
29.20
543.5
29.27
5-160
0.9844
1.746
START
HALF
STOP
8.61
75.0
0.000
5.000
29.20
86.0
84.0
85.0
1.00
692.000
697.200
CALCULATION
8.81
535.0
5.013
29.20
545.0
29.27
5.200
0.9795
1.761
AVERAGE
0.9&32
1.746
DIFFERENCE
0.8%
-------
PRE-TEST MAGNEHELIC CALIBRATION
BOX* 4
DATE 05-19-93
OPERATOR RPC
010 10* H20 RANGE
0 10 0.50* H20 RANGE
MAGNEHELIC
P
MANOMETER
MAGNEHELIC
P
MANOMETER
0.50
0.50
0.50
0.50
1.00
1.00
0.40
0.40
2.00
2.00
0.30
0.30
4.00
4.00
0.20
O.Z0
6.00
6.00
0.10
0.10
8.00
8.00
PRE-TEST LEAK CHECK
DATE
05-19-93
OPERATOR
RPC
START
STOP
VOLUME
TIME
LEAK
CF
CF
CF
(mln)
RATE
DRV
38.500
38.701
0.201
10.000
-0.002
WET
0.000
0.181
0.101
PYROMETER CALIBRATION
PRE-TEST PYROMETER CHECK
DATE
04-28-88
DATE
05-19-93
OPERATOR
AGL
OPERATOR
RPC
VOLTAGE
ARGE
TEMP
VOLTAGE
TARGET
TEMP
INPUT
TEMP READING
INPUT
TEMP
READING
(mV)
CD
(!D
On VI
(!D
CD
0.18
40
40. G
0.18
40
40.0
0.40
50
50.0
0.40
SO
51.0
0.64
70
70.0
0.84
70
71.0
5.29
90
90.0
1.29
90
91.0
1.74
110
110.0
1.74
110
110.0
2.66
150
150.0
2.66
150
151.0
3.82
200
200.0
3.82
200
201.0
6.09
300
301.0
6.09
300
302.0
8.31
400
400.0
8.31
400
402.0
10.57
500
500.0
10.57
500
502.0
010 5* H20 RANGE
MAGNEHELIC
iH
4.00
3.00
2.00
1.00
0.50
MANOMETER
4.00
3.00
2.00
1.00
-------
POST-TEST MAGNEHELIC CALIBRATION
BOX#
4
DATE
10-22-93
OPERATOR
RFC
Oto 10* H20 RANGE
Oto0.50* H20 RANGE
MAGNEHELIC
MAGNEHELIC
A P
MANOMETER
a P
MANOMETER
0.50
0.50
0.50
0.50
1.00
1.00
0.40
0.40
2.00
2.00
0.30
0.30
4.00
4 00
0.20
0.20
6.00
6.00
0.10
0,10
8.00
fl.OO
POST TEST LEAK CHECK
DATE
10-22-93
OPERATOR
RPC
START
STOP
VOLUME
TIME
LEAK
CF
CF
CF
(mln)
RATE
DRY 680.020
680.230
0.210
10.000
-0.0010
WET 0.000
0.200
0.200
PYROMETER CALIBRATION
POST-TEST PYROMETER CHECK
DATE
04-28-88
DATE
10-22-93
OPERATOR
AGL
OPERATOR
RPC
VOLTAGE
ARGE TEMP
VOLTAGE
TARGET
TEMP
INPUT
TEMP READttIG
INPUT
TEMP
READING
(mV)
CD 1!D
-------
OA ORIFICE AUDIT
ORIFICE BAPC-3 DATE 10-22-93 B.P. 29.20
OPERATOR RPC BOX # 4
RUN
1
2
3
INITIAL CF
697.800
705.500
713.400
FINAL CF
705.176
712.956
720.901
DIFFERENCE
7.376
7.456
7.501
IN
OUT
1N
OUT
IN
OUT
TEMP INITIAL
87
87
91
89
99
94
TEMP 5 MIN
90
88
98
93
100
94
TEMP 10 MIN
90
87
98
94
100
94
TEMP 15 MIN
91
89
99
94
101
94
TEMP R
TEMP R
TEMP H
TEMPAVG
88.625
548.625
94.5
554.5
97
557
TIME (MIN.)
15.00
15.00
15.00
N WATE
IN HG
IN WATER
IN HG
IN WATER
IN HG
ORIFICE
0.75
0.06
0.75
0.06
0.75
0.06
METER PRESSURE
29.26
29.26
29.26
"F
"C
"F
°C
•F
•C
AMBIENT TEMP.
80.0
26.7
80.0
26.7
80.0
26.7
VACUUM IN HQ
18.5
18.5
18.5
DGMCAL Y
0.9912
0.9912
0.9912
STDCF
6.906
6.907
6.917
STD CUBIC METERS
0.1956
0.1956
-------
CONTROL BOX CALIBRATION
Tl 1REE POINT CALIBRATION
BOX# 5 BP 20.95 In. Hg
DATE 05-17-93 OPERATOR RPC
WET TEST METER
DRY TEST METER
METER
ORIFICE
TIME
(mid)
TEMP
TW
VOLUME
VM
PRESSURE
PW
TEMP IN
Tl
TEMP OUT
TO
TEMP AVG
TA
ORIFICE
PD
VOLUME
VD
COEFFICIENT
Y
COEFFICIENT
aH@
START
HALF
STOP
12.75
63.0
0.000
5.000
28.95
93.0
83.0
ea.o
0.50
248.800
254.195
CALCULATION
12.75
523.0
5.013
23.95
548.0
28.99
5.395
0.9723
1.766
START
HALF
STOP
8.90
64.0
0.000
5.000
2a.9$
96.0
84.0
90.0
1.00
254.700
259.988
CALCULATION
8.90
524.0
5.013
26.95
550.0
29.02
5.288
0.9924
1.723
START
HALF
STOP
6.25
66.0
0.000
5.000
28.95
96.0
85.0
90.5
2.00
261.600
266.900
CALCULATION
6.25
526.0
5.013
28.95
550.5
29.10
5.300
0.9848
1.711
AVERAGE
0.9832
-------
POSTTEST
BOX #
DATE
5
10-22-93
BR
OPERATOR
29.05
RPC
In. Hg
WET TEST METER
DRY TEST METER
METER
ORIFICE
TIME
(mln)
TEMP
TW
VOLUME
VM
PRESSURE
PW
TEMP IN
Tl
TEMP OUT
TO
TEMPAVG
TA
ORIFICE
PD
VOLUME
YD
COEFFICIENT
Y
COEFFICIENT
*H@
START
HALF
STOP
7.50
75.0
0.000
5.000
29.05
100.0
86.0
93.0
1.45
930.300
935.630
CALCULATION
7.50
535.0
5.013
29.05
553.0
29.16
5.330
0.9685
1.633
START
HALF
STOP
7.42
75.0
0,000
5.000
29.05
104.0
89.0
96.5
1.45
937.000
943.102
CALCULATION
7.42
535.0
5.013
29.05
556.5
29.16
5.302
0.9798
1.783
START
HALF
STOP
7.35
75.0
0.000
5.000
29.05
102.0
93.0
97.5
1.45
943.600
949.001
CALCULATION
7.35
535.0
5.013
29.05
557.5
29.16
S.401
0.9636
1.747
AVERAGE
0.9706
1.786
DIFFERENCE
1.3W
-------
PRE-TEST MAGNEHELIC CALIBRATION
BOX#
5
DATE
05-17-93
OPERATOR
RPC
Olo 10* H20 RANGE
0 to 0.50* H20 RANGE
MAGNEHELIC
MAGNEHELIC
A P
MANOMETER
a P MANOMETER
0.50
0.50
0.50
1.00
1.00
0.40
2.00
2.00
0.30
4.00
4.00
0.20
6.00
6.00
0.10
8.00
8.00
Calibration no! necessary.
Primary standard on conlrgl box.
PRE-TEST LEAK CHECK
DATE
05-17-93
OPERATOR
RPC
START
STOP
VOLUME TIME
LEAK
CP
CF
CF (min)
RATE
DRY 248.305
248.500
0.195 10.000
0.001
WET 0-000
0.200
0.200
PYROMETER CALIBRATION
PRE-TEST PYROMETER CHECK
DATE
04-28-88
DATE 05-17-93
OPERATOR
AGL
OPERATOR RPC
VOLTAGE
ARGE TEMP
VOLTAGE TARGET
TEMP
INPUT
TEMP READING
INPUT TEMP
READING
ImV)
I!Q
ItnV) (*R
i!D
0.18
40 40.0
0.18 40
40.0
0 40
50 50.0
0.40 50
50.0
0.84
70 70.0
0.84 70
70.0
1.29
90 90.0
1.29 90
90.0
1.74
110 110.0
1.74 110
110.0
2.66
150 150.0
2.66 150
150.0
3.62
200 200.0
3.82 200
201.0
6.09
300 301.0
6.09 300
301.0
8-31
400 400.0
8.31 400
403.0
10.57
500 500.0
10.57 500
503.0
OloS* H20 RANGE
MAGNEHELIC
MANOMETER
4.00
4.01
3.00
3.01
2.00
2.00
1.00
1.00
0.50
-------
POST-TEST MAGNEHELIC CALIBRATION
BOX# 5
OATE 10-25-93
OPERATOR RPC
0(0 10* H20 RANGE
010 0.50" H20 RANGE
MAGNEHELIC
* R
O.50
1.00
2.00
4.00
6.00
8.00
MAGNEHELIC
MANOMETER a P MANOMETER
0.50 0.60
1.00 0.40
2.00 0.30
4.00 0.20
6.00 0.10
B.00 Calibration not necessary.
Primary standard on control box.
POST-TEST LEAK CHECK
DATE 10-25-93
OPERATOR RPC
START
CF
STOP
CF
VOLUME
CF
TIME
(mln)
LEAK
RATE
DRY
929.281
929.500
0.219
10.000
0.0011
WET
0.000
0.230
0.230
PYROMETER CALIBRATION
POST-TEST PYROMETER CHECK
DATE
04-28-
CO
CD
DATE
10-25-93
OPERATOR
AGL
OPERATOR
RPC
VOLTAGE
ARGE
TEMP
VOLTAGE
TARGET
TEMP
INPUT
TEMP READING
INPUT
TEMP
READING
-------
OA ORIFICE AUDIT
ORIFICE BAPC-3
DATE
10-25-93
BP.
29.05
OPERATOR RPC
BOX#
5
RUN
1
2
3
INmAL CF
949.300
957.200
965.100
FINAL CF
957.000
964.900
972.790
DIFFERENCE
7.700
7.700
7.690
IN
OUT
IN
OUT
IN
sm
TEMP INITIAL
97
94
93
92
93
91
TEMP 5 MIN
94
93
93
91
93
91
TEMP 10MIN
94
93
93
91
93
91
TEMP 15 MIN
92
92
93
91
95
91
TEMP R
TEMP R
TEMP R
TEMP AVG
93-625
553.625
92.125
552.125
92.25
652.25
TIME (MIN.)
15.00
15.00
15.00
N WATE
IN HG
IN WATER
IN HG
IN WATER
IN HG
ORIFICE
0.75
0.06
0.75
0.06
0.75
0.06
METER PRESSURE
29.11
29.11
29.11
"F
•C
•F
¦c
•F
•c
AMBIENT TEMP.
eo.o
26.7
BOO
26.7
80.0
26.7
VACUUM IN HG
19.5
19.5
19.5
DGMCALY
0.9832
0.9832
0.9832
STDCF
7.050
7.069
7.059
STD CUBIC METERS
0.1997
0.2002
-------
CONTROL BOX CALIBRATION
THREE POINT CALIBRATION
BOX# 7 BP 28.95 In. Hg
DATE 05-17-93 OPERATOR RPC
WET TEST METER
DRV TEST METER
METER
ORIFICE
TIME
(mfn)
TEMP
TW
VOLUME
VM
PRESSURE
PW
TEMP IN
Tl
TEMP OUT
TO
TEMP AVG
TA
ORIFICE
PD
VOLUME
VD
COEFFICIENT
Y
COEFFICIENT
*H$
START
HALF
STOP
12.70
72
0.000
5.000
28.95
104
78
91
0.50
39.300
44.700
CALCULATION
12.70
532
5.013
28.95
551
28.99
5.400
0.9602
1.805
START
HALF
STOP
9.00
73
0.000
5.000
28.95
107
81
94
1.00
45.200
50.606
CALCULATION
9.00
533
5.013
28.95
554
29.02
5.406
0.9613
1.810
START
HALF
STOP
6.33
74
0.000
5.000
28.95
110
83
97
2.00
51.800
57.190
CALCULATION
6.33
534
5.013
28.95
557
29.10
5.390
0.9642
1.790
AVERAGE
0.9619
-------
POSTTEST
BOX#
DATE
7
10-22-93
BP
OPERATOFI
29.20
RPC
In. Kg
WET TEST METER
DRY TEST METER
METER
ORIFICE
TIME
(min)
TEMP
TW
VOLUME
VM
PRESSURE
PW
TEMP IN
Tl
TEMP OUT
TO
TEMP AVG
TA
ORIFICE
PD
VOLUME
VD
COEFFICIENT
Y
COEFFICIENT
START
HALF
STOP
8.00
75
0.000
5.000
29.20
100
83
92
1.25
339.800
345.090
CALCULATION
8.00
535
5.013
29.20
552
29.29
5.290
0.9737
1.794
START
HALF
STOP
6.10
75
0.000
5.000
29.20
101
84
93
1.25
345.300
350.600
CALCULATION
e.io
535
5.013
29.20
553
29.29
5.300
0.9736
1.836
START
HALF
STOP
6.13
75
0.000
5.000
29.20
110
85
98
1.25
350.900
356.203
CALCULATION
8.13
535
5.013
29.20
558
29.29
5.303
0.9619
1.833
AVERAGE
0.9764
1.821
DIFFERENCE
-1.5"»l
-------
PRE-TEST MAGNEHELIC CALIBRATION
BOX# 7
DATE 05-17-93
OPERATOR RPC
Olo 10-H20RANGE
0 to 0.50* H20 RANGE
MAGNEHEUC
MAGNEHELIC
t P
MANOMETER
t P MANOMETER
0.50
0.50
0.50
1.00
1.00
0.40
2.00
2.00
0.30
4.00
4.00
0.20
6.00
6.00
0.10
8.00
8.00
Calibration not necessary.
PRE-TEST LEAK CHECK
DATE 05-17-93
OPERATOR RPC
Primary standard on control box.
START
STOP
VOLUME
TIME
LEAK
CF
CF
CF
(min)
RATE
DRY
38.650
38.878
0.228
10.000
-0.003
WET
0.000
0.202
0.202
PYROMETER CALIBRATION
PRE-TEST PYROMETER CHECK
DATE
04-28-88
DATE
05-17-93
OPERATOR
AGL
OPERATOR
RPC
VOLTAGE
ARGE
TEMP
VOLTAGE
TARGET
TEMP
INPUT
TEMP READING
INPUT
TEMP
READING
ftnY)
CD
CD
ftnV)
CO
(!D
0.16
40
4O.0
0.18
40
41.0
0.40
50
£0.0
0.40
50
50.0
0.64
70
70.0
0.84
70
70.0
1.29
90
90.0
1.29
90
90.0
1.74
1(0
110.0
1.74
110
110.0
2.66
150
150.0
2.66
150
150-0
3.82
200
200.0
3.B2
200
200.0
6.09
300
301.0
6.09
300
299.0
6.31
400
400.0
6.31
400
399.0
10.57
500
500.0
10.57
SOO
496.0
Olo 3* H20 RANGE
MAGNEHEUC
iH
3.00
2.00
1.00
0.50
MANOMETER
3.00
2.00
1.00
-------
POST-TEST MAGNEHELIC CALIBRATION
BOX# 7
DATE 10-22-93
OPERATOR RPC
010 10' H20 RANGE
, 0 to 0.60" H20 RANGE
MAGNEHELIC
4 P
MANOMETER
MAGNEHELIC
* P
MANOMETER
0.50
0.50
0.50
1.00
1.00
0.40
2.00
2.00
0.30
4.00
4.00
0.20
...
6.00
6.00
0.10
—
8.00
8.00
Calibration no4 necessity.
Primary standard on control box.
POST-TEST LEAK CHECK
DATE
10-22-
93
OPERATOR
RPC
START
STOP
VOLUME
TIME
LEAK
CF
CF
CF
(mln)
RATE
DRY
338.001
336.200
0.199
10.000
-0.0004
WET
0.000
0.195
0.195
PYROMETER CALIBRATION
POST-TEST PYROMETER CHECK
DATE
04-28-88
DATE
10-22-93
OPERATOR
AGL
OPERATOR
RPC
VOLTAGE
ARGE
TEMP
VOLTAGE
TARGET
TEMP
INPUT
TEMP READING
INPUT
TEMP
READING
(mV)
Cf)
(mVl
CD
1!Q
0.18
40
40.0
0.16
40
40.0
0.40
50
50.0
0.40
50
50.0
0.84
70
70.0
0.84
70
70.0
1.29
90
90.0
1.29
90
90.0
1.74
110
110.0
1.74
110
110.0
2.66
150
150.0
2.66
150
150.0
3.82
200
200.0
3.02
200
200.0
6.09
300
301.0
6.09
300
300.0
&31
400
400.0
8.31
400
400.0
10.57
500
500.0
10.57
500
502.0
~ to 3* H20 RANGE
MAGNEHELIC
»H
3.00
2.00
1.00
0.50
MANOMETER
3.00
2.00
1.00
-------
OA ORIFICE AUDIT
ORIFICE BAPC-
3
DATE
11-22-93
BP.
29.20
OPERATOn RFC
BOX#
7
RUN
1
2
3
INITIAL CF
445.800
453.700
461.600
FINAL CF
453.420
461.370
469.224
DIFFERENCE
7.620
7.670
7.624
!N
OUT
IN
OUT
IN
OUT
TEMP INITIAL
80
70
81
71
62
73
TEMP 5 MIN
80
70
82
73
83
75
TEMP 10 MIN
61
71
82
73
84
75
TEMP 15 MIN
61
71
82
73
84
75
TEMP R
TEMP R
TEMP R
TEMP AVG
76
536
77
537
79
539
TIME (MIN.)
15 00
15.00
15.00
N WATE
IN HG
IN WATER
IN HG
IN WATER
IN HG
ORIFICE
0.70
0.05
0.70
0.05
0.70
0.05
METER PRESSURE
29.25
29.25
29.25
•F
•c
•F
•c
'F
•c
AMBIENT TEMP.
75
24
75
24
75
24
VACUUM IN HG
21.0
21.0
21.0
DGM CALY
0.9619
0.9619
0.9619
STDCF
7.092
7.117
7.062
STD CUBIC METERS
0.2009
0.2018
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[A-U]
ARCO Chemical Co.
John Evans Phone: 713-860-4054
Environmental Manager
2502 Sheldon Rd
Channel View, TX 77530
ID/Status : High
Cabot Industries
Tony James Phone: 617
V P. S.H. & E.
75 State St
Boston, MA 02109-1806
ID/Status: High
Fieldcrest Cannon
Barbara Siffard Phone: 704-939-2654
Env. Manager Fax:704-939-2714
P.O.Box 107
Kannapolis, NC 28081
ID/Status : High
Pacific Environmental Services
Richard E Wilkins Phone: 919 941 -0333
5001 S Miami Blvd. Ste 300
PO Box 12077
RTP, NC 27709-2077
U S Steel
Luigi DiLanni Phone: 412-433-5922
600 Grant St
Pittsburgh, PA 15219-2749
ID/Status: Medium
United Technology-Automotive
Paul Dinardo Phone:313-237-4992
Env. Manager
1641 Porter St
Detroit, Ml 48216
j
ID/Status: Medium
Last Contact: 1 /26
Printed on 1/30/95
Printed with ACT' for Window
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-------
COMPLIANCE DEMONSTRATION
NO. 13, 14, IS BATTERY
PUSHING EMISSIONS CONTROL
USS CLAIRTON WORKS
CLAIRTON, PENNSYLVANIA
APPENDIX C
GRAVIMETRIC AND ANALYTICAL RESULTS, EMISSIONS
-------
KEYSTONE ENVIRONMENTAL RESOURCES
AIR QUALITY ENGINEBR1NG
ANALYTICAL REPORTING FORM
Page / of /
CLIENT
PLANT LOCATION"
PROJECT NUMBER"
UNIT TESTED ~
Us3 -
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TEST DATE
"DATE RECEIVED
DATE ANALYZED
" ANALYTICAL METHOD
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Number
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Number
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Units
Filter
Weight
Units a«>)
Soluble
Portion of
Front Half
H20 Rinse
Units
Soluble
Portion of
Front Half
Acetone Rinse
Units )
Soluble
Portion of
Back Half
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Units feyA**}
Soluble
Portion of
Back Half
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Units
0.22pm Filter
Insoluble
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-------
STACK SAMPLING CALCULATIONS
CLIENT: USS CLAIRTON WORKS TEST DATE: 10-19-93
TEST SITE 13.14.15 BATTERY PEC - STACK 2-1 TEST NUMBER: CLR-2-1-1
A. Barometric Pressure 29.45 in. Hg
B. Static Pressure 0 90 in. H20
C. Stack Pressure 29.52 in. Hg (A+(B/13.6)]
D. Average aH 1.86 H20
E. Meter Pressure 29.59 in. Hg [A+(D/13.6)J
F. Average aP 1.60 in. H20
G. Pilot Coefficient 0-84
H. Gas Meter Coefficient 0 9912
I. Stack Diameter 36 in.
j. Stack Area 7^ ft' (0.00545*P)
K. Nozzle Diameter 0-190 in.
L. Nozzle Area 1.97E-04 ft* (0.00545*Ka)
M. Average Stack Temperature 118 *F
N. Average Stack Temperature 578 °R (460+M)
O. Average Meter Temperature 70 °F
P. Average Meter Temperature 530 °R (460+0)
Q. Condensate Volume 11.8 mL
R. Absorbed H20 7.7 mL
S. Total H20 19.5 mL (Q+R)
T. Filter Weight 0.0017 g
U. Probe Weight 0.0034 g
V. Impinger Weight 0.0001 g
W. Total Weight 0.0052 g (T + U + V)
X. Metered Gas Volume 46.978 def
Y. Corrected Metered Gas Volume 46.565 def (X*H)
Z. H20 Gas Volume 0.937 cf (0.00267*S*P/A)
AA. Total Sample Volume 47.502 cf (Y + Z)
BB. Percent H20 2£_ % (100*Z/AA)
CC. Gas Volume Sampled 45.872 dscf [Y*(528/P)*(E/29.92)]
DD. Grain Loading 0.0017 gr/dscf (!5.43*W/CC)
EE. Average Molecular Weight:
Component
% Volume
+ 100
•(l-BB/100)
* Mol.
Weight
= Weigbt/Mol
H20
0,020
18
0.355
C02
0.000
0.980
44
0.000
CO
0.000
0.980
28
0.000
02
0.205
0.980
32
6.431
N2
0.795
0.980
28
21.821
Average Molecular Weight
FF. Average Stack Velocity
GG. A verge Flow Rate
HH. Standard Flow Rate
D. Sample Time
JJ. Percent Isokinetic
KK. Mass Flow Rate
28.61
3600 sec
97.6 %
lb./lb. mol
75.2 fps {85.49*G*[(F*N)/(C*EE)JA0.5}
31900 acfm (60*FF*J)
28700 scfm [GG*(528/N)*(C/29.92)J
{1100*CC*60*J]/[HH*L*II*(1-BB/100))}
-------
STACK SAMPLING CALCULATIONS
CLIENT: USS CLAIRTON WORKS TEST DATE: 10-19-93
TEST SITE 13.14J5 BATTERY PEC - STACK 2-2 TEST NUMBER: CLR-2-2-1
A. Barometric Pressure 29.45 in. Hg
8. Static Pressure 0-20 in. H20
C. Stack Pressure 29.46 in. Hg [A+{B/I3.6>]
D. Average aH 1.76 in. H2Q
E. Meter Pressure 29.58 in. Hg [A+(D/13.6)]
F. Average aP 1.50 in. H2Q
G. Pilot Coefficient £j4
H. Gas Meter Coefficient 1-0151
I. Stack Diameter 36 in.
I. Slack Area 7£7_Aa (0.00545*1*)
K. Nozzle Diameter 0.192 in.
L. Nozzle Area 2.01E-0* fta (0.00545»Ka)
M. Average Stack Temperature 122 °F
N. Average Slack Temperature 582 *R (460+M)
O. Average Meter Temperature 78 °F
P. Average Meter Temperature 538 "R (460+0)
Q. Condensate Volume 11.1 mL
R. Absorbed H20 8.4 mL
S. Total H20 19.5 mL (Q+R)
T. Filter Weight 0.0033 g
U. Probe Weight 0.0074 g
V. Impinger Weight 0.0003 g
W. Total Weight 0.0110 g (T+U + V)
X. Metered Gas Volume 47.497 def
Y. Corrected Metered Gas Volume 48.214 def (X*H)
Z. H20 Gas Volume 0.951 cf (0.00267*S*P/A)
AA. Total Sample Volume 49.165 cf (Y +Z)
BB. Percent H20 1.9 % (100»Z/AA)
CC. Gai Volume Sampled 46.779 dscf [Y^S/P^CE^^)]
DD. Grain Loading 0.0036 gr/dscf (15.43*W/CC)
EE. Average Molecular Weight: ____
Component
% Volume
+ 100
•(I-BB/100)
•Mol.
Weight
= Weight/Mol
H20
0.019
18
0.348
C02
0.000
0.981
44
0.000
CO
0.000
0.981
28
0.000
02
0.205
0.981
32
6.433
N2
0.795
0.981
28
21.829
Average Molecular Weight
FF. Average Stack Velocity
GG. Averge Flow Rate
HH. Standard Flow Rate
D. Sample Time
JJ. Percent Isokinetic
KK. Mass Flow Rate
28.61
3600 see
lb./lb. mol
73.1 fps {85.49*G*f(F*N)/(C*EE)]A0.5}
31000 acfm (60*FF*J)
27700 scfra [GG»(528/N)*(C/29.92)]
100.9 % {[lOO*CC*60*jy[HH*L*Il*(l-BB/100)]}
-------
STACK SAMPLING CALCULATIONS
CLIENT: USS CLAIRTON WORKS TEST DATE: 10-19-93
TEST SITE 13.14,15 BATTERY PEC - STACK 2-3 TEST NUMBER: CLR-2-3-1
A. Barometric Pressure 29.45 in. Hg
B. Static Pressure 1.00 in. H2Q
C. Stack Pressure 29.52 in. Hg [A+(B/13.6)]
D. Average aH 1.40 in. H20
E. Meter Pressure 29.55 in. Hg [A+(D/13.6)]
F. Average aP 1.3 in. H2Q
G. Pitot Coefficient 0.84
H. Gas Meter Coefficient 0-9832
I. Stack Diameter 36 in.
J. Stack Area 7.07 ft2 <0.00545*P)
K. Nozzle Diameter 0.183 in.
L. Nozzle Area 1.83E-04 ft' <0.00545*K2)
M. Average Stack Temperature 117 °F
N. Average Stack Temperature 577 *R (460+M)
O, Average Meter Temperature 76 °F
P. Average Meter Temperature 536 *R (460+0)
Q. Condensate Volume 9.8 mL
R. Absorbed H20 6.0 mL
S. Total H20 15.8 mL
-------
STACK SAMPLING CALCULATIONS
CLIENT: USS CLAIRTON WORKS TEST DATE: 10-19-93
TEST SITE 13.14.15 BATTERY PEC - STACK 2-4 TEST NUMBER: CLR-2^t-l
A. Barometric Preasure 29.45 in. Hg
B. Static Pressure 0.60 In. H20
C. Stack Pressure 29.49 in. Hg (A + (B/13.6)]
D. Average &H 1.42 in. H2Q
E. Meter Pressure 29.55 in. Hg [A+(D/13.6>]
F. Average aP 1.2 in. H2Q
G. Pitot Coefficient 0.84
H. Ga« Meter Coefficient 0.9619
I. Stack Diameter 36 in.
J. Stack Area 7.07 ft* (0.00545*!1)
K. Nozzle Diameter 0.185 in.
L. Nozzle Area 1.87E-04 ft* (0.0Q545*KS)
M. Average Stack Temperature 111 *F
N. Average Stack Temperature 571 °R (460+M)
O. Average Meter Temperature 80 °F
P. Average Meter Temperature 540 *R (460 + 0)
Q. Condensate Volume 8.1 mL
R. Absorbed H20 6.8 mL
S. Total H20 14.9 mL (Q+R)
T. Filter Weight 0.0032 g
U. Probe Weight 0.0147 g
V, Irnpinger Weight 0.0001 g
W. Total Weight 0.0180 "g (T+U + V)
X. Metered Gas Volume 38.309 def
Y. Corrected Metered Gas Volume 36.849 def (X*H)
Z. H20 Gas Volume 0.729 cf (0.00267*S*P/A)
AA. Total Sample Volume 37.579 cf (Y+Z)
BB. Percent H20 L9_ % (100*Z/AA)
CC. Gas Volume Sampled 35.590 dscf [Y*(528/P)*(E/29.92)]
DD. Grain Loading 0.0078 gr/dscf (15.43*W/CC)
EE. Average Molecular Weight:
Component
% Volume
+ 100
•(I-BB/100)
* Mol.
Weight
= Weight/Mol
H20
0.019
18
0.349
C02
0.000
0.981
44
0.000
CO
0.000
0.981
28
0.000
02
0.205
0.981
32
6.433
N2
0.795
0.981
28
21.328
Average Molecular Weight
FF. Average Stack Velocity
GG. A verge Flow Rate
HH. Standard Flow Rate
II. Sample Time
JJ. Percent Isokinetic
KK. Mass Flow Rate
28.61
3600 sec
91.6 %
lb ./lb. mol
64.7 fps {85.49*G*[(F*N)/(C*EE)]A0.5}
27400 acfm (60*FF*J)
25000 scfm [GG«(528/N)*(C/29.92)J
{[100*CC*60#J]/[HH*L*IP(1-BB/100)]}
-------
STACK SAMPLING CALCULATIONS
CLIENT: USS CLAIRTON WORKS TEST DATE: 10-20-93
TEST SITE 13.14.1S BATTERY PEC - STACK 2-1 TEST NUMBER: CLR-2-1-2
A. Barometric Pressure 29.40 in. Hg
B. Static Pressure 1.00 in. H20
C. Stack Pressure 29.47 in. Hg [A+(B/13.6)]
D. Average &H 189 in. H20
E. Meter Pressure 29.54 in. Hg [A+(D/13.6>]
F. Average a P 1-6 in. HIP
G. Pitot Coefficient 0-84
H. Gas Meter Coefficient 0.9912
I. Stack Diameter 36 in.
J. Stack Area 7.07 ft' (0.00545*1')
K. Nozzle Diameter 0.190 in.
L. Nozzle Arc. 1.97E-04 ft' (0.00545'K')
M. Average Stack Temperature 116 "F
N. Average Stack Temperature 576 "R (460+M)
O- Average Meter Temperature 71 °F
P. Average Meter Temperature 531 °R (460+0)
Q Condensate Volume 15.9 mL
R. Absorbed H20 8.0 mL
S. Total H20 23.9 mL (Q+R)
T. Filter Weight 0.0015 g
U. Probe Weight 0.0022 g
V. Impinger Weight 0.0001 g
W. Total Weight 0-0038 g (T+U + V)
X. Metered Gas Volume 47.443 def
Y. Corrected Metered Gas Volume 47.026 def (X*H)
Z. H20 Gas Volume 1.153 cf (0.00267»S»P/A)
AA. Total Sample Volume 48.178 cf (Y+Z)
BB. Percent H20 1A_% (100*Z/AA)
CC. Gas Volume Sampled 46.164 dscf [Y*(528/P)»(EA29.92)]
DD. Grain Loading 0.0013 gr/dscf (15.43»W/CC)
EE. Average Molecular Weighty
Component
% Volume
+ 100
•(l-BB/100)
~ Mol.
Weight
= Weight/Mol
H20
0.024
I '
18
0.431
C02
0.000
0.976
44
0.000
CO
0.000
0.976
28
0.000
02
0.205
0.976
32
6.403
N2
0.795
0.976
28
21.727
Average Molecular Weight
FF. Average Stack Velocity
GG. Avcrge Flow Rate
HH. Standard Flow Rate
n. Sample Time
II. Percent Isokinetic
KK Mass Flow Rate
28.56
3600 sec
98.3 %
lb./lb. raol
75.1 fps {85.49*a*((F»N)/(C»EE)]*0.5}
31900 acfm (60»FF«J)
28800 icfm [GG*(528W)«(C/29.92)]
{(100*CC*60*J]/[HH*L*U*(l-BB/100)]J
-------
STACK SAMPLING CALCULATIONS
CLIENT: USS CLAIRTON WORKS TEST DATE: 10-2Q-93
TEST SITE 13.14.15 BATTERY PEC - STACK 2-2 TEST NUMBER: Cl^-2-^2
A. Barometric Pressure 29.40 in. Hg
B. Static Preuure 100 H20
C. Stack Pressure 29.47 in. Hg [A+(B/13.6)]
D. Average aH 1.77 in. H2Q
E. Meter Pressure 29.53 in. Hg IA+(D/13.6))
F. Average aP 1.50 in. H20
G. Pilot Coefficient 0 84
H. Gas Meter Coefficient 1-0151
I. Stack Diameter 36 in.
J, Stack Area 7.07 ft3 (0.00545*!1)
K. Nozzle Diameter 0.192 in.
L. Nozzle Area 2.01E-04 ft' (0.00545*K*)
M. Average Stack Temperature 124 °F
N. Average Stack Temperature 584 °R (460+M)
O. Average Meter Temperature 80 °F
P. Average Meter Temperature 540 WR (460+0)
Q. Condensate Volume 15.1 mL
R. Absorbed H20 8.8 mL
S. Total H20 23.9 mL (Q+R)
T. Filter Weight O.OQ32 g
U. Probe Weight 0.0029 g
V. Impinger Weight 0.0002 g
W. Total Weight 0.0063 g (*T+U+V)
X. Metered Gas Volume 48.009 def
Y. Corrected Metered Gas Volume 48.734 def (X*H)
Z. H20 Gas Volume L172 cf (0.00267*S*P/A)
AA. Total Sample Volume 49.906 cf (Y+Z)
BB. Percent H20 2.3 % (100*Z/AA)
CC. Gas Volume Sampled 47.030 dscf lY*(528/P)*(E/29.92)]
DD. Grain Loading 0.0021 gr/dscf (15.43*W/CC)
EE. Average Molecular Weight:
Component
X Volume
+ 100
•(l-BB/100)
~ Mol.
Weight
= Wcight/Mol
H20
0.023
18
0.423
C02
0.000
0.977
44
0.000
CO
0.000
0.977
28
0.000
02
0.205
0.977
32
6.406
N2
0.795
0.977
28
21.737
Average Molecular Weight
FF. Average Stack Velocity
GG. Averge Flow Rate
HH. Standard Flow Rate
II. Sample Time
JJ. Percent Isokinetic
KK. Mass Flow Rate
28.57
3600
101.9 %
lb./lb. mol
73.2 fpn {85.49*G+[(F*N)/(C*EE)]*0.5}
31100 acfm (60*FF*J)
27700 scfm [GC*(S28/N)*(C/29.92)]
{[ 100*CC*60*J]/[HH *L*II*(1 -BB/100)]}
-------
STACK SAMPLING CALCULATIONS
CLIENT: USS CLAIRTON WORKS TEST DATE: 10-20-93
TEST SITE 13.14,15 BATTERY PEC - STACK 2-3 TEST NUMBER: CLR-2-3-2
A. Barometric Pressure 29.40 in. Hg
B. Static Pressure 1.00 in. H20
C. Stack Pressure 29.47 in. Hg [A+(B/13.6)J
D. Average aH 1.38 in. H20
E. Meter Pressure 29.50 "in. Hg [A+(D/13.6)J
F. Average aP 1.3 in. H2Q
G. Pilot Coefficient 0.84
H. Gas Meter Coefficient 0.9832
I. Stack Diameter 36 in.
J. StackArea 7.07 ft* (0.00545*1*)
K. Nozzle Diameter 0.183 in.
L. Nozzle Area 1.83E-04 ft1 (0.00545*K>)
M. Average Stack Temperature 116 °F
N. Average Stack Temperature 576 °R (460+M)
O. Average Meter Temperature 79 °F
P. Average Meter Temperature 539 °R (460+0)
Q. Condensate Volume 12.0 mL
R. Absorbed H20 6.3 mL
S. Total H20 18.3 "mL (Q+R)
T. Filter Weight 0.0018 g
U. Probe Weight 0.0054 g
V. Impingcr Weight 0.0001 g
W. Total Weight 0.0073 g (T + U + V)
X. Metered Gas Volume 38.964 def
Y. Corrected Metered Gas Volume 38.309 def (X+H)
Z. H20 Gas Volume 0.896 "cf (0.00267~SWA)
AA. Total Sample Volume 39.205 cf (Y+Z)
BB. Percent H20 2.3 % (100*Z/AA)
CC. Gas Volume Sampled 37.003 dscf [Y*(528/P)*(E/29.92)J
DD. Grain Loading 0.0030 gr/dscf (15.43+W/CC)
EE. Average Molecular Weight:
Component
% Volume
+ 100
~(l-BB/100)
• Mol.
Weight
= Weight/Mol
H20
0.023
18
0.411
C02
0.000
0.977
44
0.000
CO
0.000
0.977
28
0.000
02
0.205
0.977
32
6.410
N2
0.795
0.977
28
21.751
Average Molecular Weight
FF. Average Stack Velocity
GG. Averge Flow Rate
HH. Standard Flow Rate
U. Sample Time
JJ. Percent Isokinetic
KK. Mass Flow Rate
28.57
25900 scfrn
sec
%
3600
94.3
lb./Ib. mol
67.7 fps {85.49*G*((F*N)/(C*EE)]*0.5}
28700 acfm (60*FF*J)
[GG*(528/N)*(C/29.92)]
{[lOO^CC^'jytHH^n^l-BB/lOO)]}
-------
STACK SAMPLING CALCULATIONS
CLIENT: USS CLAIRTON WORKS TEST DATE: 10-20-93
TEST SITE 13.14.15 BATTERY PEC - STACK 24 TEST NUMBER: CLR-2^t-2
A. Barometric Pressure 29.40 in. Hg
B. Static Pressure 0.60 in. H20
C. Stack Pressure 29.44 til. Hg [A+(B/13.6)]
D. Average aH 1.46 in. H20
E. Meter Pressure 29.51 in. Hg [A+(D/13.6)j
F. Average aP 1.2 in. H20
G. Pitot Coefficient 0.84
H. Gas Meter Coefficient 0.9619
I. Stack Diameter 36 in.
J. Stack Area 7.Q7 ft' (0.00545*!2)
K. Nozzle Diameter 0.185 in.
L. Nozzle Area 1.87E-04 ft* (0.00545*Ka)
M. Average Stack Temperature 108 *F
N. Average Stack Temperature 568 *R (460+M)
O. Average Meter Temperature 81 °F
P. Average MetCT Temperature 541 °R (460+0)
Q. Condensate Volume 11.8 mL
R. Absorbed H20 6.6 mL
S. Total H20 18.4 mL (Q+R)
T. Filter Weight 0.0018 g
U. Probe Weight 0.0056 g
V. Impinger Weight 0.0001 g
W. Total Weight 0.0075 ~g (T+U+V)
X. Metered Gas Volume 40.379 def
Y. Corrected Metered Gas Volume 38.841 def (X*H)
Z. H20 Gas Volume 0.9Q4 "cf (0.00267*S«P/A)
AA. Total Sample Volume 39.745 cf (Y+Z)
BB. Percent H20 2.3 % (100*Z/AA)
CC. Gas Volume Sampled 37.384 dscf {Y*(528/P)*(E/29.92))
DD. Grain Loading 0.0031 gr/dscf (15.43*W/CC)
EE. Average Molecular Weight:
Component
% Volume
+ 100
•(1-BB/I00)
~ Mol.
Weight
= Weight/Mol
H20
0.023
... • •
18
0.409
C02
0.000
0.977
44
0.000
CO
0.000
0.977
28
0.000
02
0.205
0.977
32
6.411
N2
0.795
0.977
28
21.754
Average Molecular Weight
FF. Average Stack Velocity
GG. A verge Flow Rate
HH. Standard Flow Rate
II. Sample Time
JJ. Percent Isokinetic
KK. Mass Flow Rate
28.57
3600 sec
%
96.2
lb./lb. mol
64.6 fps {85.49*G*[(F*N)/(C*EE)]A0.5}
27400 acfm (60*FF*J)
25100 acfm [GG*(528/N)*(C/29.92)]
{[100*CC*60*J]/[HH*L*H*(1-BB/IOQ)]}
-------
STACK SAMPLING CALCULATIONS
CLIENT: USS CLAIRTON WORKS TEST DATE: 10-21-93
TEST SITE 13,14.15 BATTERY PEC - STACK 2-1 TEST NUMBER: CLR-2-1-3
A. Barometric Pressure 29.21 in. Hg
B. Static Pressure 1.00 in. H20
C. Stack Pressure 29-28 in. Hg (A + (B/13.6)}
D. Average aH 1.93 in. H20
E. Meter Pressure 29.35 in. Hg [A+(D/13.6)J
F. Average iP 1.6 in. H20
G. Pitot Coefficient 0.84
H. Gas Meter Coefficient 0.9912
I. Stack Diameter 36 in.
J. Stack Area 7.07 ft' (0.00545*I*)
K. Nozzle Diameter 0.190 in.
L. Nozzle Area 1.97E-0* ft3 (0.00S45*K2)
M. Average Stack Temperature 121 °F
N, Average Stack Temperature 581 ®R (460+M)
O. Average Meter Temperature 76 *F
P. Average Meter Temperature 536 °R (460+0)
Q. Condensate Volume 13.0 mL
R. Absorbed H20 8.9 mL
S. Total H20 21.9 mL (Q+R)
T. Filter Weight 0.0016 g
U. Probe Weight 0.0029 g
V. Impinger Weight 0.0002 g
W. Total Weight 0.0047 g (T+U + V)
X. Metered Gas Volume 49.154 def
Y. Corrected Metered Gas Volume 48.721 def (X*H)
Z. H20 Gas Volume 1.073 cf (0.00267*S*P/A)
AA. Total Sample Volume 49.794 cf (Y+Z)
BB. Percent H20 (100*Z/AA)
CC. Gas Volume Sampled 47.083 dscf [Y*(528/P)*(E/29.92)J
DD. Grain Loading 0.0015 gr/dscf (15.43*W/CC)
EE. Average Molecular Weight:
Component
96 Volume
+ 100
•(l-BB/100)
~ Mol.
Weight
= Weight/Mol
H20
0.022
18
0.388
C02
0.000
0.978
44
0.000
CO
0.000
0.978
28
0.000
02
0.205
0.978
32
6.419
N2
0.795
0.978
28
21.780
Average Molecular Weight
FF. Average Stack Velocity
GG. A verge Flow Rate
HH. Standard Flow Rate
II. Sample Time
JJ. Percent Isokinetic
KK. Mass Flow Rate
28.59
3600 sec
100.7 %
lb./Ib. mol
75.7 fps {85.49*G*[(F*N)/(C*EE)]A0.5}
32100 acfm (60*FF*J)
28600 scfm [GG*(528/N)*(C/29.92))
{[100*CC*60*J]/[HH*L*II*(1-BB/100)J}
-------
STACK SAMPLING CALCULATIONS
CLIENT: USS CLAIRTON WORKS TEST DATE: 10-21-93
TEST SITE 13.14.15 BATTERY PEC - STACK 2-2 TEST NUMBER: CLR-2-2-3
A. Barometric Pressure 29.21 in. Hg
B. Static Pressure 1.10 in. H20
C. Stack Pressure 29.29 in. Hg [A+(B/13.6>]
D. Average aH 1.75 in. H20
E. Meter Pressure 29.34 in. Hg [A+(D/13.6)]
F. Average aP 1.45 in. H20
G. Pitot Coefficient 0.84
H. Gas Meter Coefficient 1.0151
I. Stack Diameter 36 in.
J. Stack Area 7.07 ft3 (0.00545+P)
K. Nozzle Diameter 0.192 in.
L. Nozzle Area 2.01E-04 ft> (0.00545+K3)
M. Average Stack Temperature 126 °F
N. Average Stack Temperature 586 *R (460+M)
O. Average Meter Temperature 85 ®F
P. Average Meter Temperature 545 *R (460+0)
Q. Condensate Volume 11.2 mL
R. Absorbed H20 9.6~mL
S. Total H20 20.8 mL (Q+R)
T. Filter Weight 0.0032 g
U. Probe Weight 0.0027 "g
V. Impinger Weight 0.0001 g
W. Total Weight 0.0060 g (T+U+V)
X. Metered Gas Volume 46.012 def
Y. Corrected Metered Gas Volume 46.707 def (X*H)
Z. H20 Gas Volume 1.036 cf (0.00267*S*P/A)
AA. Total Sample Volume 47.743 cf (Y+Z)
BB. Percent H20 2.2 % (100*Z/AA)
CC. Gas Volume Sampled 44.371 dscf [Y*(528/P)+(E/29.92>]
DD. Grain Loading 0.0021 gr/dscf (15.43+W/CC)
EE. Average Molecular Weight:
Component
% Volume
+ 100
~(l-BB/100)
• Mol.
Weight
= Weigh t/Mol
H20
0.022
18
0.391
C02
0.000
0.978
44
0.000
CO
0.000
0.978
28
0.000
02
0.205
0.978
32
6.418
N2
0.795
0.978
28
21.777
Average Molecular Weight
FF. Average Stack Velocity
GG. Averge Flow Rate
HH. Standard Flow Rate
n. Sample Time
JJ. Percent Isokinetic
KK. Mass Flow Rate
28.59
3600 sec
98.1 %
lb./lb. mot
72.3 fps {85.49*G*[(F*N)/(C+EE)]A0.5}
30700 acfm (60+FF*J)
27100 scfm [GG*(528/N)*(C/29.92)]
{[100*CC*60+J]/[HH*L*IIt(l-BB/100)]}
-------
STACK SAMPLING CALCULATIONS
CLIENT: USS CLAIRTON WORKS TEST DATE: 10-21-93
TEST SITE 13.14.15 BATTERY PEC - STACK 2-3 TEST NUMBER: CLR-2-3-3
A. Barometric Pressure 29.21 in. Hg
B. Static Pressure 1.20 in. H20
C. Suck Pressure 29.30 in, Hg (A+(B/13.6)]
D. Average aH 1.40 in. H2Q
E. Meter Pressure 29.31 in. Hg [A+(D/13.6>]
F. Average a P 1.3 in. H20
G. Pitot Coefficient 0.84
H. Gas Meter Coefficient 0.9832
I. Stack Diameter 36 in.
J. Stack Area 7.07 ft' (0.00545M*)
K. Nozzle Diameter 0.183 in.
L. Nozzle Area 1.83E-04 ft2 (O.OG545*KS)
M. Average Stack Temperature 121 °F
N. Aversge Stack Temperature 581 °R (460+M)
O. Average Meter Tempersture 83 *F
P. Average Meter Temperature 543 °R (460+0)
Q. Condensate Volume 8.9 mL
R. Absorbed H20 9.6 mL
S. Total H20 18.5 mL (Q+R)
T. Fflter Weight 0.0018 g
U. Probe Weight 0.0059 g
V. Impinger Weight 0.0002 g
W. Total Weight 0.0079 g (T + U+V)
X. Metered Gas Volume 38.851 def
Y. Corrected Metered Gas Volume 38.198 def (X*H)
2. H20 Gas Volume 0.918 cf (0.00267*S*P/A)
AA. Total Sample Volume 39.117 cf (Y+Z)
BB. Percent H20 2J_ % (100*Z/AA)
CC. Gas Volume Sampled 36.389 dscf [Y*(528/P)*(E/29.92)]
DD. Grain Loading 0.0033 gr/dscf (15.43*W/CC)
EE. Average Molecular Weight:
Component
% Volume
+ 100
~(l-BB/100)
• Mol.
Weight
= Weight/Mol
H20
0.023
* ' < >*<> «'
18
0.423
C02
0.000
0.977
44
0 000
CO
0.000
0.977
28
0.000
02
0.205
0.977
32
6.406
N2
0.795
0.977
28
21.737
Average Molecular Weight
FF. Average Stack Velocity
GG. Averge Flow Rate
HH. Standard Flow Rate
II. Sample Time
JJ. Percent Isokinetic
KK. Mass Flow Rate
28.57
3600 sec
93.5 %
lb.Ab. mol
68.2 fps {85.49*G*[(F*N)/(C*EE)]A0.5}
28900 acfrn (60»FF»J)
25700 scfm [GG*(528/N)»(C/29.92)]
{[ 100*CC *60* J]/(HH •L*II*( 1 -BB/100)]}
-------
STACK SAMPLING CALCULATIONS
CLIENT: USS CLAIRTON WORKS TEST DATE: 10-21-93
TEST SITE 13.14,15 BATTERY PEC - STACK 2-4 TEST NUMBER: CLR-2-4-3
A. Barometric Pressure 29.21 in. Kg
B. Static Pressure 0.60 in. H20
C. Stack Pressure 29.25 in. Hg [A+(B/13.6)J
D. Average aH 1.13 in. H2Q
E. Meter Pressure 29.29 in. Hg [A-f (D/13.6)]
F. Average a P 0.9 in. H20
G. Pilot Coefficient 0.84
H. Gas Meter Coefficient 0.9619
I. Stack Diameter 36 in.
I. Stack Area 7.07 ft' (0.00545*Ia)
K. Nozzle Diameter 0.185 in.
L. Nozzle Area 1.87E-04 ft2 (0.00545*K3)
M. Average Stack Temperature 112 °F
N. Average Stack Temperature 572 "R (460+M)
O. Average Meter Temperature 80 °F
P. Average Moter Temperature 540 °R (4604-O)
Q. Condensate Volume 4.8 mL
R. Absorbed H20 11.3 mL
S. Total H20 16.1 mL (Q+R)
T. Filter Weight 0.0017 g
U. Probe Weight 0.0077 ~g
V. Impinger Weight 0.0001 g
W. Total Weight 0.0095 g (T + U + V)
X. Metered Gas Volume 35.902 def
Y. Corrected Metered Gas Volume 34.534 "def (X*H)
Z. H20Qm Volume 0.795 cf (0.00267*S*P/A)
AA. Total Sample Volume 35.329 cf (Y+Z)
BB. Percent H20 2.2~% (100*Z/AA)
CC. Gas Volume Sampled 33.059 dacf [Y*(528/P)*(E/29.92)J
DD. Grain Loading 0.0044 gr/dacf (15.43*W/CC)
EE. Average Molecular Weight:
Component
% Volume
+ 100
•(l-BB/100)
* Mol.
Weight
- Weight/Mol
H20
0.022
18
0.405
C02
0.000
0.978
44
0.000
CO
0.000
0.978
28
0.000
02
0.205
0.978
32
6.412
N2
0.795
0.978
28
21.759
Average Molecular Weight
FF. Average Stack Velocity
GG. A verge Row Rate
HH. Standard Row Rate
II. Sample Time
JJ. Percent Isokinetic
KK. Mass Flow Rate
28.58
3600 sec
98.8 %
lb./lb. mol
56.4 fpa {85.49*G*[(F*N)/(C*EE)]*0.5}
23900 acfm (60*FF*J)
21600 acfm [GG»(528/N)*(C/29.92)]
{J100^CC^60*J1/[HH#L*II*(1-BB/100)]}
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RJ Lee GroInc.
350 Hochberg Road • Monroeville, PA 15146
412/325-1776 - FAX 412/733-1799
December 13,1993
Mr. Patrick Stockton
Air and Hazardous Waste Management
Chester Environmental, Inc.
3000 Tech Center Drive
Monroeville, PA 15146
RE: RJ Lee Group Project No. INH312590
Chester Environmental Project/Account No. 300261-01
Chester Environmental Purchase Order No. B-7185
Dear Mr. Stockton:
At your request, we examined samples, provided by you, for total sulfate (S04) content.
The solutions were analyzed by direct injection of suitable dilutions, along with standard
sulfate solutions, on a Dionex 2120i ion chromatography unit. Results are calculated as
milligrams per liter (ppm) and then converted to total milligrams using the volumes of the
solutions that you provided.
These results are submitted pursuant to RJ Lee Group's current terms and conditions of
sale, including the company's standard warranty and limitation of liability provisions. No
responsibility or liability is assumed for the manner in which the results are used or
interpreted. Unless notified in writing to return the samples covered by this report, RJ Lee
Group will store the samples for a period of thirty (30) days before discarding. A shipping
and handling fee will be assessed for the return of any samples.
If you have any questions about this report, or if I can be of further assistance, please let
me know.
Sincerely,
Jeffrey A. Fumea
Shift Supervisor
JAF/dcd
Enclosure
Monroeville, PA • Berkeley. CA • Washington, D.C. • Houslon, TX
-------
KEYSTONE ENVIRONMENTAL RESOURCES, INC.
AIR QUALITY ENGINEERING
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-------
Table I
RJ Lee Group Project #: INH312590
For: Chester Environmental, Inc.
Client
Total Volume
Total mg
Analytical
Sample Number
Element
mg/L
(Liters)
Sulfate
Method
CLR-2-1-1
S04
37.7
0.1
3.77
IC
CLR-2-2-1
S04
35.6
0.1
3.56
IC
CLR-2-3-1
S04
70.5
0.1
7.05
IC
CLR-2-4-1
S04
75.3
0.1
7.53
IC
CLR-2-1-2
S04
80.5
0.1
8.05
IC
CLR-2-2-2
S04
74.8
0.1
7.48
IC
CLR-2-3-2
S04
75.3
0.1
7.53
IC
CLR-2-4-2
S04
109
0.1
10.9
IC
CLR-2-1-3
sot
51.5
0.1
5.15
IC
CLR-2-2-3
S04
55.3
0.1
5.53
IC
CLR-2-3-3
S04
88.1
0.1
8.81
IC
CLR-2-4-3
S04
89,6
0.1
8.96
IC
CLR-S04-BLANK
S04
1.58
0.1
0.158
IC
Authorized
Signaling--^ N (V \'v.
Dale ~A"( V > ) i rV\ \C t i
~iV-
RJ Lee Group, Inc. 350 Hochberg Road (412)325-1776
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