SN 16544.002
Final Copy
Test Number 7i-ci-03
Wood River Power Plant
East Alton, Illinois
by
N. A. Blessing/R. N. Allen
RESOURCES RESEARCH, INC.
A SUBSIDIARY OF TRW INC.
WESTGATEPARK • 7600 COLSHIRE DRIVE • McLEAN. VIRGINIA 22101
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SN 16544.002
TEST NUMBER
UNIT NO. 5
WOOD RIVER POWER PLANT
EAST ALTON, ILL.
N. A. Blessing/R. N. Allen
Revised
October, 1971
Resources Research, Inc.
A Subsidiary of TRW Inc.
7600 Colshire Drive
McLean, Virginia 22101
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1.
TABLE OF CONTENTS
II.
INTRODUCTION. . . . . .
. . . .
III.
SUMMARY OF RESULTS.
. . . .
. . . .
. . . .
IV.
PROCESS DESCRIPTION,.
. . . . .
V.
LOCATION OF SAMPLING POINTS
. . . . .
VI.
PROCESS OPERATION
. . . . . .
. . . . . . .
VII.
SAMPLING PROCEDURES
. . . .
. . . . .
VII I .
CLEANUP AND ANALYTICAL PROCEDURES
. . . . .
IX.
DISCUSSION
. . . . .
. . . . .
A.
Results
.......
B..
Test Conditions
. . . . .
.......
X.
APPENDIX. .
. . . .
.......
. . . . .
A. Complete Particulate Results with
Example Calculations
B. Complete Gaseous Results with
Example Calculations
C. Complete Operation Results
D. Field Data
E.l Sampling Procedures
E.2 Cleanup and Analytical Procedures
F. Laboratory Report
G. Test Logs
H. Related Reports
I. Project Participants and Titles
J. Stoichiometric Calculations
1
Page
3
6
9
12
15
16
17
18
18
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LIST OF TABLES
Table No. Title Page
1 EPA vs. ASME Particulate Emissions 6
2 Summary of Results 7
3 Precipitator Design Data 11
LIST OF FIGURES
Figure No.
Title
Page
1
Power Plant Block Diagram-Sample Locations
4
2
Process Flow Diagram
10
3
Sampling Stations at Wood River Power Plant
13
4
Sampling Ducts - Cross Section
14
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II.. INTRODUCTION
Source emission tests are being performed on a series of power plants
for use in determining the new standards of performance under the clean air
act.
Responsible for the basic test program is the Office of Air Programs,
Environmental Protection Agency.
These surveys include the determination
of filterable and total particulate matter, sulfur dioxide and nitrogen
oxides.
The tests described in this report were performed at the Wood River
Power Plant, East Alton, Illinois, during the week of February 15, 1971.
Emissions for this power plant were determined for the Number 5 unit,
consisting of two parallel boiler systems, both of which ultimately exhausted
to a single tall stack as shown in Figure 1 on the following page.
Further
detailed diagrams and descriptions are included in Section IV and Section V
(Process Description and Location of Sampling Points) of this report.
During this survey particulate matter was sampled using the special EPA
train and a so-called ASME train, employing an alundum thimble filter within
the stack.
Sulfur dioxide,was sampled using the modified Shell Development
Method.
Integrated combustion gas samples were collected in gas bags and
analyzed by the standard Orsat apparatus.
Nitrogen oxides were collected by
a grab sampling procedure and analyzed by the Phenoldisulfonic acid method.
Six exhaust duct particulate samples were collected in pairs, obtaining one
sample at each of the two parallel exhaust locations.
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~
Cleaned Exhaust
Gases
iStack
o
Sampling Locations
o
o
Electrostatic
Precipitators
-----,
-_J
Electrostatic
Precipitators
Figure 1.
Exhaust
Exhaust Gases
['Pre
Heate
Air
POWER PLANT DIAGRAM
High Pressure Steam
i to Generators
i
I
I
I
,""---) Coal
\ j
. Bins
r,----'-'.', ""'-.--1 ,----, .
'L
.~ I ""--'--
I Botler r Coal
I. .
H~a r.ed I : : - L-=:Ji Pul verizers
A~. r___':-~~-'-r.::--'~~ ~
~--
-------
During the latter two sets of exhaust samples an A8ME train was run
side by side with one of the EPA trains.
A total of five 802 and ten NOx
emission tests were conducted at the precipitator exhaust location.
The
data also includes coal and ash analyses.
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III.
SUMMARY OF RESULTS
Particulate "catches" obtained by the EPA and ASME sample trains at
the two exhaust ducts of the precipitator are shown in Table I below.
TABLE I
EPA vs. ASME PARTICULATE EMISSIONS
Sample ASME vs.
Method Duct-Run Date Time grains/SCF Lbs/Hour EPA
EPA East-EDE-2 2/19/71 (1245-1654) 0.064 240 )
) 50%
ASME East-EDE-2 2/19/71 (1300-1550) 0.032 120 )
EPA West-WDE-3 2/20/71 (1335-1803) 0.166 540 )
) 16'70
ASME West-WDE-3 2/20/71 (1415-1645) 0.026 85 )
There were only two comparative samples for the sampling trains
and there is very little evidence of duplication in results.
Based only
upon the above information, there is no correlation between the ASME and the
EPA sampling train emission data.
Operation of this power plant unit was considered to be normal at
all times and, at any given time, the operation was quite stable.
There
were differences in electrical load, however, for each series of tests.
Summaries of the various plant exhaust emissions are shown in Table 2, on
the following page.
Operating parameters of the furnace during each testing
period are shown in Appendix C.
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. '
TABLE 1
, "
. . . .
. ... - -'..-.-' ....- ~:. .....-; .. .:--:- ..'" ... '," """-. - ... .
" . ..... ...~... -... ..."
. . -....- .
, ..' ..
, . .
-'7" .-...
. ---.-- .'
. '''.
SU~ARY OF RESULTS
..
, '
Run Number 'EDE-1 WDE-1 EDE-,2 WDE-'2 ED.E-3 !WDE-3
-, ~Date . . , '2/18/71 /18/71 2/19/71 2/19/71 2/20/71 2/20/71
. "
., . .Stack FloH Rate - SCH1'* lJ{~= H7tS!IJC lI~()!i I:CO ~j~t::f~O' ,
dry 436,000- -' 406.nQO . . q;-~~o~ov
% Water Vapor - % Vol. 5.23 :>.98 4.12 8.30 ~4,8 ~9,9
~'-J-c6rVo1 .
% dry 3.3 . 4.3 13.6 14.0 13.4' 13.9
% 02 - Vol % dry 5.6 .9 5.5 5.2 5.8 .. 5.3
% Excess air @ sampling po i n t 35.0 ~2~,.? ~~~1~/.9 ~ff.'C '~.7
- Stf.s~~ S9ID~ling DateJ1 ?/17/71 '>/11771 '- 2/18171 2/20171 2/20/71
2 1 s S 1 0 S - ppm ry 3128.3 :s216.0 - 3195.1 2858.4 2462.8
',NO' Emissions - ppm dry ~~~s H7.0 96.0 N/A 409.0 475.0 441. 0
x ' Asso2 ~40.0 ~ 472.0. 500.0 446.0
Particulates 2ft Lf:
-------
The percentage of particulate material from the impinger train,
following the probe, cyclone and filter, was not as uniform as had been
expected.
This "condensible" portion of the catch varied from one-fourth
to three-fourths of the total catch.
Particulate emissions from the boiler unit were approximately
0.05 grains/SCF, dry, as filterable material.
The total catch of
"particulate" was roughly double the amount of filterable material or
0.10 grains/SCF, dry.
NOx emissions ranged from 400 to 500 parts per
million and S02 emissions were approximately 3,000 parts per million.
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IV.
PROCESS DESCRIPTION
The Number 5 unit at Wood River Power Plant is a modern electrical
generation facility using two parallel pulverized coal burning steam boilers.
After being used to produce high pressure steam the hot gases and emissions
from the combustion of coal are channeled through rotary, air to air heat
recovery units, and then through parallel electrostatic precipitator units
to reduce dust concentration levels.
Gases leaving the precipitators are
brought together in a common exhaust stack.
A flow diagram (Figure
2)
and a list of precipitator design data are enclosed on the following pages.
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t-'
o
!
f
!
I
I
;
I
i
I
/
I
Exhaust Stack
\
I
\
~
Sampling Platform
I Sampl ing
Ports
Heat Exchanger
or
Air Preheater
-_... --...-
fr
Electrostatic
Precipitator
...--
/ / Superheated Steam
I ! to Turbines
'l
in' I'
I Superheater
I' L LJ I
!
i
j
I
I
~
;
I
i
!
-+
I
i
IUI ~ T
I CO:1 Pu1 verizer '"
!
~
II
j ,
, .
(, ~
; i.
I
I Exhaust Gases
1
j
j
. f
;
i
j !
!
I
;
~
\
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I
1 !
!
1 -,
I
....---.----
.r--
f
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1
!
\
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? Boiler
FIGURE 2.
PROCESS FLOW DIAGRAM
) ,
i i
.
i
1
If I
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Table 3
Precipitntor design dat3 required
1.
Design coal analysis
2.
a. % ash 13.65
b. % S 4.06
c. Other Vol. 34.55%; FC 41.46%
Design efficiency, %99, based on 1,205,000
Total projected collecting surface area, ft2
200,340
3.
Total gas flow, 1 at~acfm
a. temperature 287°
l,205,OOO
4.
2
Collecting area per unit gas flow, ft /1000 acfm
165
5.
Linear gas velocity ft/sec
5.62
6.
Residence time, sec.
4.8
7.
Maximum voltage
- - - "'"
a.
primary
secondary
LfOO
45,000
b.
8.
Maximum current, amp at primary volts.
225
9.
Number of independent electrical sections
21
10.
Type of power control
Anacomp - Analog Computer
Automatic Voltage Control; Saturao1e Core Reactor
568,500 - Precip. alone
11. Total bid cost
12. Precipitator erected cost
13. Operating cost x
14. Boiler data
2,250,000
a.
% of ash of fly ash
name plate capacity
heat rate, Btu/kwhr
IF /hr
c.
80
2,454,000
9050
b.
15. Manufacturer
Buell Engineering Co., Inc.
Lebanon, Pa.
2.0 - 7.0 gr/cu ft @ 32°F
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v.
LOCATION OF SAMPLING POINTS
Sample port locations were installed as part of the original plant
construction and these locations were approved by the EPA Project Officer.
The sampling ports located on the top of ducts prior to the electrostatic
precipitator were not employed as part of this survey.
There were six
4-inch sampling ports across the top of each exhaust duct to the stack.
Due to the extremely large sizes involved a secondary platform was mounted
about six feet above the sampling ports.
The cross section of both ducts was divided into sixty-six equal
areas as shown in Figures 3 and 4 on the following pages.
Gaseous sampling for sulfur dioxide and nitrogen oxides and Orsat
analyses was conducted with probes placed five or six feet down into the
exhaust ducts.
All test points were selected by the EPA Project Officer.
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s
Common Exhaust Stack
I-'
W
2 3 4 8 9 10
Sampling ~ 0 0 00 ~ Sampling
Ports Ports
.4 24' . 24' ~
East West
Duct ~ ~ Duct
Flow
Flow
Figure 3 .
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I Exhaust Stack
I
I
I
I
I
I I
1 2 3 4 5 6 7 8 9 10 11 12
1 0
2 ,,-.. /, 0
11 Sample points for all ports \" ''0
~'
as shown in West Duct. Both .'-", 0 0
3 0 \..~) C>
ducts have equal dimensions.
4 () r ,"-" 0 G
.' J '-.:.>
".....-
...... 5 .-... C 0 0 0 n
~ \.-".-J
6 ,...... O. 0 0 0 (j
288" V ....-'
7 0 0 0 0 0 (7';
-,
S 0 0 0 r, n r'"
'...- ,~.~./ ,--:.J
9 0 "" ,-"'-, ~ 0 0
\..:.: I~__.. U
10 C; 0 C 0 0 G
11 r\ f'. 0 r:J 0 0
\.:...) ~J' ~
-
East Duct - 288" ~
West Duct
i FIGURE 4. SAMPL ING DUCTS
l CROSS SECTION
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VI.
PROCESS OPERATION
.
All sampling was conducted during periods in which operations
were consider~d to be normal.
An unexpected change in electrical load
was required during the second set of samples, therefore no gaseous
analyses were conducted during the latter part of this test.
Detailed
control room operational information was obtained during each run and is
contained in Appendix C.
In addition to data compiled from operating
instruments, the company supplied computer printouts for additional
information.
Output loading for the boiler was changed deliberately
between each test, so that emission concentrations could be compared
under specific operating load conditions.
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VII.
SAMPLING PROCEDURES
"Procedures For Performance Testing Of Fuel-Burning Equipment" was
printed for internal and contractor use by the U. S. Environmental Protection
Agency, Air Pollution Control Office.
It was labeled for Technical Review
Only and has apparently never been published in this form.
All sampling
followed the above procedures unless modified by the EPA representative.
Special sampling techniques were prescribed in detail at the site due to
the extremely large sizes of exhaust ducts.
Preliminary velocity, moisture and temperature readings were obtained
in order to select nozzle sizes for isokinetic sampling.
Particulate
sampling was conducted using the EPA train as described in Appendix E-I.
A so-called ASME train was used simultaneously with the EPA train during
the last two runs, one test at each exhaust duct.
Gas sampling was also conducted according to the above "Procedures".
All of these methods are essentially in accord with the proposed EPA
standard source testing methods.
Sulfur dio~ide was sampled with midget
impingers using isoprqpyl alcohol and hydrogen peroxide solutions.
Grab
samples of nitrogen oxides were collected in evacuated flasks according to
the phenoldisulfonic acid procedures.
Combustion gases were sampled in
plastic bags for immediate analyses with an Orsat analyzer.
Details of
the various sampling procedures are described in Appendix E-I.
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VIII.
CLEANUP AND ANALYTICAL PROCEDURES
The methods employed for cleanup of the EPA particulate train have
become relatively standardized through testing incinerators for government
approval.
Various sections of the sampling train were washed with acetone
and water.
The filter was removed carefully and each portion of the
collected particulate matter was placed in separate containers.
All
portions were then dried at ambient conditions and the water was extracted
for organic material, as well as being evaporated to dryness.
The alundum thimble filter from the ASME train was carefully removed,
placed in a glass container and sealed.
The water filled Greenburg-Smith
impingers in this train are not normally analyzed.
Similar cleanup pro-
cedures and care were employed for the gaseous samples.
Procedures for all of the above sampling devices are outlined in
detail in Appendix E-2.
Both cleanup and analytical procedures were
conducted under supervision of an EPA representative in accordance with
approved methods.
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IX.
DISCUSSION
A.
RESULTS.
EPA vs ASME
The EPA sampling train, being a more complex and exacting devioe
for measuring total particulate concentrations, was expected to collect
more particulate mater}al than the ASME train.
There were only two
comparative samples for the sampling trains and, although the particulate
concentrations were greater with the EPA train, there was no duplication
or correlation between the ASME and the EPA sampling train emission
data.
In one comparison the ASME result was 50 per cent of the EPA
comparative result, while the second comparison indicated the ASME result
to be only 16 per cent of that obtained with the EPA train.
Although the duplication of comparative results was extremely poor,
there was a greater lack of duplication between successive EPA train
samples than with the ASME train samples.
An added problem in evaluation
was that the comparative samples were conducted on opposite exhaust ducts,
under different boiler load conditions.
Results Using EPA Train
Three sets of exhaust EPA train samples were satisfactory for
comparison.
Boiler operating loads were changed slightly for each set
of samples.
It appeared that the east exhaust duct contained a lower
concentration of particulate matter in spite of having somewhat greater
total stack flow.
In each set of samples the greater emission of
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particulate matter was found to be present in the west exhaust duct.
The
two boiler systems were completely parallel in all respects and, as far
as known by operating personnel, the two units were completely parallel
in operation.
Although the stack gas temperatures were equivalent the flue
gas volume in each duct was noticeably different.
It would appear that the
west precipitator unit was not operating as efficiently as the eastern
counterpart.
Gaseous Emissions
The gaseous emission concentrations of S02 and NOx were relatively
uniform.
The slight variations which occurred offered no particular
correlation with time, location or operating conditions.
Due to an
unexpected change in boiler load during the second set of samples, gaseous
sampling was eliminated by the EPA representative for the remainder of that
sample period.
Sulfur dioxide samples were normally obtained at some period
during each particulate test.
Because of the double duct sampling, with
insufficient manpower and equipment, the two S02 tests were not obtained
simultaneously.
The NOx test was arranged so that one sample would be
obtained at each exhaust duct near the beginning of a sample and a second
test would be obtained for each duct near the end of that day's particulate
sample.
The necessary manpower to obtain these samples was obtained in
between movements of the heavy sample probes from one sample position to
the next.
-------
Uniformity of Results
As discussed under EPA and ASME results, there is some unexplained
variation in results.
The possible reasons are difficult to unravel
because each individual exhaust duct appeared to be noticeably different
in emission of particulate matter.
In addition, there was a deliberate
change in boiler operating conditions for each set of samples.
The two
ASME samples were obtained so that one was from each exhaust duct on
different days, so that comparison between the two results was nearly
impossible.
The operation of the power plant, using rather homogenous and
uniform fuel, should have been extremely stable at any given condition.
Although the total amount of particulate or gaseous emissions might vary
with operating loads it would have been expected that the ratio of
filterable particulate to condensible solids would have been relatively
stable.
The results of sampling did not show such stability, but the
"soluble particulate" portion varied from 26 per cent to 74 per cent of
the total catch in the six EPA results.
There is no completely satisfactory explanation for this variation,
however, it is believed that some of the problem would be a result of the
difficulty encountered in handling such long probes and in completely
rinsing out those same probes.
There would appear to be some justification
for noting a correlation between large soluble particulate or small per-
centage solubility compared to the length of the probe being employed for
that particular sample.
Note the pattern of probe use under "sample
locations and problems".
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B.
TEST CONDITIONS
Sample Locations
The outlet sample locations were placed in a satisfactory location
for relatively good sampling.
They were certainly placed in the only
available locations.
An important consideration was that the electrostatic
precipitator would have removed most of the large diameter particles,
therefore it would h~ve been expected that the remaining particulate
matter would be relatively well dispersed in spite of the large horizontal
duct.
Each duct cross section had been divided into eleven equal layers
by the EPA representative.
The sampling period at each point was
adjusted because of the inability to reach all of the 66 individual
sampling positions.
Sampling Problems
Just about all of the sampling problems were related to the fact that
the horizontal duct had a depth of 24 feet in which sampling was to be
conducted.
This extreme length meant that glass lined probes could not
be used due to the almost certainty of breakage.
Special probes were supplied by EPA for this survey.
Ten foot incaloy
tubing had been made with interconnecting fittings.
The bottom section had
fittings to match the nozzle attachment.
All three sections were designed
to fit together.
A ten foot section of teflon tubing was designed to connect
the heated glassware box to the top of the third section.
Each section of
probe was wrapped with a heating element with electrical connectors placed
such that each section could be heated independently.
The entire probe was
then wrapped with heat resistant electrical tape.
-------
Pitot tubes were provided for each probe assembly and these were
connected in sections also.
The pitot tube was clamped to the probe assembly
with ordinary stainless steel hose clamps after all individual sections were
assembled.
The combined pitot tube-probe was not strong enough, or stiff
enough, to be lifted into a vertical position without permanently being bent
or broken.. The entire assembly was therefore clamped to a 30 foot length
of two inch pipe.
Th~s final assembly could be lifted (with some difficulty)
into each sample port and positioned at any of the eleven individual sample
points.
Two probes were constructed in the same manner.
The 30-foot combined probe assembly would have required some sort of
mounting for the EPA glassware box, or some sort of flexible hose which would
reach from the elevated platform to the top of the probe assembly when the
top (or Number 1) position was being sampled.
As only a ten foot semi-flexible
hose was available, this could not be done.
Interconnections on the three-section probes were not interchangeable,
therefore practical considerations determined that either one section or
three sections must be used at any time.
When three sections of the probe
were in use it was necessary to insert the entire probe into the stack prior
to being connected to the sample train.
A rubber stopper at the top end of
the probe presented excess blowing of the fumes into the assembly.
After the
probe and sample train were in position, the heated flexible teflon hose was
quickly connected to the top of the probe.
-------
In a similar manner, the single section probe, attached to its 3D-foot
section of two inch pipe, had to. be placed into position before the sample
train could be connected.
However, in this instance it was not necessary to
place the probe nozzle within the stack until after the flexible teflon hose
connection was complete~.
The number of test positions that could be reached with either probe
assembly was limited by the total travel of the flexible teflon hose.
This
teflon hose proved to be a problem.
Very gentle curves, or changes in
direction, were required to prevent pinching due to the probe pressure or
weight of hose when the probe was in an elevated position.
This would
choke off the sample flow and would eventually form leaks and cracks across
the hose.
When the three-section probe was employed only five bottom positions
could be sampled.
When the single section probe was employed only four
upper sample positions were accessible.
During the first two test runs on
the east duct, the top of the duct was sampled, while the west duct was
sampled at the bottom.
During the third test the probes were reversed;
the bottom of the east duct and the top of the west duct were sampled.
Each position was sampled for five minute periods.
During sample number two the flexible teflonhose developed a crack
where it had been crimped.
This hose was unwrapped and repaired in the
power plant instrument shop.
The necessity of forming smooth, gradual bends
in the hose shortened its usable length and limited the number of points
that were accessible.
Additional sources of error were created whenever it
was necessary to remove the hose for the move to a new sample port.
-------
During the last set of samples, the hose on the second unit developed a
break.
This hose was not repaired 'because there was a simultaneous problem
with high wind velocities which made it unsafe to handle the 30-foot probe
assembly.
The final sampling port was therefore eliminated from the sample
traverse on this last pair of test runs.
There was a major problem in cleaning up such long probes and flexible
hoses.
After each sampl~ was collected the probes were disassembled, so that
only ten foot sections were handled during cleanup.
The nature of the
particulate matter caused a great deal of material to be collected within
the probes, prior to any separation or filtration in the cyclone and glass
fiber filters.
These sample collection devices were maintained at elevated
temperatures (1500F) within the glassware sampling boxes.
Due to the constant handling of such long and heavy probes the electrical
connectors began to fray, and be pulled apart or broken, as sampling progressed.
By the time probes were being employed for the third samples most of the
electrical connections had been repaired, or had become unrepairable, so that
some probe section temperatures were maintained only by virtue of being within
the exhaust stack.
Where the probe was not in the exhaust stack there were
certain portions which may not have been properly heated.
This simply served
to increase the tendency for collection of material within the probes and
thereby increase the difficulty of quantitatively removing all particulate
matter during cleanup.
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Procedures
The basic procedures of sampling were essentially the same in all
respects as shown in Appendix E.
Whenever any departures from the standard
procedure were necessary they were made under the direction of EPA
personnel.
A trial run was conducted to select sampling parameters.
Gas
velocities and temperature readings obtained during this period remained
fairly constant.
Moisture content was also determined during this period
and utilized in obtaining the "K" factor setting on the nomograph for the
test runs.
Test equipment was also checked during the trial run.
The ASME train had the same problems of long sampling probes which
were not strong enough to be handled in such a deep duct.
A length of
1/4 inch stainless steel pipe was broken before deciding that the ASME
train samples would be conducted in parallel with the EPA train which was
obtaining samples at the top area within each duct.
Processing Information
Process information was normal and complete data is included in
Appendix c.
One man was assigned to do nothing else except monitor and
record the various control room instruments.
Because the emissions were
so important in determining future standards the precipitator design data
was included as part of the process description under Section IV.
-------
APPENDIX A
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.' .. .
..~
TABLE 2
. . .
-.-. .-.-
.---..-.....-
-- .~- .. .-:- .'. .......- - -'..
. _.&. .. .. .. .....
. . -...- .
. .
. .
. ...
. .
SU~ARY OF RESULTS
..
.
Run Number 'EDE-1 WDE-1 EDE-2 WDE-'2 ~-3 WDE-'
'Da te .. ') /18/71 /18/71 2/19/71 2/19/71 2/20/71 2/201.71
-.
Stack Flo'rl Rate - SCH1'* dry ~J~. ce "=u ,11:Zo;r~ ~~ I 41f...2"COO -
436, OO~ L. -,VV,", --. '" /Il~'(;~"o
X Water Vapor - % Vol. ~.23 ~.98 ~.12 8.30 1C!J:J1; B &:::!s5 ~ 9
~":--:X-CO ---=-Vo 1 % dry 3.3 . 4.3 13.6 14.0 13.4" 13.9
2
~ 02 - Vol X dry ~.6 r+.9 5.5 5.2 5.8 .. 5.3
~ Excess air @ sampling po i n t 35.0 ~~z.~'.Z; - ~/..~~ (/ 3G:;:063 i,
r:"T.--o, -"';(" ott. ~ ~. "31..'
.. ~8e~~ S~~ling Date~ ')/17/71 ')/17/71 . - 2/18/71 2/20/71 2/ zU/ /l
2 ,ss,o s - ppm ry 3128.3 216.0 - 3195.1 2858.4 2462.8
.NO Emissions - ppm dry B~~s ~17.0 96.0 N/A 409.0 475.0 441.0
40.0 ., ~ 472.0 500.0 446.0
X ASS02 --!jt "'.
Particulates 617."
.
Probe, Cyclo:le. & Fil ter Catd ). 0337 .0782 0.0427 0.116 0.0439 0.0511
*
gr/SCF dry
gr/CF @ S ta c k Condit; ons 0.0229 / o"'<-ir; p.0306 ~ Q-.6~ ~~ ~
.f!) 7S"S ,(n..
lbs./hr. 126 ?60 101) 400 170 170
Particulate from impinger train 50% 26% 67% 3370 45% 74%
(%" of .Tota1)
.-
. .
- ...
. ..
Total Catch ).0674 ).105 0.0636 0.173 0.0810 0.166
gr /SCF * dry
gr /CF @ Stack Cond it ions 0458 "..~' ~. 0458 - '- ----
. ofnciLJ J" 1l1- "&)i=;1? -; j'i {/
lbs./hr. 252 ~50 1240 600 310 540
"7
1,..
"Average Stack Temperature, of
280
280
280
.. 285
.
282 .
275
. --. .
. ". --. .. - .. ..
. --:. :;--'-:-::=-'. .
A-l
* 70°F. 29.92 II Hg
-------
REPORT NO,
. . .
, PAGE
SOURCE tESTING' CALCULATION FOP\l'1S
OF
PAGES
, .
...-.. .-.---..... - -- -
...-.--....... -..-.-..".
.. .... ,- - ......... ..
, .
. .- ..,
, .
'.
", '.
.. .."
. . ~.. .-
,Test. No. ED + WDE (1-3
.,
" ,
No. Runs
6
, .
Name of Fi nTI
Resources Research, Inc.
-.
,location of Plant'
East Alton, I1linois'
, '
- Type' of Pl ant
PQwer
. - - ....- -.. - -. .
,
Control Equipment
Electrostatic Precipitato~
- -
Sampling Point Locations East and West Duct Exha~st prior to Common Exhaust Stack
Pollutants Sampled Totai Particulate, S02; Nitrogen Oxides
Time of Particulate Test:
" ,
Run No. EDE -1 Date 2-18-71 Begin lilO' . End 1649
Run No. WDE -1 Date 2 -18-71 Begin 1105 End 1650
.Run No. EDE-2 Date 2-19-,71 Oegin 1245 End 1654
Run No.;, wbE-2 Date 2 -19 -71 Begin 1245 ,End 1655
Run No. 'EDE - 3 . Date 2-20-71' Beg~ri 1347 . "End 1'721
. Run No, WDE -3 Date~p-71 . Befin 1335 End 1803
CLJU\ IE Et~1 SSIOi' DATA
-
Run No.
I-
-
Pb barometric pressure) IIHg Absolute
~. ori fi ce pressure drop, "H20
Vm volume of dry gas sampled @ meter
conditions, ft.3 "
Average Gas M;ter Temperature, of . .
Tm
"
V Volume of Dry Gas S~~pled @Standard
ms td. Conditions, ft.3 .
Vw Total H20 collected, ml., Impingers
& Silical Gel. . .
V Volume of Water Vapor Collected
WgdS ft.3 @ Standard Conditions* -
--
EDE -1 ~E-1 EDE-2 WDE-2 EDE-3 ~E-3
'----- ----.....
29.9 29.9 29.9 129.9 29.9 '~9:9
"
-
1.21 0.83 1.22 0.94 1.25 0.85 1
I
.
,
73~22 80.35 61.28 70.92 72.29 ~7 . 01 I
- .
76 80 68 74 56 .1 46 I
!
72 . 28 78.23 61..60 70.27 73.78 f59.54 J
. ~:l
84.1, ~23.7 56 134.2 79
. .. --- -- - 3.7416.541
3.'~. 5..61' 2.65 6.36
---_J._- --.-.- .. J
, * 70°F, 29.92" Hg. .-
.--.---:. .... -------......
1\-2
--- - .....
-------
. '" .'
, ,
. PARTICULATE EHISSI0N DATA (cont I d)
.. -. ., .. . -- -... . . _. ... -.... - - . . ' ,
Run No. EDE -1 WDE -1 ~DE -2 ilDE -2 EnE -3 WDE-3
-
-
SM - % Moisture in the stack gas by volume, 5.23 6.98 4.12 8.30 4.93 8.55.
t~d :.. ~10 1 e
% C02
% 0
2 -.,
fraction of dry gas
---~.
0.948 0.941 0.956 0.917 0.962 0.901
-
13.3 14.3 13.6
4.0, 13i4 13.9
-.- --.- .. -- -
--. ..
. - .____-"_4- - - ..
'.-.----.
'.
5~~ - D. 2 -
5.8
5.3
.,
-
5.6
4.9
% N2 -
M W d. - ~1olecul~r weight .of dry stack gas
M W - Molecular weight of stack gas
-
81.1 80.8 80.9 ~0.8
80.9 80.8
-
l\.Ps
Ts .
~J5. P sX(T s +460)
P - Stack
s
Vs
As
Qs
- Velocity Head of stack gas, In.H?o
- Stack Temperature,oF
30.34 30.48 30.37 pO.44 3~035 30.44
29.7 29074 29.82 ~9.40 29.88 29.21
0.079 0.065 0.081 Jo074 0.081 0.065
-
280
280
280 . '. 285
282 275
7.64 6.93 7.75 7.40
7 '. 73 6 . 91
29.96 29.98 29.99 D9.98 29.98 29.98
- Stack Veloci ty @ stack conditions, fp;J11114 1010 1123 1080 1120 1013
- Stack Area, in. Z 82,94482,944 82, 944~2, 944 82,944 82, 914
Pressure, "Hg. Absolute
- Stack Gas Volume @
Standard Conditions.
*
SCFM
~36, ocr 393,(00 440,000 406,000 ~4~cro ~80 ,roo
Tt - Net Time of Test. min.
On - Sampling Nozzle Diameter, in.
%1 - Percent isokinetic
-
mf - Particulate - probe, cyclone
and fil ter, mg.
mt - Particulate - total. mg.
Can - Particulate - probe. cyclone,
and fil ter, gr/SCF
I Cao - Particulate - to ta 1, gr/SCF
t Particulate - probe. cyclone,
, Cat -
grlcf @ stack conditions
120
150
100
125
125.' 120
0.375 00375 0.375 0.375 0.375 0.375
105
99.2 103.9 103.6 99.2 ~7.7
158.4 397.6 70.7 530.8 2l0.4'1199~8
31601' 53302 254.7 788.4 38805 p40.9
6-;olJ cY.-Oi82 0.0427 0.116 0.043cOoOLAO
I
0.067~00.105 ).0636 00173 0.081O~.141 ;
. .. I
& f i 1 te r I t1/. h n
r.0229000561 0.0306 0.0825 b.03~73 :
-------
PARTICULATE E:USSION DATA (cant I d)
o .
O.
Run f.I~. .
EDE -1 WDE -1 EDE -2 WDE-2 EDE-3 VIDE-3
Cau Part; cul ate. total. grief .
- O.075~
° 0 .. O. 045E 0..04 58. 0 . 123 0.057i
@ s ta c k condo 0.12 0 .
-
Caw - Particulate, probe. cyclone.
and fi'lter, lb/hr-. 126 260 1~0 400 170 70
Cax - Particulate - to ta 1. lb/hr. . 252 350 240 600 310 ,40
% EAo- % Excess air @
sampling p~int - 35.0. ' 12 !h82 36-.-59 32.'24 37. 28' 3tT. D6
.. .-...- .. .. ... ----_...-------
*
70°F. 29.92" Hg.
-------
EXAMPLE PARTICULATE CALCULATIONS
SAMPLE EDE-1
1.
Volume 3of dry gas saMpled at standard conditions - 70°F, 29.92"
Hg, ft .
17.7XVm~B +Pm \
V = ~ . 13.6 -) = Ft. 3
mstd (T + 460)
J\1 .
) ( 1. 21
(17.7) (73.22 29.9 +~ )
76 + 460
.'
=
72.28
2.
]
Volume of water vapor at 70°F and 29.92" Hg, Ft. .
V
w
gas
3
= 0.0474 X V = ft.
w
= (0.0474) (84.1)
= 3.99
3.
% moisture in stack gas
100 X V
w
'oM = gas
V + V
mstd w gas
= %
= (100) (3.99)
72.28 + 3.99
5.23
-------
4.
Mole fraction of dry gas
M = 100 - '7oM
d 100
100 - 5.23
100
= .948
5.
Average molecular weight of dry stack gas
44 32" 28
M W d = ('7oC02 X 100 ) + (%02 X 100) + (7.N2 X 100)
= (13.3) ( .44) + (5.6) ( .32J + (81.1) ( .28)
= 5.85
+ 1.79
+
22.7
= 30.34
6.
Molecular weight of stack gas
M W = M W d X Md + 1 a (1 - M d)
= (30.34) ( .948) + 18 (1- .948)
= 29.7
7.
Stack velocity @ stack conditions, fpm
v = 4350 XVAP X (T + 460)
s 5 5
1/2
I . 1 t = fpm
Ps X M W ~
= (4350) (7.6lf)
[
1 1/2
(29.96)(29.7) ].
= 1114
-------
8.
Stack gas volume @ standard conditions, SCFM
0.123 X V X A X Md X P
Q s s s.
S = (T + 460)'
s
= SCFM
= (0.123)(1114)(82.944)( .948)(29.96)
740
= 436000.
9.
Percent isokinetic
)032 X (T + 460) X Vm - '%
%1 =V X T X P X M X (D )2"
s t s d n
- (1032)(740)(73.22)
- (1114)(120)(29.~6)( .948)( .141~
= 105
10.
Particulate - probe, cyclone, and filter, gr/SCF
Mf
C = 0.0154 X V
an
mstd
= gr/scf
=
(0.0154) (158.4)
72.28
=
.0337
11.
Particulate total, gr/SCF
Mt
Cao = 0.0154 X V
mstd
= gr/SCF
- (0.0154)(316.1)
- 72.28
=
.0674
-------
12.
Particulate - probe, cyclone and filter,
gr/CF at stack conditions
17.7 X C X P X "Md
an s
Cat = (T + 460)
s
= gr/CF
=
(17.7)(0.0337)(29.96)( .948)
740
=
.0229
13.
Particulate - total, gr/CF @ stack conditions
C
au
17.7 X C X P X Md
ao s
(T + 460) = gr/CF
x
=
- (17.7)(0.0674)(29.96)( .948)
- "740
=
.0458
14.
Particulate - probe, cyclone and filter, Ib/hr.
C = 0.00857 X C X Q = 1b/hr.
aw an s
=
(0.00857)(0.0337)(436,000)
= 126
15.
Particulate - total, 1b/hr.
C = 0.00857 X C X Q = 1b/hr.
ax ao s
= (0.00857)(0.0674)(436,000)
= 252
"A-8
-------
16. % excess air at sampling point
100 X % 02
%EA=
(0.266 X % N2)-% 02
= OOOH5.6)
(0.266)(81.1) - (5.6)
= 35%
= %
-------
SUMMARY OF TOTAL PARTICULATE EMISSIONS
(ASME EQUIVALENT)
Sample Location
Date Sampled Time Sampled Sample No.
2/19/71 1300-1S50 EDA - 1
2/20/71 1415-1645 WDA - 1
grains/cu ft,dry
gas,20°C,l atm
1bs/hr
East Duct Exhaust
0.032
120.
West Duct Exhaust
0.026
85.
DETERMINATION OF TOTAL PARTICULATE (WATER IMPINGER)
Sample Location
Vstd~Metered Gas Vol.
.Samp1e No. grams grains (drv,20°C,l atm)cu ft grains/std cu ft
!
EDA - 1 0.1418 2.19 . 68.04 0.0322
WDA.,. 1 0.1062 1.64 62.79 0.0261
East Duct Exhaust
West Duct Exhaust
STACK AND FLUE GAS CONDITIONS
Sample Flue Gas Avg.Ve1.Hd. Vs. Flue Gas' Flue Gas Flue Gas Vol. CFM
Snmp1e Location Number Temp. of Jif (in H22l Ve1.,fps Moisture.Vo1.% as is (drv.200C.1 atm)
East Duct Exhaust EDA - 1 300 0.278 18.9 4.91 653,000 430,000
West Duct Exhaust WDA - 1 280 0.250 16.7 5.30 577,000 390,000
>
I
.......
-------
ASME SAMPLE CALCULATIONS
1.
Isokinctic SOQpling (D~y Gas) (cfm)
2
nm :: .33 x ~~ x V s x d x
Ts
Ps
Pb - Pm
R~ (corrected) :: r~l x Me
Estin:3tcd Value: :3.3.X J~_6. x. 1~.: ~ .(.:4~6~ : ~~~t=..~7: : .94 = .635
- - - .. - .. .. ..
Calculated Value:
.33 X 576208 X 18.9 X (.1406) X 29.3 = .674 X .99 = .668
26.4
2.
I~ater Vapor Volume (cu. ft.)
Vv = .00267 x Vw x Tm
Pb - Pm
. .00267 X 38 X 528 = 1.98
27.0
3.
Condensate Correction for Meter Rate
He ::
Vm
Vm -I- Vv
77.29 -
= 77.29+1.98-
77.29
79.27
..98
4.
Hoisture in Hetered Gas (cu. ft.)
~~1 =
V.p. X Vr.1
Pb .- Pm
.667 X 77.29 = ~ = 1.91
27.0 27.0
5.
Percent Bois ture (%) Stacie Gas
% Hoisture =
Vv -:- j-int
Vv .... Vm
x 100
1.98 + 1.91 = ~ = .0491 =-4.91%
1.98 + 77.29 79.27
Saturated at
4.91
%
6.
Flue Gas Volume (cfm)
/'
as is C Va = Vs, avg. x A x 60 =
1134 X 576 = 653,184
dry, std cond = Vo x 5280R x 100 - % Hoisture = 653 184 X 528 X .951 = 431,560
Is 100 '760
7.
- .
Sampled Volumes converted to "standard"-conditions (cu. ft.)
V C:V -1-'
dg m '111
°
Vstd c Vdg x ~. x Pb - Pm
Tm 29.92
528 27.0
75.38 X 528 X 29.92 = 68.04
77,29 - 1.91 ~ 75.38
-------
APPENDIX B
-------
SULFUR DIOXIDE SAMPLING
Sample Date Time Total S02 1b/106BTU 3
Samn1e Location Number Sampled Sampled mg of S02 1bs of S021& Vo1.Sp1e ft (Vm) Tm Pm % Ea
St. Louis E1 2/17/71 1600-1622 394 -6 5.56 2.00 514 29.91 35.49
868.8 x 10
Exhaust Ducts -6
W1 1645-1707 383 844.5 x 10 5.23 2.00 522 29.91 29.82
W2 2/18/71 1730-1752 380.5 -6 5.33 2.07 526 29.91 36.59
839. x 10
I
E2 2/18/71 Not Run Due To Change In Plant' Output.
E3 2/20/71 0920-0942 358 -6 5. 02 2.00 497 29.91 37.28
789.4 x 10
W3 1000-1022 344 -6 4.58 2.00 501 29.91 30.06
758.5 x 10
O;j
I
-------
""
",
. ,
SO, EI~T~~Tn~ DATA
. 2. ."''''"''''''''''''. .
... .. . . "'-. '. .-.
.... - -.. ".""'" -.. .. -.... .. -.. '"
--, .. ---
, .
. ...... ...... -- -. .
. - - - .
'.
'.
. .' ..
~
-
Run No. EDE-1 WDE -1 EDE-2 WDE -2 EDE-3 IWDE - 3
Date - 2/17/7 2/17/71 - 2/JB/'71 2/2.0/71 2/2 0/71
mg 502 - "-.0__- -_. -.. -.. - e" . ; . j~4 383 -. - 3-80.-5 358 344
"
of - -
T - Average Gas Meter Temperature, 54 62 - 66 37 41
m
P-b - - ~Barometr; C Pr.essure. IIHg abs. 29.9. 29.9 -, - 29.9 29.9 29.9
V - Volume of dry g~s sampled @standard 1.65 1.56 1.64 1. 78 1.83
m conditions, ft. -'
. ppm _502 - -, 3128.3 3216.0 - 3195'.1 b858.4 0462.8
, '
. .'
., '
, . .
---- . -.-.... --. .-.. . ----
, :':: ,- '.' O. 733~i~--W2"-~ .t+m--+'. 460)
.' .'-..- _._-- -- - - -- - . .. .
- , ppm.5.o2 =,
Not used:due to vacuUm on meter
-PL--X-...\L,----.,..- '
-7", - u, m '
, .'
-".." .
- .
~
, 1..- .
..
FORMULA::.mg'S02" ,
, ,V'std
=
mg!SCF x 13.1 ~.ppm S02
. ....
EDE -1
PPM S02 =
(394): 03.J,l
(1..65)
=
. .
'31-28.'3 .
. :S02 EXAMPLE CALCULATION
EDE-1 ".
C~nversion of Cubic feet to standard condftion& .
530 Pb ._.~ '
Vstd=.( Y~)(Tm+'460) ( 29.92 ). . -- "... ---.-.
Vstd." (-2'.00) -( ;ig) (~~:~2) = 1.65.. . -. -_.-...._.!.~
... .. . .. .. -.. . ..
.. ..
.....
..'~-';".-" ---..'":""':---:..:
-. ..----.-"....-
-------
'j
~~
. .
. ..
NOx' nHSS.IOH DATA
. . . . ".-... _.'.",---- ... "", ".'-",-",'"
. .- ~_.- --. ... .
. .
. .
.0', --." .... .'... -:-'. -
.._- -.. -..-...-.----..
.,. ... _.... _. . .-.
-
Run No. . IDE-2
EDE -1 - WDE -1 EDE-2
,Da te r;./17/7~ 2/17/71 2/17/71 2/17./71 N/A /18/71
mg NOZ :1..61 1. (j8 1.92 1.90 N/A 1.53
Tf .: Flask Temperature, of 45 45 "45 45 N{~,,- 5~L..
- -.- .. - - - ..--. ...-
Vf -. Flask Volume, 1 i ters 2.125 - 2.146 2.131 N/A 2.125
- 2.141
P. Initial Flask Vacuum, IIHg. ...
- 27.5 27.5 27.5 27.5 N'/A. 27.5
1 . - .-. -
Flask Vacuum, IIHg. :
P - Fi na 1 0.5 0.5 0.5 0.5 N/A ~ O.S
o' f
ppm N Oz 417.0 440.0 496.0 ,493.0 N/A 409
. .
. .. ..:',
.' ..
o
.'
~.
.---...,. "'._-'-~~:'!
". . .
!
: I
. .
- '
, !
- --- -, ':~_::_~~:: ~,..:- ,29.63 x mg NO Z X
. .
. I..
-... ppm N02=.. .
. Vf .X., (Pi - Pf)
.-
...1 ' .
. :
. ..'.
-..-.-. -_. ....- ,'-... .-. .., ....
(Tf + 460).
. .
,
. .
-
. .
-
, . EDE":' 1 -.. -' '. '.. . . - .. - .
~., .~ _(:l9.63Y (1.6l) (.505) -- (29.63) 0.61) (505)
.PPM N02 - - (2.141>"'(27.5 -.5)" - (2-.141).(27;0).
.,".... .
=
417.{J.
- -
_." .
. . ...,..' ..
.. - .
. -... - .
. . .. .
-
. ,-. .
"
. .
. .
, .
. . .. "-.
- .
B-3
_. . . . . -
-------
. .
. '", ','
. ,
NOx' EMISS,IOIl DATA
-..
,.".....- --... --- ... .., ....-." --"
. .' .
.. --- --.... --. .. ."
. .... .
. .' .
'0. "-." ... .,... .'--, ...,-..... ----.------.
. .' .
~ - .. -... _. . ... .
Run No. WDE -2 . EDE-3 2/20/71 ::~;7I .;;f=
,Da te 2/18/71 2/20/71
mg N02 1. 78 1.81 1.91 1. 70 1.71
'Tf - Flask Temperature, of 58 40' ',40 38 38,
. __'0"
. _.- .. - - .-.. ,-- .. . -
Vf -, Flask Volum~, 1 i te rs - 2.141 2.125 '2. f41 2.146 2.131
P. - Initial Fl as k Vacuum, IIHg. .-
1 . 27.5 27.0 27.0 27.0 27.0.
- - _.
.' P f- Fi na 1 Flask Vacuum, IIHg. :
0.5 0.5 0.5 0.5 :>.5 ~
ppm N L2 472 475 500 441 446
~.
. .. .",'
-... .'~-'--:-~"!
. ..
,
: i
.. .
. .
, !
. ,
- .~. " ':~-'-~'~_:: ~,~.~. ..29.63 x mg NO 2 X
. I
I . .
. -.. . ppm N02=.. . .
. Vf X., (Pi - Pf)
.-
. ,.1 -. . .
. ... - . -_. .--:-... - ",...
(Tf + 460)
. .
. .
-
. '
. .
. .
-
. '.
. ". .
. 0
--"..... .
_.- .
. . ".,..' ..
.. - .
. -... ..
'. .. .
--
. ,-. .
"
. "
. .
. .
... "
. . . - . -...
- .
.. -.... .. .
. .
-.....-------
-.... . .._h._.-
..-.".- -----..--
.. - _. _. .
...... '"
..
. .. .. .e- -..
. ... . ...- ..-.. .... .
.. . ".
.... _... ... -- .. ... .._.- _. .. ~ -- ',"'0 .-.. .. ..-. ... -."
o .'
B-4
. . .
-------
. .
- r o. Part 7. p. 1 of 2
DEPARTMENT OF HEALTH, E~~~A7ION, AND WELFARE
P:Jblic Health Service
National Center for Air Pollution Control
FORt.! J\PPROVED
BUDGET BUHEAU
NO.
APPROVAL EXPIRES
ORSAT DATA AND CI\LCULoATIOil SHEET
Orsat Analysis - Bur.ner Only (From bag sampled
Sampling po)nt location
Date
Time
-Analysis Analysis Analysis x = \'It/mole !
1 2 3 Avg mo1e.wt (dry)
I
-102- (V~~ ~!_~~l Td.?T -
N/A 44/1 00 . -
CO (V be), % vol (dry) .N/A - 28/100
" +
02 (Vbd) ,% vol (dry) N/A 32/1 00. +
- .-- I
N2 (Vbe)' % vol (dry) N/A -. 28/100 +
0..
- -...... -. -Mbk = Av~ ~olccuJar wt
.. - -
N/A
, of dry stack gas= I
Qrsat Analys"Ls for Test - Haste and Burners (From bag sample)
Date Feb. 18, 1971
Sampling point location
Time 1110-1649 Run No. EDE-1
East Duct Exhaust
Analysis Analysis Analysis x = I "f7iflOIel
1 2 3 Avg mo 1 e \'It ( dry) I
C02 (Vbf) % vol (dry) 13.4 13.2 - 13.3 44/100 5.85
~ (Vbg)' % vol (dry) 0.0 0.0 - - 28/1 00 + O. 00
02 (Vbh), % vol (dry) 5.6 5.7 - c;.~ 32/100 + 1. 79
N2 (Vbi)' % vol (dry) 81.0 81.1 - 81.0 28/1 00 + ?? ~A
..
Hb. = Avg mol ecul ar "It of I 30.32
J dry stack gas = ~
,.
NCAP-22 (12/67)
B-5
'0 .
-------
, .
. Part 7, p. 1 of 2
OEPARTHEtlT OF HEflL Tii, EC~'I-.1;7iOil, AND \JELfARE
P:.Jb 1 i c I-!ea 1 th Serv; ce
National C0"ter for Air Pollution Control
FOR/.I /\PPP-OVED
BUDGET UUf
-------
. .
. Part 7, p. 1 of 2
DEPMlTl-iENT OF HEALTH t E;:;~',-.i;7l()il. AtJD \IELFI\RE
r~blic Health Service
National Center for Air Pollution Control
FORII f~PPROV[D
BUDGET BUT
-------
. '
. Part 7, p. 1 of 2
DEPMnr.iENT OF HEALTH, EC~'''./~7lO1I. f,rJD \IELFf'\RE
P;Jblic Health Service
National Cpnter for Air Pollution Control
FORI.! f\PPHOVED
BUDGET UU[
-------
. .
Part 7, p. 1 of 2
DEPMtTiiEtH OF HE/\LTH, E~::;.k;-l Oil. AtJD \IELr/\RE
r~blic Health Service
National C~nter for Air Pollution Control
FORI-J p,ppr;OVED
BUDGET UU;{Ef~U
NO.
APPROVflL EXPIRES
ORSAT DAT!I AND ClI.LCULATIOil SHEET
. r
Orsllt I\no1ysis - BU1:.ncr Only (From bag sample)
Sllmpling po)nt location
Date
Time
C02
CO (
°2 (
. N2 (
""fiI1a 1 ys is [-\na lys is Analysis x = \h/mo 1 e
. 1 2 3 I\vg mol e . \'/t (dry)
(Vbb)' % vo ,--( dry) -- -
44/1 00
-------.-..- --
V be)' X vol (dry) ' 28/100
. +
--
Vbd)' % vol (dry) 32/100. +
-----_.~.,- - -----
Vbe)' % vol (dry) 23/100 +
.- - -- ------
Mbk = flvg mo1ceu)ar wt
, of dry stack gas=
Orsat Analysis for Test - Waste and Burners (From bag sample)
Oate--Fe~ruary 20, 1971
Sampling point location
Time1335-1803
West Duct Exhaust
Run r~O. WDE-3
Analysis Analysis Analysis x = \'1 mo e
- 1" ' 2.-- - 3 Avg mol e \'/t (dry)
- _.
- -
C02 (Vbf) % vol (dry) 13.8 14.0 - 44/1 00
- 13.9 6.12
CO (Vb), % vol (dry) - - - - 28/100 :r -
9
02 (Vbh), % vol (dry) 5.4 5.2 - 5.3 32/1 00 + 1. 70
N2 (Vbi)' % vol (dry) 80.8 80.8 - 80.8 28/1 00 + 22.62
.. -
t/
Hb' = Avg molecular \'/t or! 30.4[;.
J dry stack gas =
NCJ\P-22 (12/67)
-------
APPENDIX C
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,J ~1M DIFF 8f BURNER TILT TIME OPERATING DATA,
'I } % A B HOURS TURB. BLR.
. .9 109 2- THIS MONTH ..42 44
I +30 TO +15
j 300 63' THIS YEAR 1170 116(
'[ +15 TO 0
;.5 6"c; 59 49655 475J~
o TO -15 I.) SINCE START
:l HT;; F2 11.1 -15 TO -30 '71 ,GROZS MWH THIS MO 10<:20
.,. HTR G2 1.8 ~9IUTES AUX. MNH TH!5 P,10 5~'f.
ILLINOIS POWER CO,ll,? A':-lY
WOOD RIVER PO','/£;:1 STI~.
HOURLY A:-1D DAILY LCG
UNIT 5 .::\
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rH.. T F=
0:2 :.0 71
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CONTROL ROOM DATA SHEETS
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5:001
t''', :f. n~: Po~_nt
.~I?L r;o"
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5:001 T 493
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:~15 'E 337
;:316 T 330
:mu 'r 339
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lO~5
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31 1025
31 1.025
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5n18 30il(;\1' - Unit 5 5B3S-
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51;124 T 322 Rehc&ter Outlet StC2am 'l'~et'a't:ur.f1 ()Tf 1025
::;~~~.F 313 Soot Blomtt;JSteem Plow f;/Rr:.. x 1000 1/:.5
3~26 '1' TSS Soot B10t1ing :!teGm Tcmpel"~tul:'a oj! 2903
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5B37
5n38
51139
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&,!1QT. - Unit 5
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2
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1.'
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Sl1pe;:ncat Real'.1Ior1z. Spc1J. Outlet :UU~6 ~)J.t'e Tcmporatm>J of
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51354
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5B5':- T 4.69
5B55 'E 470
5~S6 T. ~.71
51.157 T l)o72
5);)53 T f~73
5P:59 T 47/"
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5D51 T 730
5:C62 '!.' 731
5B63 :? 132
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Conden3~te t.o DC nQ3t~r
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35 130
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Co~donoate SY8~€~ " Uni~ 5
Description
. Condonsat
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5DOl Draft Syotem - Unit 5 Sn15
Point Foint lll~t'm L:tI:d.to
10 .50. .Descr.i.~tion Unito !1u1t. L~l-] 1Jl~!l
y-... -
5»01 T 568 SA F.D. Blowar Uotar Cutboa7.tl Boarlr-.g Temp. of 175
. .5n02 or 567 SA U.D. Bl01l01' fIotor Inboard Beaz1nB Tamp. of 170
5DOJ T 566 SA F.D. BloHS;: Inboaf:'d nCD.i~.ng T~mp. o!i' 150
5»Q4 T 565 SA P.D~ Blot'Tel' Ot.\tbosrd D~l.\r:.i.ng T.'~Tl1p . C'1)' 150
5D05 T 572 5D F.D. Dlower ~ctor OutuoDrd Bearing Temp. cl? ~.;O
5D06 T 571 5D P.D. 31ot:1~r. 110£:07: Inboard BG~~ing . TI?11l1). oJ! 170
5»07 l' 570 SB F.n. Dlower I11bo«u:d Bearing Temp. vJ! 120
5003 T 569 5B F.D. Bloiler Outboard Bearing Tenrt>. 0]:' 12Q
;:;009 T 31~ SA F.D. Blouer Inlet Temp.. 0" 32 119
I '.
j
5~1.0 '" 31.7 sa F.D. »loncl' Inlet Tem~.:i or: 32 H9
.1.-
,
, i
51)11 T 344 SA F.D. Blow~r Cutlet Temp. of 37~~
~iDJ.2 T 345 5B F.D. Blower Oatlot Tc~p. 0", 371~
I:
5D13P 631 SA P.D. Bl~er Discharge Frean. In. 1120 x .1 330
. L;1)14 P 632 513 F.D. Blovar DischarGe 12'rE;so. In. u 0 11: .1 3:!O
£°2
~D1J 674 Humidity. lbo. moist. I lb. Drl Air: x~OOOl 10 SO
(')
I
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-------
5916 Draft System - Unit 5 5D~O
l'oint ro1nt AlBro Lirdt~
.m .' 130. Desc.!;}."pt:i.op 17~ ~.2!!.:. .l~?3~ ~. .
" ~: '2:f.Q
-
. 5D16 T 3l.6 sA Air Heater Air In 'Emp. 0U 37l).
5D17 T 'jl~ 7 SI Air BaatG~ Air In Temp. 01] :;,'''-
.5»18 348 SA Air Heeter Air Out I 619
T TCinp. 0'!I
5D1.9 T 349 S8 Air J:Ie4tor J~ir Cut T~Jlp. oJ! 619
5D20 P 633 Furnace Wa9t t.rindbox Fr-cas.. Xn. 1.120 x.l :If-1Q
5D21 1:» 634 Furnac.t! Eaot tUndbo:t FraGO. I In. i!ZO :t. J. 0 230
5D22 T 350 SA J!um.:lC4a Gms Temp. (Pr.obe) 0D' '-CO!
5D23 T 133 53 Furnace Gas Temp ~ {l?;:obe) of lGJ)l
52)2l~ P 635 ~ Furnaco Prcso. "1~.... n....o x.l \) ~co
.::. io'. "
c.
~!1~2S P 636 5:0 FUi'l'lace Pr0se. .1.11. U?v 2~.1 210
<.,
I
!;D26 T 351 SAPand. PJl Gas Outlet T~.. cLi :n 1151
5D27 ')~ 73!~ S13 Pcn:1. 1m Gn:J Out Temp. 0p 31 17~~.
5:028 1? 637 SA Prim. Superhaster GaG in r>ras&i. Iu.. H20 2t.l 19Q
.~n29P 740 SB rdJDa Supel'hcntQr Gas in Pl"eso. - 7120 n..l lG5
.~11o
:;:;)30 'Z 352 SA Xeon. G~s Inlet Tei:ip. c... 330 !);!,
~:
(')
I
W
-------
S~)31 D:t:cft: Syat~ - Un;.t 5 5D~5
Point Point Alai:'(.' l.:~.<';)1.1:. a
:m ::70# "~Gc!:"..Et1.ol1 l.!nitf}. lJ~1& ~ .llt;sl!
.....--...- ....------ -.....-
5D31 T 735 SB Econ. GaD. ltilet '.Temp. OF 33 99l~
J
5D32 it 71.1 SA Beon. Ga.s Inlet PrC3~. In. "'/0 It .1 110
1:.
~;)33 P 7l:,2 5B Ikon. GaD InlGt Fi:'css. In.. H20 , 1t .1 170
5/)3l:, 'r 353 5,,'}, Beon. Gas OUt TGil1p. or! 31 7(~9
,';:l35 .T '136 5» Beon. Gaa Out Temp. Or.'! 31 7[/";
..'
5D3~ r 6:18 S.\ Econ. Gl!9 out 1n:'ess. lrt. n20 -r .1 If:,O
..
5r.t37 P .7lt.3 5B leoD. Gas OUt Pr.OS3. In., H20 x .1 JAO
,
.')~)38 675 O:tygen in FlueGss I % x .1 29
I
"
5D39 67(& Combustible ~ OJ 41: .1 0 10
i ..,
5Dl~O T 351.. SA Air. RelAter G~a Out Tomp,. of 249 320
:11141 T 355 sn Air IIe~t~;.: G~s' Out 'L'eir9. 0y 21.:.9 359
.:Dl)2 p '639 SA Air Heater'GaG Out Pre6SJ. In. IIZO 1:: .1 0 70
,51)(:.3 P . 64Q 5B Air lIeateI' Gaa. Out PZ-CS9. In,; n"o ~[ .1 0 70
/.
5DM~ p 6cU SA Dust Collector Outlet Pr:SSD. In. U...O ~ .1 0 20
J.
51J1~5. '"f ,6{~2 SB Dunt Collector Out10t Pra~~. In. H"O x .1 ZO
~.
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I
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-------
SD '.6 Drf.lft Zy;;,tfl..li1 - Unit 5 5J59
Point Point Aloi'm I,~~iil:l. t s
--I!L NI>. Dssc1:'1pt:1.on l!.f.I.:li!l !t.tJJ:.~ ~ IH$h
---...-
5D46 0 l~
5~4.7 0 I)
51).47 0 t~
r:~/.C. 0 l)
"'~::J-...~I
;ij)~ 9 0 t}
5I150 P .r.. SA Fttii:'ll. to P:d sa Inlet D:I.:::£. "H20 j; .1 0 ~'.."t:
..
5D51 p * 5B Furno to Pri. SB Inlet D:UL lip 0 ~ .1 0 ..::~~
t? .
5n52 p ~'t 5..'\. Pri 511 Diffo liH20 x .1 0 ..:;..:
.,
:3~:} 5. J P -:: 5A Pr.:t SIT m.ff. , "rbO :lC .1 0 ....:~Y.:
i
:1j)5!~ p "" SA Reon. D:1.ffo Ill-I 0 x ~ 0 ..~...
.. .....
2 0"
~~"i: 5:~ 'j .:: 5B Beon. Diff. "il;!O 1: .1 0 .":~':
i.
5DSf; P. ..~ 5l\ Ail' I-Itl'. Diff. (Gas 0ide) "U?O -. .1 0 ...:..'~
.~
;:~57 Ii ~ !in Ab' Ii tr. D1ff. (Gas Side) "H20 ;( .1 0 ~'...".
...
~:.~'.5D l1 ..":. S~\ i}1.3::i t Col.. ri1f~. uH2Q -~ .1 0 ';"....::
.. ...
:?)59 l' * 53 Dust Co. Diff. "lbO x .1 0 i;..-:
Co
~./
C~lcv.latcd Vnluo
()
I
W
~
.....~C
-------
4
5~Ol
faint Point
.JJL ~-
SEol T 519
51':02 T 520
Sr::03 T 521
~Z(}~~ or 52?
5f'~1' '" 523
.:t'..,> ..
S;~Q 6 r~:. 52,..
5EOi 'E s:n
!?:ea'T r?n
..")_t4-
5209 T 533
5'nO 'l' 53.!~
:mU ;) 627
~
:;;~12 '1" 525
'-
5k":13 T 526
;~,::14 X 527
5~15 '" 528
.;.
5;::1..6 T 529
S~1107 'r 530
o
I
(,a)
U1
Ganezntor & Eiectrical Gyatem- UDit 5
Ih:!8c.:~.t) t1.0\:1
...-..-_..._--~
tiP Generator Statol;' ' ?.r;"if}:?Ct\."-.:.ture I."o:tut i
HI' G9nereto~ qtator Tcmpcrqtu;:0 roint '.
~
NP Geuere.t:OJ: Stator ~:~~r~~f~ratU1:(} FoLnt "1.
~
nt' G::'Ii1ol'ator Str.to1: T0wp~:i:.:1~:U::c
Po~.r~t; l:.
"
iW GQnci:~to1: 5tlltO:-:
TempC:;~;:'t~1~~
Po~.12t 5
liP Gouara.to~ Seator T.empezoa:tm:e T?ol:n i: U'
.
UP Generator nydt'oge~ Te::;\?m~''i!l.'"tJt'c k.w.'tJb:::: CQolo?: Ko. 1
HP GtZiR0E'Ator HYf..1rQgon
Tt~::.t>a~"'at1~1:C
I.c~~;vJl~[~
(:01):1.0r
1:0 ., :~~
.
U? GenoratorBydrcgQD Tcm~a~4bl~C teavi»r, Co~lc~ lio. 3
:;
D~ Genc~~t~~ Eyurogc~ T~mYF~~t~~~
laJcnv1.rig
R~ GGnQr~tor BYdy.ogon'Pr~Qcure
l,p Gez;.erator: St:~..tOi': 'lcmi?C1:8tm:e ro~.ut 1.
tP Gen~rator Stator Tempcr.aturo roint 2
LP Generator Stator '.['~pe:'{\tui:~ !'Q;:.flt 3
LP G!1n!aI'atol" Stator Tcmpe;rli1tura .Po:f.nC 4
!.P (;ei£Qrator StacGr T£IDilCZ'.:ltuI'0 r'o:l.nt 5
LP G~nerator Stator Tcmpar01wl'e PoinC 6
<:,1)010.: No. I,
.llil:~.~r:
;:\c
°c
o~
.~,
0(;
Ce
°c
°c
Cc
0(;
C'C
PSI
DC
°c
0(;
°r
...
C."
-v
0(;
5"'- ...
_",1/
Mnlt~
/\J ,~i.li\
7}.!_t~!.:::\
1::!2!.
Iil.-~~~
n~
:'.1.
Q';
" ..
n
P.,
... -.
?1
01
," J.
'}.. 1:.5
,.1
27 45
21 . {~5
'r' t~3
...1
X .1 65 35J
Sf.
91,
9J.
9l
n~
:J /..
-------
:m18
:fc:'f.nt
..,.ZL
Point
NOe
--
5318 'f 535
SfU9 't 536
53'-0 ~ 537
~1~2J. "£ 5JU
~~22 r 623
5E?3 V 2SS
5E~4 U 258
5r~2S R 259
~1'~:2 6 A 260
~~:!.7 l~ 26t!.
5.Ei;S ~v 219
5~29 a 270
5;?-30 H 269
3;~:;1 V 211
r.~"..~"" i~ 272
.I~,:'~
~if.':33 l-:. 273
!:'i:::3l. A :~7l)
5~35 A 215
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Gc:nc~ato~ & Elcct~ic~l Syot~~ " Unit 5
. QQfT£1:b'2!~ .
Ll' C~ncrQtor Bydv-v1.';Cil T~pe;:at:c.e:o ~a".1:hV3 Coolor j~Oa 1
lJ,J Gen0~e.tor nydrogQn 'Ecmpawl.ttlJ:0 I~n...rif~Z CcolcA' p.~)o 2
LP Gen~r.Btor. Hydrogen T~pm(,:1tui'e Lfi}n.'.1i¥"~ CQolor I~oo 3
L~ {~3U~r&tor Byc1~gwn
Lc3vi~g C~olQ& No. ~
Tcmpc-;;stu.::a
LP. C~~rQtor Hydrogen P:;-oc;.:..\i'C
G!s.ma.:.s1tgr. VolcagG
G~oss G~ration ~ Mesm~Qtt3
Gross Output - Mogavars
ill? Ggueracor &lpct"es
I,P GOIlG1I"3tor JI.,mpGrea
Coal 't1&1dling tnad
:!
., .
. .
I
Aux11ia~y i~ar~formar Lo~d
RCDCr.vQ AuXil!a~y TrDncfolirtO~ to~d
4160 Volt BUD SA Volt.age
4160 Volt BU3 5~ vnlc~u~
4160 Voit Bus SA t-1.~in 1'~'t\Pa!"ras .
.4160 Volt }juo 5B ~:1f.n A~1pcr0a
4160 Volt tius SA Romel~ Amp~r~8
Urd.t8
. --=.-~
0(;
0'"
'V
c.,.,
..,
')G
~81
P'U .
...~'J
tom
H\i.~R
A'.il~)O
A:1':.pn
?.r..;
":,'.J.
i-~:1
l0j
~~v
r~;J
J.j~i1p f}
A\;1~'S
l~\7,?c
5335
.w.11 t.
l\l.3E'i'l l.in! t8
~~~2~
!~!r;!~
21
27
2:P
27
... .1 65
~
.. .1 0
~.
x .1
-s
(i
o
x .1
x or
...
x .1
x .J.
3 .1
45
~5
1~5
1~5
:~5fJ
;:H
3852
3!J7
6lJ.G6
G7(10
-32
2!fO
1.:%
t:l?
. .
l:Jj
1150
'.15Q
-------
5E3G
!o1ut Fo1.nt
JdL: No..
- -618
5236 A 216
S!<37 'E 539
5~3S V 262
5339 A 263
.53/joO V 2()]
51~l>1 A 268
5!.;'~:-2 a 265
5T!.l:.3 !t 266
:;l~l:L~ . 'i' 193
5::.:4.5 T 7St.}
r:r.-J... t:. 1: 795
~Ji:"'''''\,,;i
5:~;!:.i T 79()
~~~~.G T -0-
1,1
5;:!:.9 'l' 79D
5~!:-o T 799
5~~;1~.
~r52
.5Jt5 3
0
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Generator & Bioct~icel ~ysteM - Unit 5
P~~!;ip_~~,2.~
92.:1. t~
4160 Volt Bus SB ReoQF.vo t~p~r~a
lU;:tp 9
~!ain Power Transfoxmer Rotspot
0(;
UP Generator Fiala VoltQ3c.
Volt::!
RP Generator Field ~mpcreG
LP ~snc~ator Pield Voltage
[;:;:~~a
Voli.:G
Ll'.Gcntilrator Field Lunpc!'es
t~~'Jpa
LP G(1ucrator Output .. (.lcg~r;l~t:':fl
r;i.~~
L'P. G~n6)rator Output.. Nogt\va.::s
r:~i'f~lt
UP Exciter O. D. D~ar.ii1g Oil J)):aiD 'l'emperat:m:c
O!-1
,.
- I
i
n~ Ehcitcr Air Out Tcmpa~a~ure
:'
°c
- - .
m' I);;citcr :&::UGl1 Rigging' rl~~ldor Tcui'c~at~,:;;:
G;-.
'V
ID1 E1tc:l.ter O. B. 13011;:1ng Drain - Tem:}(~l:l1tm:c
o~
t!! E~;c1tGr I.B. D23~ing Oil Dx-niu 'fompcrc.tm:c
OJ!
LP na~1t:er Ai~ Out TC'.ii1perature
ClC
tP Exciter Bru5h Rigging Bolder T~~paratu~e
CiC
1£:lh
~; .1
/!.l.':'\T.w
1£51
o
o
o
o
c
-25
...
5~~!i3
I.im:1.. t f!
;!;~":~:I~
1150
106
37G
u:oo
37G
123!J
~:;:co
153
1 ....,"
...J~)
r,;~
vI.
1'1
lSS
15J
In.
71
l~
4
-------
5ES4
~~;tl1f.:
Tn
-:.:...---
5~54
5~SS T
5P.56 T
Point.
1!!oo
LI .....-
~
-::
G~ner~tor ~ Electrical System - Unit S
Descript:1oi'\ .
!!~
B.P. Generator Rotor ~"'ipQ~aturG
°c
L.P. GenGrator Rotor Temperature
°c
*C~lculated Value
n
I
W
CD
Unl t.
-...---...
Sf-56
A:irJ}:m i!:l:mitG
1E:~
!H~h
~.
".'
o
gO
o
-------
51701
Point ro1.nt
ID No.
51;>01 F 302
51"02 T 782
5jf03F 303
SF04 'f 783
5F05 F 3!)!~
5F06 F 78l~
5'!JOl T! 305
5:{;'08 T 185
.,PCJ9 1! 306
.:;~.' 10 T 186
.51711 F 312
SI(t2 P 655
51"13 P 656
Sr!ll;. 16t.~
.'::ns 775
5li'16 l' 573
5"J17 T 574
o
I
W
\0
Fuel System - Unit S
DOACr)_p ti~!!
SA, Mill Coal Flot'l
5...\ Mill Outlot Teperature
SA Mill Coal T!lotl7
, 5B Mill Outlet Ta1!.po~attt1:e
5C Mill Coal Flow
5C Mill Outict r.rc:mpC7:fltu!'e I
5D Mill Cosl P10\11
5D Mill Outlet Tempoxatu~e
5~ Mill Co~l Fl~~
.
.
I
5J~ Nill Cutlc,t TampCl'fitm~e:,
Ignition 011 PlON
,
, i
Ignition Oil Supply rA~O~r.C
Wa~ Up Oil Pressure
SA EU1.uQr Tilt F08iticn
SB BU:Lil~'f: Tilt Poolticn
5A hiv. Gear CaS(/! Oil Tcu:porll.ture
SA Pulv. Kotoi Inboard !}aarh,13 Tcroper.9.tur.a
!!;llli
TonfJ/nr.
°l~
Tel;:?s/!lr. .
O]!
Tons;Ht.
0.,-"
TO:1s/u): .
~
Tons/n;:.
o'!?
G~"U
1>:n
1'~;1
(bG.
d~G.
OJ!
OF
Mul t.
SFl7
Alarm LimitE;
1,0\-7 'fl1.~h
-- --~
o
42
'170
.0
l~2
170
o
42
1.70
o
f. .',
'{.,
170
o
1.:.2
1.1'\;
5
49
. 5
1/:0
5
95
-30
~o
-30
~{}
13,)
-------
510'18 J!uel Syst
-------
SFOl
~;Q:l.i1t
It>
--
srOl P
5I!02 T
51'03 T
SPO!:. T
ji?05 T
51:06 T
.5P07 T
5!?08 ]:'
:;f09 T "
~'ij~lO T
5::11 T
~:;:n 2 l'
5;;"113 1.1
:J~;:14 T
!i~15 f!
:"iJ;'!6
'jl?17
n
I
~
....
Faint
No.
657
324
326
753
323
325
752
309
1l.~9
750
15;
630
303
75J.
307
6i1
679
Miecellaneous rlant Valves - Unit S
})esc.ri~~
~
Control Air Pressure
P3I
Circulating Uater Inlet TCffiPotatuze - Eeet
OF
Circulating Wator Outlet Tcmpo~acu~a - East
0p
C1rcul&tiDg Water Outlot Tero?CLa~ur.e - ~e.~t
0,..
::
Circulating .Water Inlet Tcmr>b>:
-------
5P18
~.:)int Point
~rtL Ito.
-
51'18 P 169
.Sll19 P 670
511'20
5I?21
()
I
~
N
ServicQ Water Prossure
Barometric treasure
aZ14 Statton Net Generation)
)
).
)
)
. 81.\15 un Intorc:hanza 'o-~t
I
8RlG UE IntarchQuse In
'0
Miscellaneous Plant Valveo .' Unit 5
. De&criptio~
It" x2l~OO
Printed out
Hourly
K~f :
-------
51:0).
Point
ID
S'f01 T
51.'02 P
5T03 P
5TOl) T
5T05 T
5'l'OS T
Point.
No.
318
603
60iJ.
115
716
717
Sr.t,'07't. . 718
51:08 T .
5'1'09 T
5'.1.'10 T
5TllT
5'1'12 T
:iT!3 P
:)J?14. or
STl5 P
o
I
0l=Io
w
719
720
721
75t{.
716
605
319
606
Turbin~ Cycle - Unit 5
D2Dcriptiou
!i~~. ts
_in Steam Temp. at Tl!t'bin~
OF
Main Steam Pressuro at: TUl'bine
rSi
Steam Cheat Inlot PreRoure
)":'31
UP Turbine First Stage Inne1.' ~h.~il
.. t.:to';'iCl:
0lj'
1W TurbinG Firat Stago Ot\tcr Shell ~ LO':ier
'Stop Va.lve .'1 .. Above SQat Inn~r SUi:f:acc
I
Or:
OF.
. ,
Stop V41ve 11 - Above SC3t' ,Oute.r SurfacG
OF
Steam Chest Outer Surfl1c~
OF
Ste3m Chest Ilmer Surface
OF
Exbaua t Hood .TetP.p,,'
.
I
,
c.
~
:;
.
8tbStngo ~~~cl Gpace Tem~.
CI1
1st Stage Center of Ha.. .
0;:
First Staae ~esBure
l13~
Cold Reheat ".fc::!m? at Turbine
OF
Cold R.ebeat PrseSU1:'e at Turbine
PSI
It'ul t.
5'£15
t~3't-:
-....".-
t..l:lt:l.i 1..wi to
]11£~
"'.,.
:'1.
:n
33.
31
31
3!
31
31
~l"''','
2.!;. ~
1071
2073
2201
1020
1001
1On.
1071
1071
1071'
160
'9;;0
1\iOl
.;.--::
729
-------
5';£46
!.:,') !nt Point
!T.) N:')~
~--4A. ~-
5,:46 T 723
STt.:.] T 72l~
5T48 T. 725
5'1'49 T 538
51:50 T .SG9
;liSl '1' 590
5t~S2 T 591
5T537 60D
':'T5!. '!' 601
S'r5S T 126
5'1'56 T 727
ST57 T 728
::.'£56 'i' 729
.:;'I59 'J: 595
':;-:;60 T 596
o
I
110
110
Turbiue CyclQ - Unit 5
De r:c?':7:~t~.o~
~_..~.~~,--
UP Turbine '!:i:n.:t.mt ~~ei::al T'~::p.
tIP Tlitb1ne 'ih~ust Bearing Oi1.
D~'~in
F.P 'D.Jrb:ln~ Throat Bo~::~.n~ on n~:.\~,n
UP . Turbine No.1 BC2aring on. Drf.1~.n TC:TI~.
. I
itP Turoin~ t~o. 2 Dearing Oil Dra:i.R T/~7"o1p.'
HP 'lurbina No.3 Daaring Oil Dr~in Te::l?o
UP Tu>:b1ne tJo.4Bcnring Oil D!:'<1:f.a TeJ.i1l>.
L.? Turbino thruat B~Gring nuxp.
. . I
LP Turbina
:;
thrust De.:u:iri;j T.emp.
. i
Throat ~~t~l 'l~..,.
r.... T\\rblutn
12 'l'ul'b1.na Tl\:i:'UQt !-1$1tal T~l'.
L1' Tu!:'bice 'Xhruat DQaring 011 Drain
t.P Turbin~ 'lh1'Uot )Waring 011 Drciu
LP Turbiu~ N~. 1 Baaril16 011 Drain Tc&p.
LP Tu.bina Ro. 2 Bearing Oil Drain T~r>.
1\).,') ::'"1l1
QaJ.J:l:.
t "-.r.'"
.~... -~
-~~
OF
OF
0,.,
I:
O'f:I
.:
A,-
"".1~
OF
c.,
!.'
OIl
a}!
OF
Of!
CJ'J!
o~?
O"i'i1
t.
°11
5'1'60
1,:i..rn:t t r;
. ":,"f.. ~::...
~;;;.::~:;;:...
170
155
155
155
155
155
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170
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170
155
155
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k~o:~nt
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l'oj.nt
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'1,,1 " 1~ 506
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jJ:17 p. 621
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f: r-t-,,, i' 79J.
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T.urbine Cyclo - Unit 5
D~$c~'j.f1 t1.on
-=-~'-_1: --~-...
Extraction Ste~m Temp. to ~G liaaters
St(2~m J?1.'6'tzzm:c to. 5G E:~
-------
51.'31
r\;~_~\t
.7aL~
51'3'- T
5'1'32 P
51:33 'F.
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61,)9
765
629
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161
762
659
518
601
662
593
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722
Turbine Cycle... Unit 5
lk:~s~2.~-
Extraction Steam T~~. to ~~ BoatGA
Ste.:m 1':':c@l)ur.e to SA ncet~r
L~ Tf.~t;b:ht3 i::~rh~u3t - Teriip.
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CondonHe~ Ba~k P~~8GUra
Ccndensar B~ck ~rQ~~urQ
Co!dm:moz." Badt {>;rcssu1:a
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TUr.bi~a Oil T.~~p. f~om Oil.Coolor
Tm:b1no H;..'f1Z'r.~~Hc Oil rh"~COUF.'G;
Tu~~in~ Ec~r1ng Oil FressuAo
m.~ Turbi&t1 'l'af:..'fjt B@orinB
'l'Cwpo
HP T.~rb!n~ Th~ust B~aring T.~mp.
:a? Turbinq: 'Thi'U;"~ Uet~l Temp.
1~~~~ ri'l.11t.
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170
170
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51'63
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1,.1' Turbine Hoo 3 Boa;:!n:; Oil DJ:Iil~l) T£Ei,p.
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Temp 0 D1f1:.. Pj.r3t S t..'1ge Sholl QutGJ: .. CcnC~r of U'AS9
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~ h(J 11 II l,{}t.o l'
RIJ:a of C~~!!ZC of Temp., 1& 'It'.rM.D$ Pirct S(:(:3e Ot.\tnr
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FecawLlter Syat~a - Un1 t 5
Desc::1pUcn
Gland Se~l Water to BFr
BF~ T~rbine SA nr Stop V31vc Ou~e~ ~Qt31
n~~ TurbiD~ SA Gland GtcaQ Vrcosure
llFP '1'ui:M.t:1~ 5A Eydra\~Hc on i're::}3\u:e
E~? Turbiac SA Dca~ing Oil 0
nIoT !\\~binQ SA Oil teaving Cooler
Err T;.H'M.n~ 51'.. t~ctive ~\h~H)t r1.e~al
l'~i,p .
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Df? SA Bcariug Oi1 ~roQsU.G
EFP SA Inbol.'!.):d Bec.::1n3 ''ct:'.mp.
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Deoc7.'iption '
B1i'P SA Spaad
BFr TU1:t>:2.!1e 5.~, B~,.,l 1(4CGCl!~e
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5B Sto~ VDlvo Ou~c~ ~~t~l
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BPr Turbine 5B Dear.inZ Oil Pres3u~e
DFP T~3~bi~Q 5B Oil 1~£viQ8 C~Q1Gr
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,
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620 StQQIl Prcno. f~am 513 Bl1'l'T to SF BcctGt"o 1:31 0
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610 Ste;;im Presso to 5I" Ul':Jtlt~ra 'tiS'i.
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5rJ.'~i i? 616
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DT to 5!! Heatcr.
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Ste~w T~mp. to 5~ E~ate~
SeeGm P~cG~urG to 5B ECfitc~
UQatina Ster~ ~lo~
Dp~ting StQ~i ~re$Gure
l:c~ting Stearn ~emp.
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Stc~m Tempo f~~~ 53 BFr-L to 5D n~3ter
Stoam Prc$o. f~cm 5n BFFX to SD ae~ter
Scellm temp. to t1r.H!tar 5D
Staam rAe~a. to iloa~er 5D
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.. Arcn 83 Rl«:r.tdcal (32 V41ucl)
Iotem.} Location htemal Suh DMc:r1pt1on Unitt; HultipU.or Input. Type of
Iud.: P'llD PTID Value.
n?A). 219 333 8EOl B9 Aux., Tr8not. LOAd. m; .' I' 5El9 lIr. Intcg.
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224 3.40. 8EOu Gr033 Output ~~g6var5, MVAR 5E25 " "
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232 360 8114 S;'8re
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CALCULATED VALU2 TABLE (Continued)
Loc.et1ou Extr:roal Scal~ Dcacdption Unitt HultipU.or IDput T:;po cf
PI'ID Fl'ID Vduo
355 8119 D12 H.P. Gt;n. HydrogC!ln PrB:28., PSI DV(.' X 10 SBll 3 tU.n.. Ava.
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360 8~22 .£.2; 'Tot~l Gcno~ator Loo~c~. H!~: EQ STn. It II
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362 8E24 [' 1- WiG Chec!t,! MW
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363 SE25 Hourly I.,
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3114 8E26 L/ L t10et Out!,ut D~l1y KW II t f
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366 . 8Ela .r~ 5;.r.:;;8 I\,' ,
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3TU 3~?,o GXOS8 G~n Qtttput Monthly, '-- M'ii 1 " "
371 "r.~, Lo~' Lond LoS - Lo"~ Point, r!W D~ta IMC!rt
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arOj ~A2 Cold RH At 4urb, 'r~p up 51'14 . 3 11161. Ava.
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1.') 25/Y 376
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16
CALCULATED VALUR TABLE (Continued)
rl-,t~rl1~l Locnt:to~ K::tc::nal S calQ P~3cl"ipt1oJl Un1t8 Multiplier Inpu t Type of
Xudox P'£!.D PTID Value
( 255 '177 Oro5 B9 LP Tuhb Em. !B. P.) Pr('.m~ "HgA X 10 5T34 3 HiD. Avg.
J 256 400 aT06 \lond. lI~ck })J:"/.I8IH\ rft "HgA X 10 5T35 " " II
14 \
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l ::::n {~OZ ArOe " tI " " X 10 5T37 II " II
T':( Z :,(, 40) f, ~'O ') au '. ~ "ruTh. Exn01uo t T<1111p., ~ of 5T21 " " tI
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J"9 ~'h.i 1,04 f\J'lO 1, P T\.1~h. 1:1\~t: Pr~':\n. P~n: SI22 " " II
O::7i\'X /.6'1 {}05 STn ~X( St1:! ~o Ut.n, !jG] &. 5G2 l~?'J of ST16 " II "
'rPB'X Z~2 !~06 (1,T12 5:rU "".r\~.f'~t To Ht¥!). 5Gl & .~(;2 Pt'~:~o PSI 5T17 II " II
.
t.; r:~ x "n', ';07 :;'r' .:: P.:t t. ;:\ fro ;t(\ 1'~ t l' 5D '): r<,,1lp. Up 5T23 " II It
\,". j
~.r[:2 X " .., \),0 ~~T14 5tm :~Z}.:; .It: 10 ~T) htt', rr~_'Hj.. WX ST24 It " II
6.'(! ., ...,
I
,,-r£.3X :/,6) 1;/1 i;'XU E:o:~ 3 ti..\ .ro ft, :>C T~in~~) A " OF 5T25 " ,, ' ,II
~:C~ 1 x ?('f. (, i 1 a-':'6 Er.t St;I\t 1." H::,' 5C x."J:t{~.:!;"f r;) PSI ,I..": i.. X 10 51'26 " " "
';-J.1-I ~ lX :i:(~i I~' 3 ::",''{ 7 BJ:t ~rLZJ '10 Ilt:" 5C 'r~t\:?, OF 51'27 " " "
~P33 i,X 26,~ /) ~ 4 ':)'\,,#1 ~ (;ry '.ut~~ 10 HI:'1.' 5r. P;(~.1D, PSI I..' X 10 5T28 u II U
'" ,(., 'J
':'-'j',r:4X ) ( .0, I. ".s ~T1" F."'.~(: ~:: .~:... 1'0 lH:-=: ~., rlt:mL"" of 5T29 " " II
._v .'~
-'.. ~ 1~;)~.. X ;; .1 i) :, :, () ;".'720 :,; ta .~ t; ,~ ..~. :ro ric~ ~r. V,.,1~,~ h~J X 10 jT30 " II "
"";',G5X ';.{l ;. ~ 7 1~',~-..2'~ ~':'i..t. :~ ;~~, ~tu l!!: r~ 51. 'r("';~p.. -, "r 5T31 It " "
"'~;"}J~X 212 '+20 8'.11.2 St;n1 TuJlltt "'0 Hr.r ~A l~~~.('~r....- "Ug "v& x 10 5T32 " " "
,
2.73 421 h'_;'2'~ ;, }oIl Xl1 ~ S t41~;O P A'''! " I;&. , PSI 51'13 It " "
()
I
~
~
-------
1,
CALCULATED V ALU~ 1M\l.,E (Contiuued)
I:!t~rnal Locat1ou Bxtom:11 Seal.. ' J>."
i tm5 2&9 441 8'r39 BiZ LoP. Tut'b r,=:~ To lltr SA Flow (~ '. ~.J/mt EQ 5T)'7 II I /
I , 5'
;
i I
i Wu. 2~~ 442 8T40 B12 Cold &.5. FJ.owTo BI1F l\n:b A 6 B M~/lIR EQ STo tI .
F4 291 443 8T41 B9 J..vg. Back PraDo. tiJ1&.,'\ 'I j ) P4 II j Ii;. 1'/
" ,
()
I
0\
W
-------
.!.if
I CALCU1_UED VALUE TI\ilLB {Continued)
I
~ InternaJ. Location Eztfl1."DQl SeAl. D~:1('rj.pt'ton Units Multipli p.r :input: T;-p-! of
~
a lndt\~ FrID PTIt> V IlJ.UO
~j
~ B'. 292 444 8142 812 Md.n Stm EI1thalp~f h1 Ca}c
v
~
I I
H3 293 445 6T43 I Hot RU St;tn Znthdpy 11) II
"
~ B2 294 446 8'(44 CoJ.d rul Gtli1 RntbaJ.pr -h2 "
!
t1 89 295 447 8145 Cr.ORGOVOr Entt;ol?y ... II
~ 1 "!J
~~ 64 :l96 450 B~'iJ (, Vl.RP EQ 51'20 " : .I
r]
~" 2C)]' 451 8T41 819 Turl> Opel' HrR. INB >10 lffi$ Mont.h To D:lt:e
I)
~'
q 298 l~ '12 6r4~ B~9 II II II II YfI:!T U};S Yr.a~ 1'0 D1!\te
'.'
~i
!.; 299 453 BT49 &'.9 II " I' S ~.n~4 Sti\1.'t l;P.S Start 'fa D~te
r'1
~..i
~ 1 1)~Q ac Cond4'lD!1.11t".' :.29 V"'U"8~
i :
["J .
v:~ ;'I/~.-',;- ,.
~ ": t:~:n.. JOO 454 BCOl 812 Couc.hw1',u DC Ht1" Plow t1~;1-m 5C17 Ht" Xnteg
,'II To 1/1000
. ,
::1
,', \iDe 301 4'5 ~~O7: BU RT~ 5C Dxoo:1n Flo'if 1iJIP.R 1/100 5ell " It
i :
" 'f
~ . J
~., "j ~!" JHR .. It I'
,! ~r.f 3.02 456 fiCO 1 B12 M.a.I:.- A- U p Flow 1/100 .sCOl
i :1
~ i VIR 303 457. 8C04 »'.2 Spill F10"or1 KQ/l~ll 1/100 5C03 " "
..
'!.'~C ;-.04 460 ei.~05 B12 Cone. From Uotw~J1 T~ap,. of 5C04 3 H1n. Avg.
I
) I
P4C ~~ 461 8C06 I CClI' d~t' '\, t". H~"":"T r1~ jf'{:; r; . . PSr. seas " II II
I
:.i I
'l'5 306 462 8C07 Cond 1'0 Ht:: ~i.. l"'~p.. ;Jr' SC06 " " "
i I
7.5" Z07 463 scos Cond 1~ :-0::1 Iff:. ~ oIl 5C06 II II II
1 51\ Tamp."
(IF -'CIa " 11 "
TSB zon 46l; aC09 Cond To UtI' 5C T(>mp. J
~()
; I
:0'1
-------
t1
.i
.
CALCULATED VAlUE T.\nLE (COla; 1f\ued)
.!
Intornal LocaUoza hteraal Scale D~ecdpt1oD ~.:;.~~. Multipl1er Input. T.'.p'-" of
.1
i !udox nIl) PTiD VlI1ue
f
:1
'I T5e 309 465 8CIO au Cond FJ'om Htr 5C l'CliAp. I 0..,. 5r.~? 3 ~U.n. It.vg,
;t
:J .
ti T5D 310 466 8Cll CODd To Htr 5D T«ep., ~F 5C14 " " ..
; .~ TSZ 31.1 467 sell ('.and P~Cl'l Ht 1.' 5D T-cp.. of 5C16 " " "
"
p
~:
q 1'6 312 411) aC13 CoRd F1"Ol1J Htr iR ':t"'1llp,. of .5C19 II " tI
;,
I:
:; f6 313 471 8C14 D!"P S\1Cft.~on rtc;JJJt. PST 5ClO II II "
!.:
i: "
:: I
n IIl\ 314 472 aclS lItX' SA uA:dn 1'mup,. of 5C07 " " '1
t;
~ i
11 :rDB 315 (.73 SCl6 Uti' Sf, l)-;:'i\tn l'n~? \, 0p 5C09 " " "
n TOO 316 414 8C17 Btr 5C Dt."aL) 'l\~"P.. v}, SCll " " "
Ii CJF
." 'ruD 311 475 gC18 lU:r 5ri I'I17ahi T~.. 5C15 II II II
t'
l ~
I, I
.;
,{ 'n1 318 476 8C19 l'U\kt~ Up 'I emp . . of SeD2 II " It
:.'
,. ..:) '-:~ ' ,
,
q b'1: 319 477 BC2~ DC Htr Stanga T£nk L~;;cl Ft. X 10 5C18 II II II
.1 m~CA 320 5\10 8C21 HtT. .5.\ Dr. Cooler T.D of DHCA Cnlc.
. 'r,!
,i J:.
'j if'';~ 321 501 8C22 " 55 " " rr tt DNCfi II
~
,~
'4 DNce 322 S02 8C23 " SC " " " " DtiCC "
"
; ..
\ IniCD 323 503 6Cl4 .1 5D H " " " D1iCl> II
"
1 324 3C25 lttr' SA 'If: ),U{,M ). of
g '1':14\ 504 J I'Iiff Ti'!A "
~
} 11m 325 505 8C~6 I " SE " If II TIm "
,
~ -n:c 326 506 GC2l .. SC :1 ., Ii 'mc II
I ...
t
~()
a I
.0'\
-------
.
r.. CALCULATED V&\LUZ TABLE {Conrinu8d)
~!
t,
U Internal LocatioD Ixt~mal Scal" Dfltlcdpt10D Un! to r1u'-t i.plier Input Typ*' of
.'( Inda:x n1D PT!D Vtt!tle
L
, of
t'; '1'HD 327 So7 8C28 812 Htr. 5D Tarm1unl Diff TIm 'Calc "j
ii "'".(
[.:; .t
rj
~ 328 510 8C29
r,
f; Ar.cu! ail Fco;;n,aUr
~ W3!-fS R 32~ 511 B't10 1 IH2 Fe4watRT.TO nou pr FJ "'I MV!PR 1/1000 5W63 Hr. IutaS'
I'
~ "'4~ 330 512 H'/lm 1/100
! ''U¥ SW02 B12 s. H. Spr~y W~tGr ?1ow 5\0161 " "
t:I"L ~:n S1.3 81-:03 '812 It. H. . SpJ"AY \-lato):' F},ow J!~ ~Im 1/100 5H62 II II
--
332 514 aW04 812 Gland W4tftr To ~?P Flow Hi'/ITR 5~;o 1 " "
~2 333 515 8;''05 »12 HcaUng S t:e.:r;a :Flow Hi."/HR X 10 5.152 II II
~
334 . of
T7 516 8W06 BJ.2 FW To;5P HtfB. T«l.iLp 5W68 3 111n. Avg.
:P7 335 517 m:07 ln2 8F:r~D~CiCb.8 Bdr. lrp.88 PS:t 5W67 II " It
\
f7Al 336 ~20 CliOS 1312 FH From Ht!' 51"1 '1'~.. of 5°w71 "" "
T7b.2 337 521 aW09 B12 l'W From Ht1!' 5F2 T 1It1l1,!), r 0p 5~17 2 " " "
T81 JJ:I 522 a~fl(1 &12 FW P'rC1n Etr 5Gl To.mp.) 0, 5H75 II II II
:j:u2 33~ 513 8WJ.l B12 PW F'-"C1D Htr 5G2 TCllt:Ip. J of 510176 " " "
'l':?1 3I.~O ~2tt 8t
-------
CALC'"JL+\'IID> VAJ.UE TABLE (ConUnuod)
Iutenaal I.oUt10D l1Ctoxuo1 Scal~ D~Gcdption Uni tD Mult1pU...I' Input T)-p'" of
Indzz l"TID PTID Valu..
TBlA 344 530 8W16 ~ Bl2 SA BFPT 1;nt S tm To Htn SFi & 512. 0, 5W40 3 )1111. Avg .
nu 345 5311 8Wl7 D12 SA BFPT Ent Stm To UtI' 5F Pre~$. ro"' SIf4l " " II
.....
TAU 346 532 8W1S ,,;' 5A BII'PT Ext S ton To Htr 5B J Temp. J of SW46 " II ..
h2A 341 533 mi19 5~ EFPT Sta To UtI' S~ Fr~ss, FaX 510141 It " "
TaU 31.0 534 8t420 SA BFPT Ext 8m Tu HtI' SD, TPmlpJ of 5'155 II " II
P:J3A 349 S3S 6\0121. 3tm Fr'SA DFPT To P.tT. SD ~~GOO PSi SWS6 II " "
DiB 350 536 ati22 5B BFFT Ext Stm To Htrs 5F1 & 5F2.
-------
22
c:A1.CtL\TED VAL1m TABLE (Continued)
Int~rDl}l Loc~tioD Ixt I'Jrna 1 Scale . D~cr1ption Uni t8 MultipUer Input T7p. of
Indt;\x PT~D nID Value
l'hl 363 553 8W35 B12 Sta In BUD 51' Pr...... t PSI 5W45 3 )tin. A-.S.
4»2 364 554 6V}36 1 ~t. P ti!1 To UtI' 51 Tamp. t of 51(50 " II II
:::2 365 555 8t1!37 8 em In - To Uti' 51 PI'008.. PSI SW51 II " "
'''.''
U.;,.A 366 556 aW38 B15 SA BIIP Spaod L~ SW16 II " "
dl:m 367 557 ml39 B15 51 DFP $p~o4, UH 'W31 " " ..
I of
368 560 8W/~ / PW To Economizer Tm3p. t 5W77 "tt "
PUA 369 561 8\-141 BU SA BFP Tu~b Dowl Preaa.. 'P3I Sfi17 " n "
~'.AD 370 562 8\-142 I' 58 UP£- 'l'urb Bowl l)r~I1'.. ~31 5W32 It It II
I
r-~:~l 371 563 W4) Ht~ Gl'n~atD Cooler TD 0}l' DtICG 1 Calc - Ii} ;./
I '-
,
D:HX2 372 561. &'J'.4 Rtr G2 It " " " DNCG2 II II
i
I;l?l!l 373 565 5H4S I;tr 1'1 'rIDrm1.l1a1 Diff of T't'.P'l " I,'
m::.u!2 374 566 8W,6 UtI' :Y2 " " " 1'MP2 II I ,
l! CD 1 375 5G7 ~{~7 l1tr Gl " II " 'I1!Gl " ; I
)j'.i':.G Z 376 570 C:~4n v Htl" G2 " " " 1HG2 "
~';D~A 377 571 mil.~ 1)9 DFf T~~b A Turb Eff. 7. EQ 5T24 II' ,1,. ~
.'. I /- -
r::~D:!J 37u 512 ar:~o B~ 1Fr Tutb D Turb Eff. 1. EQ 5T24 "
, I
~l'~:f,A 37fJ ,.73 e:.5J. t? Rnill\ba f,FPA EQ '724b " ' I'~' I /
()
I
0'1
CD
t
-------
2;;i
.,.-'
-------
~/;
;1 CAJ.CU1.ATIm VALUE TABU {Cozat1.ouGd)
.~
~..~
'.
L",,~o=:1al Locat1OR External 8cale ~cr1ptioza tJni t8 Hu1t1pUor In~t 1';r;'3 of
~ 'i Ind.ex PlII) fTm ValUQ
.,
:4 615 of
;~ Tl 3~7 8B04 812 S1r sn Out Tcup., 5519 3 Ian. Ava.
"I 1'1 39a 616 8D05 B1r SB Out Pres.., PBI 5820 " " "
!.t
'J TZ 3!;!) 617 8:C06 P103ZinS S m Temp., of 5t05 " " "
;1 PZ "00 62C 8807 Pessing StmPrcc8., PSI 5E06 " " "
~.~
'.
~ i
;; r~l 1w01 621 anoa, I>n:3 ~8cure FSI 5n03 II 11 "
~ ~
~ ~ 1B3 402' 622 8B09 Soot B1oviu8 8 tm 'leap. 0, 5n26 " " "
~!
!:
, ~ P1'1') 403 Soot D1aw1ns Stili P~uo. f~I 5n27 It " II
623 8niO
; ~ "'
,. or
; ~ 'l~'; ~ 40~ 624 aRU ""(1 1iro= Ec:on. T=p. 5t01 11 " "
~- of
,:;
D~41 1005 6Z~ 81112 n9 DnmaJ.eva1 "11 X 10 51102 II " It
. 20
I
1;'J6 E?r. 831) 812 n1r a.a. Cut Tt!'ri~.. '7 SD24 ",II "
;~'J
t:1 1;07 621. 8D14 1;12 ~:lin'Stil Flow Calc. l~ JIm. EQ 574 Calc //," ,;)'
EFBI/L ;1
-:-.~'~:-::-:!~ ~oo 6~\) antS 139 Blr nff Hqnt Lo8& 7. EQ 5'3J. II
~
;j rF5Ip I;'A~ "
!:. .'~ :
~ Lii~;D l.~~ 631 &~16 159 B1r Eff Input-Output Z ItQ 5nIO "
£,H.
tro~ :~:.O 6~ 8~17 B!) Dlr Sff Deviation Fr Contract 1. "
, l~ll 633 &!i18 BU:<1~r Tilt A 1'1ca -IS 1'0 - 30 Hia CAlc Int.
,
,
~ .
1;,12 634 8319 Burnor Tilt A T~ 0 1'0-15 111D f1 II
413 63S 81120 " " II II +15 To 0 HiD " n
414 635 8B21 .. n II h + 30 To + 15 Min II II
()
I
.....J
0 .
-------
I':J'
CALCULATED VALUB TABLE (continued)
..
I~:-;\.n--~l toc.GtiOD Z::tonal Scale Dcccript10n Un! to Multiplior Input T;:po of
I~!1,:x PilI) PTID Value
415 637 . 8B22 BUrlier Tilt B Timca -15 To -30 }tin Calc: Int.
416 . 61.0 8n23 If " B" 10 To.1S " fI fI
417 641 8D24 n " B" +15 To 0 " f1 "
418 642 8n2S " " B u +30 '1'0 +15 " II ,!
419 643 ~n26. B19 D1r Oper Rro TbiL'l Uonth. lITe 1!oath To Dt1te
I
420 644 8327 119 II u. II Th1c Yur, " Yc~r To Date
421 M-5 GD28 B19 " " " Since Start, " St::rt To Date
\.'1:1 422 64.6 81529 B12 Boilor Dloudown Flow, ~ti/Im Datil Insert
.i j
, -~.~~"-.£U.=~ -;.~
I
! I
i i
""--"'~,"
! .'." oJ
i
t.I:,:..".:.:tiJ r;,""1 (2.6 Va'-~c~)
r; PI17 t 41.3 6.H 6n)). L /2 rlr I8~itio~ Oil Flow, ern 51"11 Hr tn:ez
424 650 8J!02 ['/? B1r Ignition Oil Flow, (},a 1 S?l1 24 111' Int4s .:
r:Icj 425 65'1 8F03 D'-9 Heot Input Conl, 10 vn'IU Cdc:
~';;I~I 42G Qt;' 8104 B19 " II OU, I " "
oJl.
I n::::;:; 42.7 6~J BFOS D19 " " Total, " / fI "
i (''';/'\:/-.5
I
i -:: :~~ :.J. 1~2~ 654 8706 F/2 5 }t1.1b Tot~" Co.t\1. lI'lc)H :Ur} , '1'onrJlill Colc: Int~8
('0/..5'1)
:-'.~'." . ::.i, ~.29 6S,S 8F07 BU ~ lUll D411y Cod Flow TOM II rt I
()
I
-..J ..
-------
--3
;'1 c:AI.CtJL\ TLD VhLUE TAnI.ll {Continuod)
,.
"
Internd Location Ext orna 1 Scala DcDcdption Uul ts Uultiplior Input 'rype of
, Indax P'lID PTID VaJ.uo'
h
t. ('I- L. ,S£;'
L
f ~::.~ ::.~~J:t 4:;0 656 8F08 B12 511 11111 Daily Coal F10\-1 Tonti Culc Iutog
1_1 L,' I
~ (' f'7S.' -~~. !:-
5C-:~.~ 431 657 SF09 812 5C Hill Ddly Coal F't::>w " " " I;
"
~ (' 1'L ~:j;
:1
~~ Sl:~-;~:~~ 432 6(..0 8PIO BIZ 5D II If " " II II 11
\j
~ ff! -.:;f:-
g ( ,~ 661 8Fll B1Z SE tI I' II ,. II II 1\
- ~"'>.~ 433
~l ,/v/f [~P.
~1
:.~ ~~~:~~~ 434 662 8F12 B19 5A HU1 OV"rheul Tonti. TOnD Calc & Data 1:10 I
:-.i
,- rfi//! - i,'
ii
t:
\1 ~~-:~:~'t 4~5. 663 BF13 B19 SB II II tt ..
~ ~
f:i r1 t/ II..:.<:'~
" ~ "'.".--:~----''''!I... 436 664 8'F14 B19 5C tt II If "
a .~"'I";.J~
t' 1...1//'/: 'r,
~~ ' - ../
~ ~;:~.~':~:.- t'~37 665 8F1S B19 5D ~' " r; "
"
~ '/.!!.J(l _:: / - ,,~
~ .to. ----.-::-' 436 666 811'16 B19 58 II II " Cnlc: & D<1tn Xn.oI
:i I
., .,
t~ l::fl 4:i~ 6G7 GF17 B19 HHY Co~l BTU/i1 PIiV D;1ta XD-';'UfT t
:..i
~ i
\; Ct.. 440 610 8Fl8 S .. /1..- ~ Cnrbou/~ Conl 'C '1\ II
~
:;~ I' I'" f" , '.
,.~
. CAn 441 671 .8F19 f C:lrb Durn'Jd/f! CoAl Cab " "
"
i UC 442 672 611'20 I N1trogen/\} Cod 1~ I' II
~
~
II
~ (i'J 443 613 6~21 ~ Sulf.ur/~ Coal Su fI II
[j
"
r.
~'. AC 444 674 aF22 '1 1.(!.u/IJ Conl A II II
~ 1/
~ OC 4l~5 675 8123 /j 0),.j8ooll Co:!1 0 " II
~
~ U2 ..46 (.75 6li'24 ., Ryd:rog('u! ,'\ Cod n.. II II
~:
~ '
11
~ r.c 447 671 8P'2S tJ II in Puol Lo.,a HZ in Watnr 1:& " "
~; 2
..
~
&1 v.p l~:O 700 8F26 "I (i Wator!I Co:11 fiT) .. n
~;I "
..
!,-....J
-------
....
CALCOlATF.D VAUJE 'I:ADLE ~Cont1DUed)
Intomd LOell tiOD IUttomal Scale D6ocrlpt1oD Uniu Hu1t1.pU e\:' !nr>u t 1)'p~ of
Xndcx PrID PT~D V.duo
AroQ eD Draft (22 vduca)
~FG 449 101 8001 89 t OAY8~n in F~u~ GSG, '-, XlO 5D3a :3 HiD Avg.
...
TG17I. 450 702 8002 aU 5A leon Gos In T(>illp. t o. 5D30 " tI tI
i
1'C 118 451 103 8003 5n Econ Gcs Xn T~r., of ;J)~l " " II
T21.\ 452 704 8D04 SA A.a.' G~." {)",1 t !t:,:oJp.. of 5nltO " tI "
'1218 453 705 . Soos 5n A .W. Goo Our '.i'P.ro:-'" ()r 5i}L,1 " II It
TiallA 4Sl. 706 8D06 5A A.H. Ai 1: Xn T"Ij)?.. of 5DJ.6 " II "
U1U 4SS 107 SD07 sn AoU.. A\1 r. !n T-wp. ~ of 5D17 " II II
,
'L\l4A 456 710 8D03 SA A.:t. M.:: Out '!~" t {'F 5D1Z " II II
TA143 457 711 8009 5B A.~. ,:\i.r Out: At.'!mp... of SDJ.9 " " II
'IG19i-\ l}5S 712 SDlO 5ABc.on G.;:~ Out T~.. "p 5D% " " .,
IGlSHS '~~9 713 aDU 5D Eco~ Gtl!) Out T4F:1Up., of ,)D~5 " " "
460 714 8D12 'fJ 1 Co~~uatibl~ Xn ¥~uo Gae. .,. X 10 :iD39 " " II
Ie
461 715 8D13 BJ.2 5.1t FD Blo~(\~ tn\~t T~mp of 5ti09 " " II
462 716 &D14 B12 S:.J FD 31o-","'r Xnl(lt T'~p of SD1.0 " II "
....}:A 463 71.7 ann B9 '1. E~ce.:.J8 Ai" ~5B26 Cdc ill" ," .' I ~ '..:
£i' AI-:A 464 720 8D16 B9 AnR, 5.\ Eft. 't 1:;Qsn13 II I I
!~7 f.!:J 465 721 8DU JJ9 A.H, 55 Eff. '" EQSUl:i II 1/
..
()
I
~
-------
26
i .~
.,'
CALCULATED VALUE TAtLE (Continued) "
H
iJ
Intcn1Dl Location External Scale Description Uni t8 MultipUer Input Two of ' ~'~
, ,
i"~
Ind'."lx PTXD l'TtJ) Value !";
,~ 1
j ~<
W~~ 466 722 ' 8DlS 89 A.H. ,5A Air Leakage EQ5Bl2 Calc. SJ 17]; IJ fJ
rl
I'
, II tj
t;Lr,B 467 723 8D19 B9 A.H. 5B Air L'Jakoge, ,KQSBl2 "
fll? - A :t;? t:
r:::?EZ 468 72'. 8D20 89 Bconomb~\" Bif. 7. EQ5B14c II ~ ~
.' :3 I'Y}; AJ iJ
of '
!G1.7 4W 725 8D21 Bl2 FluiD GQ:; Fr AH Avg. Te:p tu19 II i
\'
j'
'1'21 l;70 726 6D22 D12 Flua G.M 7r All Avg. Temp 0p t21 II II ,.
!
;
D~1IN 1.71 727 8Fal B19 Dl::t1UI Writer Flow. GPn SPlS B\:. Integ
~Ij ) I~~ S'..1 472 730 Sro2 B.l2 Cond Fr. Glycol Exch. F:tow M~/BB 1/100 511.3 " "
473 73 "A. aF03 B12 Glycol ,To A.B. Coils J'low aPH SPOS " "
I
,
.f.," :~.....,. . '[ \ 474 731 BP04 Dl9 DEd!N ~Qt.r Flo~ Gal 5P15. 24 Hr luteS tf /;-1,
,
i of 5Pll
Tn31 475 73;; BrOS, D12 Stm To Glycol Ib:ch. T~p., 3 Mia Avg.
1;1331 L; 76 73" Sro6 St1:1 To Glycol E1tch. Tc."::j)., of 5P12 II II "
TG 477 1~ Br07 Cond Fr Glycol Exch. TC'IQ.. °u 5P14 " " "
42tJU. 4~'" 136 8P08 C.W. In IN: (UQstj T f::1!p . , oF 51'05 It It "
'"
TZ~~~' 479 737 8ro~1 c, ~';, Inlf!t (Eaat) Tf1I~.. of 5ro2 "" II
'l' A.;;ro. 420 740 ai')l0 G,W" Outlet "1'!C'!1) t} Te:.~., 0*, Sro7 " " II
Zl~~ (,81 741 RNl CW Cutj.~t {r..:\.., t} Tl!Jrp.. of Sr04 " u "
i
i
TlC?.) l:32 7"2 81';'2 I C,W. Outlet (WQ;) tl '! CT.ip . , of 51106 n,, "
() t o~,
I "'~CZ'A 4B3 143 a~n C,W.. C".1tlot ~!.:I! tl Tr-or.p, ~ Sro3 " n' "
-.....J 4.....
~
-------
I
-"... '
CALCULATED V.'\LUE TABLE {Cont1m\od)
Intornd 1.ocat10D 1xt:C)gnal Scale Doncdption Units Hultiplier Ir:pl1t: T-.lIH1 0 f
In~~: PTID PIID V~J.uo
nw; 484 744 8P14 19 BArom~t.Qr Pre:1e. ~ "RtI' X 10 5P19 :3 1110 Avg.
485 745 DP1S Sat Stm Conduct~v1ty. HKP~ X 10 5P16 " " II
486 746 8P16 Cona l'ump Dbc, Co..\c1ucd.v1..ty, 1i~ro3 X 10 5P17 fI II "
fiB a. 487 747 8P17 B15 C41c Plant Ht'tlt Rate- n'lU/lGTH Eo15T26 Ca1.c L:: /-1.
reR.!O lieD 750. 8P18 115 '(uput-putput: rAt li.R. BTU/rom EQ5T25 ;'
"~ I '
IT:Ima 409 75.1 OP19 »15 ~lt HR D~viutlou F~ ]lozio EQ5T29 "
.
"~
," f '
", FG 490 752 8P20 59 CondtJo3 eX' C1c,ndineao Fuct. 1. EQ5C3 "
", -r z.. r f;J p-
of ' .. I' 17 V."=
~.;.-r 491 753 8P21 'n12 Ci J:'C "latur 1.0 k;& 1'c;;.p. t " J f ,:
i
! /7 .' )
. 'l2C~D 492 754 8P22 ,Ja" C.W, :!n 24 Hr ..\vg T~").. 0, " :. L.
.
,I, I
. ~
<
. 433 755 8P23
i I
! i
494 756 8P24 Ti~A Fo~ High Lo~d LoS Data Iosert:
.
I 495 757 81125 Ti~ For Low Lo&d Log II II
j
!:z,';:f",. az IU.r.c~UC:1eou£l (I~ ~fE.r~_y'a1~~: 16 V~~!..L
tr.-ro 496 760 8Z01 19 Dry Flue Gaa ,g/i) COG! EQ5nZ<: C31c //1. /.
'!'].~"1~tf 497 761 szoa all CW, O\~ t 1 (\{; .;:W',,~ t-; .\78. 1!t:<:lp.. all' 3/;'
, ; 0
tlCiJ1 498 762 81.03 512 C.W" Outlet :EM t Avg. -r.1JIp.. 11
TGl9 '}~9 7t3 8in4 au Bean G3.') Out AvS. ,!,t:!w;?" " 0p ! I .
r..;~? 500 764 81.05 di~' liP. Gen. rom Groa~ Mil J' / ': ;". /..;
,':
() '. 501 765 31.06 .1; , I Au2t USA Dal1y {Bum 81:07 & 6J?03} 1-:.1 L I,'
I A'WhO ' -
-..J . , -
01
-------
. r, .
~TED VALuE ~LEt 'Continued)
Multiplier Iv.rout
PTID
I( J{/ FI t11 502 7'5 . 82X>7 8/5 Aux Uuo Honthly (SU1:t SEll & 8E12) 1m X1.
CrfALO 503 767 8ma srL Tot~\~ Coal Flow Da11y
~ 504 710 8Z09 89 Ilumid.ity S W'. 71f} OZ14 If
510 776 8Z15 "
511 777 8Zl6 It,
. i
Internal Loc:.:lt1on E;t~roal Scale
Ind~x PilD
Daacdpt1ol1
UnitS
()
I
-..1
0"\
"""--
. I
'IJr~ of
V~lue
. CAlc
£,11,
..
~/H.
-------
, -
..
, ,
I ." . ;:,.-
:~ ,i'~ ~~eam-Electric St~tion:
--:
.-
."
" .t
Ui; 1 :
:t£ ~ w(")~,f\~-....,..
;2,:18-71
¥h~-~ ~Qa,_..:Q-
CD
Data Sheet 1 of 3
Date:
Soi 1 et'
\ [ . -I- TiL(=i~'.) L~:--._. -~C~ -:
- ::::::~:;::~:) (lbm/hr) -I! -\ -!-..---.-1==:j-~=~:::~:~-
Exccss Air (X). I --I i - 1 ~---t-_._._.
-- I 1- I -I - ! . .,1__.__+--.--
,-_.-~~-~~ Flue Gas (%) ,1 ' ! ! ~ , ;
C02 il1 Flue Gas (%)'-'!--'-----r.'tl' -- -r -J----"-;!""-'---T'~'~-'
---....-- "'.-__..r,-....-~....--.-_-.--.,i....-.....~ ---".''''''.._.r_!.''''--,''''--''--~ --~..,......._~-, ....~--.......-L......--",
S_oot~~o~Jin~__- ' --,-'-.,,. .i .I---..i I ! \ -_t------I-.----_..-
Boil~~_F~ed Watcr Flow ~~_~~/;,r) ~.L--I---J I i !- [___L.__---
Boiler Recirculation Pump Leakages (1bm/hr) i I !! . '
,-,----._---- ' --_. ","'" .--..._-z__I- r'-- h_1 -:---- .!_------+--...-,--
Boiler Inlet Feed Water Temp (OF) I ! I j I !', J
Boiler Exit Stea~ p~~'~~~~-(p5ig) '--, ~ ! : j--;--"/"- -:-..-----...
-- --------., ~."" ....,---.- .."--....-..-----. ---- t ..._--_..l-_~.......-_~.t~.__._._-"~.......w..._-_.__J~_...-. _..~._-_..__.l-..._..._.._._.
Boiler Exit Steam Tp.mp. (oF) , ; i I \ jl j J
..~=- ~~e':i~..!~ .le::~~~;pr:~s~u;-~~.s~g}---=-~l~-j~~-_-J=~_I --~=~l -- -r---
. -----~~~:~;' t~~_~n_~~~._~t_~~~ _.~~.nl,~.~.~.._-- ' ~.l-_..~-~---L--{----l i .._-~----
_"'d_~e_he..~te:_..~:~.~_~~e_~_n~~~.~,~~~- (psig) .!..---------~- j, ! ~--___.._.L.._- I
. -or; Re he ate r E X~~._-~:~.~ _!.:.~P..:....~-~1-. --------1----- -".. - ..;"'-_.._--_._j.:-----~.- -~'----i' - --- ~, "'----11______-.--
-..J .' ~ , .' ..
-..J , .. i.. ' :.., ; - ! ' ; I '
-------
.
,';'
, .
Steam-Electric Station:
U .... .., ,
111,,: "d,
Date:
:Z-/~'''I
Boiler
'.."
Data Sheet 2 of 3
Parameter
'Turbine Steam Flow Rate (lbm/hr)
, Condenser Pressure (in Hg)
..:..-...-----------------' _.:. '
, Boiler, Air Inlet Temp: ,(oF)" !
Boiler F1 ue -'G,a~-E~i t-T;'~p .-'0F)
~-_._-;""-",-..._...._~..;.~.j ...1. .': .
FD Fan Pressure Rises (in H20)
-,... .--...... .0"- "",,-""-"--
,/ FD Fan Currents (amp)
-
""-"'---"""".--
, ,
" FD Fan Voltages (V) .,.-' v""
--- ...----.-.....---. """-"~'..._-_...
:~~~~Pr~r:.~_!,~~s (in~~O)
ID Fan Currents (amp)
10 Fan Voltages (V)
Ambient Air remp. (at)
i,':'.''>'( ,:" ...t Time (min.) --
! !: 7 q" 1",' 3 L-: !.&~ 7---.j I ~; 3 7 'Lf.lL!'h----"IT+~---'J:;-
h~t- ,:':;(7 ~tl"7(: /~i;_~_~'?" ':"::':':""_~--~.'::'::''' v'", J ~.!l- i/("<:' I---:::>"::=--~~-,-
I t4- i IJ. P. ,:. : II /) I I~ I z, 'I ,'1 l \ \,. i ; ;', "I I' I~,
10).,., d+:'tO i LJ)(' ~~O: '0,1} J.h,~ L '/."" 'f).'f!) 'J';'~ ~-RO ~ V.7'~ "'2...Ql C!J, 'i4.~
-_~J.8i..........-.':f"~~.'-r- ~\~-_......- ~- -. I - ~'t
t~ ..-. ! -- :~---I.' ------1---.-'
! I ~
I !
I.
I
I
j
f
!
1 !
~! !
-----.---1-
! i
i --t
---...:---.-
i I
J -~J_,------_.
i I!
I, i ---.'.;------.
, ~ I
i I I
t-- '-r -+---r---'----
! ~ ~
i 1-' --- -_._-'-------
--+----_..-tl_---~-----T-----'
ii,
I Ii, i '
./
Ambient Air Relative Humidity (%)
.
\
\
-'
./ Fuel Sample (......)
<--' Ash .,?a~~_....-1
6.oi ley Heat-Ri!.~j~BTU/kw-hrt.
---
, /
"./
()
I
-.J
-------
Steam-Electric Station:
Unit: :d- ~
Date Sheet 3 of 3
() '.'
v.Jl>"C>-~ 'i~ <'."""" -
r:) "" Ii ,j
61~ £'(-li.-Y
Date:
~- , S.... 7 I .
/'.'07
Start Time:
Electrostatic Precipitator
Parameter
'.' , /
,. .r . / : '''' ( .
...--.- -----""---
) ;~.. .J! '
---.....-....... .,.,,..---...., .
i \- : ' , /1:: (' -) JI: .t: .,. 1 1:,,,.'0'7 / ~.' ~ 7 Z I~ ~ 7 II" :r 7='
j ", I .. r, i -
4;;~-'',:I~~-I..., 1~~8-;t'n--'-s-~:i T ~ - -; -Ii' "--"6-')''';;' b.-l-A-,-e-17r:--g-"
"'- . ~ i.,1 ., '" . _I" l' " ~ i ,f ... J. J -/II ,.., ,...
..,.N~ ("(--' !A 0(...'> ':2.' :l....~ i?. /l..,J',J" ~.OJ!~ ;l..~ !A.' ;:?." I...J ;z.>:
--, r-"-:--- --. ..-.... ----'-.,..,,-.---.-. '-~--l'----------'- ..'~ -r---, .
: . .. --- - -1- , T. --- .
, , .
- ~ v- 1. ~ ----- -.----- ~~.. ~ J -.-.......-... ~- -
b
Inlet Temp. (oF)
v
-
Inlet Pressure (in H20)
Ex; t Temp. (UF)
- .--... ....
Exit Pressure (in H20)
Rappi ~ g ~Cy;i ~- 'P~'~i' ~d-{';{;;-:r-
Controlled Sparking Rate (sparks/min) "
,.3\ .
: < 'Operating Voltage (i01) It- - 12 'l;.A
~. .:.,.e "
--_.._.
r-"-- "._..-.......- ---
llL.£i.~bA~_~g. - ~._&_311 D'
B 3 ;2..0> /j :>~o ;; !J':;'O
- v
~,3sD e 3~o e 3 $"0
[) j 5'D D 3:;-r;:> '~.3 t;;.-:)
I~
G ~ ~o E 3 GO £. ~ $"0
~---_..-.' ----_.-- ....... 4'.'. -._.~_._- -.---..--.....
; . ."~ . . ;
.:_../1 .~;!J:?. ~:.Ll.. j" LJ,.£L
1.3 3~O ;.; 3i.J,o
c .3~-o C j5D
f) JSo D ~~"
E 35'b ~ 3~7J
.,l'L._J.!/R .1:.:.: jt..J.1!-.~.'.
6 51<'~' I J},()
(! ~.f; 0 (~'3 :..ir.-
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/3.:;..:0
!} 35£.')
13 :3S0
()
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\D
. --. .. .-. -
, .
-------
S,eam-Electric Station:
Unit:
Date:
. ,
~ /) ..-tJ,
, .'
-\ -'. .",,--\1
Data Sheet 1 of 3
. G)
/i I
.:pi .:;r I/J o -J
7-/8-7/
Bo"il er
- ..._-
Parameter .. Time (min.) ~. ,
"
~: o? 2.'37 13,'(.)7 J....., 7 . 'I: 0 7 u~;---
..>. :,.,
(MW) I r ~, (-'
Gross Load .
I
'\ l---- .-- ---...~_...----...._-_.
(MH) I
Net Load I I I
\ I
- ! ; I I
- ' --.- ----.
.I __1___-
[ i
-'1'------:"--'----
t- ;--
!
,...,-~J._-_--o.__._.-
I
L
I
I-
I '
I
-j
Fuel F10\'/ Rate (lbm/hr)
Excess Ai r (%)
H
-- ,
. I
i
i
I
t
I
.
I
T
I
I
-~-
i
-l
_.1
I
.
I
~1
---'---'-
,
i
i
: i
. . I
!' !
""'J4"""--"'''~r-
: I
02 in Flue Gas (%)
C02 in Flue Gas (%)
Soot 810\oJing
Boiler Feed Water Flow Rate (lbm/hr)
J-
\
culation Pump Leakages (lbm/hr)
-"---
Feed Water Temp (oF)
I
I
- .
i
!
l
,
~
~ ,
,
I
~.. -
Boiler Recir
Boil er I n let
-,
J
i
I
_L
i
I
j ! i
---- -.-.---t-- I . !
Iii
I
if;
t ' J
. '-'--Rehe~t;;. EXh Steani Tein~:-( oF) I I I
..---..-. ----_.- --....._------_.- ~"--"--"'i -----.---- .'......--
i
I ,"
Boiler Exit Steam Pressure (psi g)
...~ ---- --_.
Boiler Exit Steam Temp. (oF)
Rcheater Inlet Steam Pressure (psig)
......----. . ~ ,- '- . .... .-.. .-.' .-.. .... .. "'..".,-----
Reheater Inlet Steam Temp: (oF)
.--
I
-.--R~h~.~t~-;:E~i t-St;~-;rtP~~sure -('~Si g)
=J
I
j I
1-----1.--
-+. --{---
,
j
-----
()
I
(X)
o
J
i
I
!
-\.-.--..
!
i
-+----
.L--
-7'---
;
-------
. Steam-Electric Station:
Duta Sheet 2 of 3
~J. ....--
Uni t: J-J- ,::-
!/ i :"j .' i ;, \!\ .:. L'"
'.. \... ~ ... ,
.,-, '
Date: .2 - I g. 7 J
Boiler
- -..
Parameter Time (mi n .)
.~. 0 "/ J.'37 t ~;;;:o7 '?I'~? "-' '" L.....-1 !!J.!:L- -~~.C!_Z_,.,'
- ' _. ......!'-:.~....-.._--
.Turbine Steam Flow Rate (lbm/hr) i I
I ;
\ I
-----'-. -- ~ _.-...
Condenser Press uTe (in Hg) I i
!
! I
- -.-.....---- -l---'-' --~-_. _........------'~
'Boiler Air Inlet Temp. (oF) ! I I
- i
.__._-----~.._-_.._-"'--
Boi ler Flue ~as Exit Temp. (oF) . I j I I
j
.' I ' I
.' .. ,_,,__,,--,-'._-----~"."" "'-'-""'--- . ~ ~ y i ~ 1-...---- -_.-
. I
-~...-.._..__..... -.. .---.-".'--
I ~ I I I
(I . .'("-l~-- 1'1 7.5-I~~ J;- '-;j:' IJ' ~r7f
I ~~' u: 'I <" 0 ,v-fJo .:!:.!?.~ '-I C'f}r ~ ¥.c_~_L:t~~ (') o,ll',,?o
1/'1' 6 I R /.J i PI (5! ;q. 1,1 i fJ
i,~ 00 /!'!'orb:,! './...! I
) J.
--.A--rt----r-,' -.----
.8 ' r _un l::c ,I '1 "'.>
~.PO I ~.~_'t.~L?_~.
I!J ! I .
' -.A0 j ~o "1;J.,.r~ t/'Jb '7-..~
FD Fan Pressure R1ses (In H20)
~ FD ran Currents (amp)
-- FD Fan Voltages (V)
,!. " r~ ~~-< ~3~ 4(1,,', jl.~D 11. t:?~1 II" 0
-------
Steam~Electric Station:
/ ,
Unl't. .Jj. 0-
. .,-,..- v
Date:
() "
, (JJr>~-c,,~~
()
t)L~>---'
Start Time:
/1.'07
~-/g-?I,
Electrostatic Precipitator
Parameter
Inlet Temp. (OF)
In let Press ure (in H20)
Exit Temp. (oF)
i :r(\ 7
v
Exit Pressure (in H20) If.'V' lItf'n'I..~
(;.';'-' :0 c> r...,-f
._----,..~--.. -"'- -.. .._~... -,'.- "'''.A.-.~'.
Rapping Cycle Period (min.)
Controlled Sparking Rate (s~arks/min) ,
-
Operating Voltage(KV) ~7~"Jl! fI 't
()
I
CD
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12' 3.?
i " !
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l,t- 13.f ,.i . '5 fi'
f~.d~L .~ .. ~.5, ./}..
r-I -~ -:- )~ -
..:, ; .~:..:J: ~ :;.5'
-~... -~_..----- "--.--....-.......
-..._.~._.--..... ----.rr-
:3'10
B 3;:l. t:>
c 35"0
o .3 ~$"
E 3.50
._, II 3 'ft>
B ~..l-O
C. ~::>o
/) .3;..0
c. J.tIP
--
- VI..-
1iCJ'3<,t:.;. rr~~v
_!.:l-....-.......-.- ...-.--.---..
.,.
(3 3;1..7
~,.,
C 3':'~
!) J ~o
,.,
E 350
13 3;;.. G'
c 3;:-~
P lsc>
-------
:tcam-Electri c Stat hn: () . f(1.)/1 ..1
Unit: j:! (;)- C/.J )-J.Ll/~~ t:~ r:c.,,~1,-A
Date: ;;L ... I g - 7 I
Boi 1 e r
Data Sheet 1 of 3
Parameter
Time (min.)
- 5; 37 I
-
Gross Load (MW) t
-- ~--1-----'----""
Net Load (MW) --+---
Fuel Flow Rate (1 bm/h r) I I I
-- t- . f --~-L--
, '
i i I I
Excess Ai r (%) i I i
I I -L--.
i .........
02 in Flue Gas (%) I ! 1 I
I j .,'-!--
- !
I -r- ! ..
C02 in Flue Gas (%) I I \. !
I i ; I !
-- ! L "'-- -- _!-- ....--- .'.. --
.1
Boile r Feed Hater Flow Rate (lbm/hr) 'i I
Boiler Recirculation Pump Leakages (lbm/hr) 1
---------... t-
Boiler Inlet Feed Water Temp (oF)
Boiler Exit Steam Pressure (psig)
I
!
.
,
.i. -
I I
I i
1
I I
1
I ,-
I I
T
, i
! !
f I
I
I
i !
I
I 1
i
. I
I I
I I
. ---;
I I
t
Soot Blowing
I
L
\
I
.L
I
t
!
!
j
1
r
j-
! ,
i
I
f-_. ._---,"
1
\
I
,
-------
!_-
.._-,----~--- .
-
Boiler Exit Steam Temp. (oF)
\
t
I
i
-----.-.--------
Reheater Inlet Steam Pressure (psig)
--~--- _0.. ... ..". -- -...- ow",' ..-- .. .... ".,. '.,- .~.. .-. ",. ." ,~.... '. .-'.-
Reheater Inlet Steam Temp. (OF)
~-_.,'.-
....-~.,_..- .'-- ....----....---.--._w-----
.
Reheater Exit Steam Pressure (psig)
~----_...-----_._---
I
I
----r
I
I
Reheater Ex; t Steam temp. (01=)
.-.
---_.."--
()
I .
(X)
w
~-
I ,.
\
I I
-'" ._----~ ._- _.._-~~._--_..-_._...
i ;
.~; ~-----_.
! t
I I
i t
I ! 1----
._~ - ~~=--=i==
I ! I
: i ;
-------
- .
Steam-Electric Station:
Unit:
Date:
c ~ ,
V) .:} :" .'\,~{....v---
r+-C
. \
(~b/' .-..."'.1_>-(
..;.' .
~._~
Data Sheet 2 of 3
;J ../ I
;l-fj-
Boiler
I
! 5t ~3 '7-1 c,' 0 ")
II
! ' ,: I
, I
"f
I oj
/---
'I r: r'
Time (min.)
I
Parameter
f
i---~
I
I
I
I
.. I - .
I
r--
--~
~
!
;-
.'l~-=-~
~Turbine Steam Flow Rate (lbm/hr)
Condenser Pressure (in Hg)
...------ ---- ~._-
. Boiler Air Inlet Temp. (oF)
Boi ler Fl ue Ga~-Exi t--T;~p-.--(oF)
-- ~-,__-",,,_.,,,.-.---,-, .. ..,-....'-""-.--
~ -------.
., - -.--------- .
j
_. !
\
I
/':":'~'j~ H L 1.3' -~_.-
, -:-:; ..-,i lJ f)? (/.';-0
".; ;'~~1-
~") ~ 1'1" c-
u .z?.Lz:.z2..-_1
: . I
I I
J ~_._-- r----
I I
~ !
I
I
!
,
I
I
!
,
-'--'---"-"._~'''---.''-'-'-''''''.~' ". . ----.-.....-
FO Fan Pressure Rises (in H20)
-''''''-'''''''-' .....--_..~---
-- FD Fan Currents (amp)
i
I
I.
I ,:~..,: '/~'
1." .' ~...
I Ii .; /7-, //
v FO Fan Vol~~~_~~-~-~~_. . - -----! I/,~,o.. I(~ .~-O
, . ,. t
IO Fan Pressure Rises (in H20) i.'
I ~~-~n c:~~~-~.(~~.~)---_._. J
I
~ Ash Sample (v)
BQi ler He-,!~-.B..iLt.~_LBTUI.~~)
!/
e-.--
-:
I
,
T-
I
I -
\
I
i
r
I
-I
I
.j
t
I
!
'-.- ----..-
i
I .
.'---I--~==
I
I
I
; !
~ . 1
I.'.~-I----
-r--r---
L .:
i I
J_-- i
I I
~-----~t._--------
I
I .
-f--- ,- -.---
r------ ----~.
1--',-----'-,
----
--a.._-.
ID Fan VOltages (V)
Ambient Air Temp. (oF)
-----..---
i
'-
~ Ambient Air Relative Humidity (%)
--------
---
Fue 1 Samp le (v)
~._----_...~.._---_..
i j
--;------_./'
. I
I
I
i .
!
I
I
,
t
L-
I
!
!
.
- '
(')
I
CD
,e:.
-------
...
Steam-Electric Station:
/;J~ ~~
r'\ " ~
W~--1 yt~
Date Sheet 3 of 3
Unit:::H S
Date: I)...{ g - 7 (
Start Time: / /: D 7 j!J 11~
Electrostatic Precipitator
Parameter
. ~\.' 3 7 I &: - 0 7 c:. ,: 3 7
Inlet Temp. (OF) L~ ! " I
Inlet Pressure (in H20) /. II f...., J4,;,..(j !;; I!:'~ II a ~,,:/ ,,/:-f,: '~ -iI'
, '~1 ~",' , LJ, ~.:), :z ~:_~-J,d)J. r-'!~ - -- _..:.. '
Exit Temp. (oF) "I'....,:,,' " " - ..---1- [
Exi t Pressure (in H20) ,. ,or - --'- " j-'
RappingCy~i;p~~i~d'('';in.)- T~ ----t-.- _.,-- ._---~
.. - a . ----- -...---.
Controlled Sparking Rate (sparks/min)
./'
--..-"-
./
Operating Voltage (KV) fJ,~---'"
;
A 3~D
--
P .330
C J(.(2
f) 3Co
£- 3::)0
1) ,
t"7,~'tI/, ,> r,' '\-
/i 3C;o
/S 3:J. :>
e '~::I;)
,1::' .1 ~ 0
;:: -:>::0
...., -
()
I
CD
U1
..
..-.
rl :; '7 C>
------
6 330
~ !J 00
~ 3'~o
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S'~~~m-Electric Station: 1/.1t)t":1....:v'..~,,.( "::70 w C-~
un; t : :r.J; 5"
Date:z...; 19-7/
51;.},' cr--
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Data Sheet 1 of 3
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Boiler
. '
Parameter
Tirre (min.)
-=1____1_-=1
I ! i I
!- .-
J j
-1-~ ~.
I ~ . ,
I i ~ I
I I ! .
f - ~-----. --- ---~- J.
! , , J ~~::-J\~~
. . j , 'I' ,;
; '.. ,
,__~ 'i I
f i
i
'-"' Gross Load (H~1)
.... 'Net Load (t.1H)
,[ I:-J: 4,'; ,
-~.- --
, I . ,
I
- "', ...-....-..- --,.-.---- .-."
j
!
r--'
~
L
. .
,,/ Fuel Flail Rate (lbm/hr)
Exccs: Ai r (%)
02 in Flue Gas (X)
C02 in Flue Gas (X)
O.
!
I
'-
!
i >..: .~J. I~I ,,' . .
-L.::::.:.::2~
::.-e?~1 ~(..2 OD.
rip,) ,I L~ ['ocf'
'0. ",,:,''-t-..:;z;..-..,
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Soot Bl')'t,ing
"L ;'J"'J". ,.. ,\\..,",:! t~)'r. t: II hI}
.- J " , I
::;. B 2. 5 ;.,-:-) r, c ('\ -;; 't
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.,
~
Boiler Feed Water Flow Rate (lbm/hr)
-' Boi lcr f:::ci rculati on Pump, Leakages (-lbm/hr)
.1-
-
I-
I
I
,
I
-_.
i,
Boi1~r Inlet Feed Water Temp (oF)
Boiler Exit Stearn Pressure (psi g) '.
Goiler Exit Steam Temp. (oF)
.+---i-
~--- --- -;1---'---"'11,_" 1
' I,:
, '. J
5 7 Ie . ---I -; J
'--..'"\ . -,.--.-----..- ..-----,--. -[''''----''--'~--"-----'''r.
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J
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I f-=
I---L--
1---... I '/ '/ :; ,
i I .
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r------,-----"
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Reheater Inlet Steam Pressure (psig)
Ret;;;~er I~l~~t .s';a~"T~p'''' '('0"F-)----
';
"
1.\
i ~..
--...-..--.-
Reheater Exit Steam.Pressure (psig)
.? Reheater Exi t Steam Temp. (oF)
~
-------
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~t~am-E1bctri~ Station: W~~
Uni t: -tJ;::) ,
Date: ..2.. , 9 - 71
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Parameter
t~
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r.
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:Turbine St~am Flow Rate (lbm/hr)
i
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i .~
ft
L
,
;
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,
4
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J/FD Fan Voltages (V)
ID Fan Pressure Rises (in H20)
i
:":
ID Fan Currents (amp)
ID Fan Voltages (V)
Ambient Air Temp. (OF)
)
;..>l
~
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I
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)
Y" Ambient Air Relative Humidity (S)
~, Fuel Sample (v)
:.~
:~
.,
.;
1~
v' Ash Sample (.-1
/. Boiler Heat BnL(BTU/kw-hr)
{J
I
m
...,J
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'I
1-
:~
."
;1
12; uS
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(.I :J I?
l./?r--
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.',
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Data Sheet 2 of 3
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I'~ 171- l..rt-...:S----7:;-'-i""4 ~-h--1"--::,---::- £ ,if' . /:i' i'
V,U)i UJ'c- tJPD+.-U,-'t> 9J.j tfiJr:> tJ.~c: 1)1.:50 L/:Ib !, ::\r) (/.!~(I-
-0 I .l1 /; I" ;; 1 d' (:> I r{ 1:. H e
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i y --_.J-- . ~ _l; -
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Time (min.)
.2.: I~-
.,
~ 02: 4::>-
I
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J' Ie;,
/. Condenser Pressure (in Hg)
. Boiler Air Inlet Temp. (oF)
Boiler Flue Gas Exit T;~p'~-(°F)
---'-""""
FD Fan Pressure Rises (in H20)_b_~_'~' :
---------~ \ 5 f:) \ ._\ I
./ F () II- '.(d If
V' FD an Currents. amp qJ',.?: "30 I,I.~()
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Steam-Electric Station:
,W~~~
Unit: 1J ~
Date: .2.-/9-7'
Start Time: I); ~~ ,jJri')
Electrostatic Precipitator
Parameter
, -
Inlet'Temp. (oF)
I 1 t P ( . H 0) 1//" .tIfl..fJT-
n e ressu.re 1n 2 <'-11.5 ,,,":, u+
Exit Temp. (uF)
Exit Pressure (in H20)
...
Rapping Cycle Period (min.)
Po-vJ-' aP.J-
, I)..: 1/ ~
,
[~~~ 6
.3
.
I
I
-,
i
Co~trolled Sparking Rate (sparks/min)
.Operating Voltage (KV) 'P~C't-,Ir-,~: V-\"'-I" J1 3>7()
j
;
.
()
I
00
o:>~------
/j 3.1>-:J
Co ~ (,. ~.
o 3SD
E '3 ~o
Date Sheet 3 of 3
1:/:>
Ti fir> (mi n \
I 1;/1-5' ;;2"/~ 2 ;).:'-15"
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r:..
H
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/1 '
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e ~ ')'.
b 3 5()
e 3G'::>
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3: t), ~-:-
t1 - 3
~,.".~
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;:? ,-: t'
f'
8 p. It~
.3 :!..~ 5
~
.3
..
B 3~; 0
C 2.7 t?:'
D3t/c
£.360
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-
-
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.'} :~ (.~ \':"7' 11 :3'70 /) 3 (~C.., ,d 306
13;3 -0 g :l st:> /..' :3 Ct> B 3£0
t; ..:;;>
37D .. 3 7.(:- ,:-' /) 375
~ I:.. I! !I '7 t.? L
/)350 - P .3 40 I) 35D
I) :3!J 0
E 3~~ - CJ~o E 3(;0 E 3t;o
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----~_.._----- -_._-~.__.,..--_._----_. "'..-'"
.- ...--4---....----.---.--""--'--'-"-----
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Stcam-El ectri c Stati on: t/.J a-.."~.f ;t'....~ /;L'A"~~''';
Unit: iJ 6-
Date: d- Je; - /7/
iJ/.l ~'
(J::'c.;~,",1
Data Sheet 1 of 3
Boiler
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/ 'ro.',. .
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A
(min.) J
Parameter Time
-
i '
L./.. 1:;- , 6:tJ.S- ,.'Ie-
, Gross Load (r-1W) j
. I
j I ' ", ,-.' ---1'----' --_.
Net Load ( t4\oJ) I
! " -j-
'-
i
Fuel F10'tl Rate (lbm/hr) I
Excess Air (X) '
.
I I I i
. 02 in Flue .Gas (%)
. I
I --
1 C02 1n Flue Gas (X) j ,
i I
~ ' t
, I
1 , , I i,'j.' r\ '-' .!....' /.; ,J :.-,- (,>(~, .' \1 't..::. :>..(]/"".'('\o '
I Eoiler Feed ~.ja ter F10N Rate (lbm/hr) i I. I
I
, I
~
\ Bo1l(;r Recirculation Pump Leakages (1 bm/hr) t I I
"
~ I
1 -
4 . Boiler Inlet Feed Water Temp (oF)
1
'! I
.--
J B011er Exi t Steam Pressure (psig) J
1
( B'oiler Exit Steam Temp. (OF) I I
)
: !
i Reheater Inlet Steam Pressure ( ps 1 g) . I
!
'. - ~ ..
- .-- '.- -.-.- -....~,., .._--.-- . I ~-
'i"""' (oF)
~ Reheater Inlet Steam Temp.
f
i .-----, !
1 Reheater Exit Steam Pressure (psig) .sT J 9 LJ7b 'I- 7 <-J t-/76 I
j C-~
. Reheater Exit Steam Temp~ (OF)
:0 -
'(1) I r ,
\D ..
.. ~''''- ....--__.--'-f~~"'" -........---.." --~--- --,.---.-----..---... -~---)_.._--_. ......._--.~---.. -
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, . Steam-E1ectri c Stat1 on: {).J~~tl--..Q cP?,.I./'J..-r~ ~?~-.:J
Un it: ::l1:::-
Date: {;,-/9- "l'
Data Sheet 2 of 3
Boi 1 er
(')
~
o
. -
, (min.)
, Parameter. Time f
~ ", , ;:' " (,': iJ-:J"'
tj.: I'::> '-I.: 'f.:{' i 5".. 15 $": u 'S - .,~... /:;-
t.: I!...j .:.
-.....
. Turbine Steam Flow Rate (lbmfhr) I
. I
! Condenser Pressure (in Hg) ; I
I
; ' !
-- ------ I -
, . Boner Ai r Inlet Temp. (oF) I , j
; I j
--------_. ... ""OF) -
" Boi ler Flue Gas Exit Temp. i I
...---...-.
(in H 0) ~ 1>/3 ;1. 9. f, ~ 9. r...J. I :-s£~ C?_. ---
FD Fan Press ure Rises ' i "
2 .5 D 1L.j ~9. 7 ' i ------
_.._--~-- . '~_._' ;J. 9. ¥ .L :2.9.1.- .
/' (amp) HI !3 -,; ~ I I .~~ -' ---1-----1-------
i FD Fan Currents /',
<130 u~~ '/3D '1301 //;';0 ~l)! 0
; """--F 0 ,'n 13 ~ 8 ,'';'' I I
Fan Voltages (V) f /"~ I
--'--.--.-'- 'lb.? '1/5' y..~o 'II -~ i If ')..,p 7"/6""1 I
I I t ' I
10 Fan Pressure R~.~es (~n H?O) I i I L
I ;
I I l j -
10 Fan Currents (amp) I
I I
I
I 10 Fan Voltages (V) I I I I
I I :
; "
I I --
(oF) l I I i
Ambient .4.i r Temp. I i i
I
I i . I I -
Ambient Ai r Relative Humi di ty (::) ! I
v- I
I I I
~ ;
",,- Fuel Sample (.,,) I ! \ !
. i
t
, V (v) I ! I , I
Ash Sample , ! i i
I
. I I i
Boiler Heat Rate (BTU/kw-hr)
j L.,.- i r-- - "'''--'
I '--.--... -...-- ,---,-- ._.---~,...-
' I
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Steam-Electric Station:
UJD(.' ~Q
~
,,/; ..I.
~/~t;'H~_~-
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Unit: d::l= ~
Da te: ;i - I '1- 7 J
Start Time: /).' 1./;' 111'\
"
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Electrostatic Precipitator
Date Sheet 3 of 3
-
: Tim (m; n )
I Parameter, -
" j't.l,' /; ~;I-;;- I 1
j it : ¥-6-
~ t
\ Inlet Temp. (oF)
;
1J""J -(-I L~~- -
, Inlet Pressure (; n H20) I~:o( Gh"~ /3 5
I ," , ~ I
, .,t.7 .3 3
- ".S' -~-----i--='
; ( () r-)
Exit Temp. I
I
~
Exit Pressure (;n H20) , ~_.-
.... -~ --
Rapping Cycle Pe r; od (mi n .) .
i
=1=--
i Con troll ed Spark ;ng Rate (sparksjmin)
'
(KV) -- -_.
Operating Voltage j) ~ "], -
(,?"A..~ ~ ,):?..fA';'(''''''''' .'1- 2> {, ~ 1/1- 3 (p!:J Ir.t 3; (., ~- .4 It J1-
, -{ .- -
£, ;3.:>0
C 370
? .t.:""S'"
/) .?-~
£~fo(7
13 350
C :3 '7D
1) ~ 5''(7
E 3(;.0
B :; ~- b
Co 3.70
p 3 5"6
E ~ L- 0
8
C-
D
£:
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i '/ /
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- ---"",-.,,,-
15
Q.
1>
E
.---
13
c.
9
£.
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;;;-~ea~-Electric Station: UJ:>f"'..o &{:-~..-~~
Un'.. t. '/+ -
I . --- u
Date: ~ -j.~ ~ 7 {
Boil er
Parameter
'/. '\ /)." ,/ r~
f'~""-J""---r' -, , .~~... I ~ ~.,
(32)
-- "
Data Sheet 1 of 3
',,/J -.1.
X:: ~-~;;.~-y ().J.'.:',
r
Ti me (mi n . )
. 8: ~D /,.OD I cr/ ~D 110,:0 c> ,'/o:~o' '//: OP
Gross load (MW) I q--'
£ --"---- . I" '.-. ---.,-.1'------'''''1 "', ,--.'-
Net Load ( t4H) I
. ,
.1 I I j~=- -::~,. < .'" :
-.' I I ._I,.._.,-----_.~-,._-_..
-1 .-1 f I L L_-
I I . ! I !
'lJ. 00 H~' \luc':-~+--~oo-+--'-' .t770(':;J..:--hr.3o-;;-3""""~){--
5'-o~-4 {I 0 ,;-~-~~~f;;cc/i1rtt: C~r:i~1 (> C>'~ D :d !jt.,-;:-:-;,;,~q-I-SOO-(:;';!
~.r . ,- I L. ' f '1---'---'
,L ILL 1____-1-_---
I ' ii", '1
r .' T i r~1--==~~~~
i I ! [. "-~r~J:==
-i-- -r ---!-., -j ..j-.-1---
: : i I ! I
; ,-_! ----
46 9 ! 16 (p i 'I? (/ ! ¥ ~ 8, - 11 (~7 LL/ (': '} r~7 G 9
! Ii, --...---\ 1----'
---- ---_.---~.i. ----_. _.l~_.-_.. ........... f ~ l._---_J-_._-----
. -'t"""----/,'-- ! f
i I:' ., I
! i 'I i
I I . .
-__I
Fuel Flm'lRatL (1 bm/hr)
-'----"-
Excess Ai r (~~)
-----------------
02 in Flue. Gas (%)
-- -.--
C02 in Flue Cas (%)
S -t 131 . --.. ':j~;'-sr"'! ",.1 ~ 13:::- C. ()(,.10 C' )
00 0\'/1 119---;'- ,., .. .
..._'::7...-2..~~ ')( R D,::1, i '/;1 !'(~i> )
Boiler Feed ~!ater Flow Rate (lbm/hr) ~ ,
, t
Boiler Recirculation Pump Leakages (lb~/hr)
----------
.. .....---
Boiler Inlet Feed Water Temp (oF)
---~--. ---
Boiler Exit Steam Pressure (psig)
.--..--.-- -
Boiler Exit Steam Temp. (oF)
-.-- ~._----_._-----.
" Reheater Inlet Steam Pressure (psig)
',.-.--.. ..--0"___'"''''''''-''' ..-- .- ,'" "...-- .. ' '0" ._.--,._.~~---.- - .
Reheater Inlet Steam Temp. ( F)
."'--~"""
-. ..--- -.._--~_.. .._--_...-....~._._-_.
Reheater Exi t Steam Pressure (psi g) :J- r /9
.- -'. '~"'''---''''''__''''_h____'-._.
Reheater Exi t Steam Temp. (oF)
-----'-....-..-----.,--
(')
I
\0
II.)
,
-j 1/,' ~o
--,----
.
I
I
I
I
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'.
. Steam-E1ectri c Stat1 on: uJ o'(~'e.e
Un it: -:t:!. ~
Date: d-- - ~fJ- 7 .
ce;",,--, Ul.AAJ-e-.I
n ""J
.,,),.9..:".J..Z,-=-;:-~---_! I. PJ'<>:9.. . .L Q~J~ ~_::~2- j J..:--~9~_.
:Turbine (lbm/hr) I ' . .
Steam Flow Rate ! , ~
Condenser Press ure (in Hg) i ---1 . r-'
-"'.".-""-----.-.- -----_-....:....... ..- t -- .-'" ------....-
Boiler Flue Gas Exit Temp. (OF) . i I'.! .
FD";" p;"'~;;'r~-Ri-'-~~Ji OlD) .5'0 'f , :2- 7,7 . - ~,a !~~2~Z::::- ~ ? :e-i ~.:J; L? , e- 77'7,;-::
'.". .-.----.,..---- )(, 2 ~D - :2~.' ::{Ii,:? l d.,j.o ~.2- t?-:c....~ J."?,y /;/.7
...... FD Fan _curr~~:~_~~~p) I.*D ~~-; -;;o~-~~o '~~'~I'-;;Jr)-- v;~- '/bq ~~'.2~ r~::;"-}~~.';r::~':~-'- I"~.';'-
v' ( ) 'II J!J I r , ."- --'.I~ t/- ~ !J I A---1TTa--i:.1"
FD F~n Vo~~.~~_e~- .~._----~ 4 4~E--K...~~~O 'fZ,t;?j ~c~o '!./£~ ").0 ~2/)! J;'Po rJ~J(\ :~ LJ.j~~~:..
:~ ::: ~:~~~~~;~~;.~-~.~~O). ~-~I--:"'-_'-_".~---~--~ ~:_~--J-_.-
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I I ! I i I-
. I I _._..._~------
j I i I! i
I t------;--- -,----~_.- ~ .. -.----
i: j! I
' f) I 1
.1 i ! 1 1. --.'-'1--'----
I : I j-_.! -_-1_--t--~.._--
I: I j i'
~ .-......- .-.. .... -_...__...-.:.-._._-~~--~ --_.~_._.__.._---_." 1.....:......--_...--,- .
j i : I I j j
1 , j ,! .
: -------_!_.. ~._-_.{-_._-_..~,_._.._.._.._--- -""-"'''''' ..'
I ! ! !.. i.. !. I.. :
ID Fan Voltages (V)
Ambient .l\ir Temp. (oF)
Ambient Air Relative Humidity (%)
-----
.--./ Fuel ~ample (v)
./ A~l!-~~~P.1~ (v1
Boi ler H~~LRate (BTU/k~=hr)
()
I
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-------
Steam-Electric Station:
(;)('0-\
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Ij..........~-
r,
\',~:~ ....L"".. '.._f. _.~
,. .
:~.:.£~:!, ?~~f-
Date Sheet 3 of 3
Unit: -pi ~
Date: .:J... -:;.6.. 1l .
Start Time: '8;.3;0 _kA-
. Electrostatic,.Precipitator
Parameter
Inlet Temp. (oF)
Inlet Pressure (i'n H20) A:v 11"':ri..,.GH~
c9\.tT
j 8; ~~ 9:' Q b 9.._~ l>.
I I . i J
f71 }j I 'c: .6;. ';:5" I-T - b
fd. J ;?.':8. ~., ~~.~ f~'./ :t' g sZd-2.!..S
/b:3o
/.' :; (')
-~------;u-_. . ........ .. -....... . ....-... " ...j..-. '........-...-..- -'--'-----.--.'''-, l' ___a
Exit Temp, ( F) ,
,
[ ,
I I
- ...-
Exit Pressure (in H20) -~-~+.
'-'---.-"---.' ---- '''_1_..... ""'..~ ." .. .....6.-...~ I I-i~ J
Rappi ng Cycle Pe r; od (mi n .)
- -
Cor. tro 11 ed Sparking Rate (sparkstmin) ~-3(:;; ~3';o . .
.------------- - ~
Operating Voltage (KV) (!.,..~~. .),
--- (1H..-...., '~4'!I I-l 3S-o !n 350 It 3 6.5'
I ,
~.r
!
1
._,i_- -----
8 ..
~,9 -~..!.-?..!-fQ.:. -~d.. J). ~ -
i
I
--:----:-j---.-.--
i .
--"'.-:...-r--'-'-'----'.
IJ 3(-;>0 (3. 3 (of.> /l/ 3 6 D 13 3 G-, (..., ;' .3 ~-~- I} 3 ~-:r
..:.
C 36 Do C. 3(,0 C- 3 ffD IJ jc'D D
E 37D ~ ~ {,~ --3" ... ""c..4~
£ :3 ']0 E E 3G~ .:::: lk. ~~ '- ~.'-)
:3 7e>
I
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.-_~.. _..~_.----. --- .--...-". ~...
b2_9-~ _30 o'
I; .3 G ()
.' 360
L.
~ ~-
,..)~O
()
I
~
~
\
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, .
. .' -
Steam-Electric Station: UJooA 'R.'voQ.'I'
Unit: f!. !:J-
Date: '2...2..(.:)- 7'
,-fh woQ-,.I "V \ -c1 _-t
Data Sheet 1 of 3
i
. ~
x -;: 1.r~ ~~ ~.
8011 er
F
i
. --
I
(mi n.) ,
. Parameter Time ~
,
"; I;': 00 J)...' 30 I,' (:;) (;) I.' 30 "to' 00 ~,t ~ (,) I ?J " 0 C:o
,-
, load (MW) I
Gross
- , - .. -'-r-~'
i
Net Load (r"~l)
.',"
,, -
J Fuel Flo'\' Rate (lbm/hr) I I I
..
Excess 'Ai r (%) ' I
-
. !
' °2 in Flue Gas (%) I
'
, C02 in Flue Gas (%) . i
:
, Soot 810...11n9 ..L 'AI .s '7'£7 N -r ,b- B 2. b- (X! 0 0) )( '/:J. oc:ti l/~ (') P ::' ' t/-OD-:r:t. '10/ 00 1'1- +'1- Oo.:lf L/ C/- OD /.:
~ /,./ F""." ,." ~.Ct4 {! ?(XIOO;;) )( -,,~c> 00 tl v.;J OD 0 U / 9 OOl~" £/.IODO#. /9 ono.:;J ~.J I OD[.' J,
I I (lbm/hr), I !
, Boiler Feed Water Flow Rate .
,
Boiler Recirculation Pump leakages (lbm/hr)
I Boiler Inlet Feed Water Temp (oF) 1
; I
j
--
.. Boiler Exit Steam Pressure (psig) I
1 Boiler Exit Steam Temp. (OF)
"f I
: Reheater Inlet Steam Pressure (psig) I
I
j I
~---- --- '.- _.' .-.. -.. -. -. ...--..-- ~ - . _.'
1 Reheate'r Inlet Steam Temp. (oF) I "
.....----.-. I I I L/7 /
! P-eheater Exit Steam Pressure (psig) 5T J '1 ,-/-(;;5 I Lot L" 9 I l! .' (~, 1/6'8 ~73 '1- 7(;>
! I I'J (.)
,'0 Rehcater Exit Steam Temp. ,(oF) I I
: I I I'~-'-
U1 '1 I ,-.. . I
I
! J I
. .. '
,- - -, '--' .....- ~ - ~,,'.'.._-,.-,
-~- _...- ".' "',_.__.----~-- .__.~-------.
. .'.. ~ ._----
-------
.
:
~ .
.Steam-E1~ctric Station: vu ~ ~~
Un it: .p..-5"'
Date: ~r-;2. t:> - 7 I
p~~
~~
Data Sheet 2 of 3
Boil er
1 0
0
; Parameter Time (min.) .
~
; I c<.' ~Io
~ /':<.00 I)..: 3u /; 00 /:30 ~:OD .3 " c '0
- .
~ . (lbm/hr)
:Turbine Steam Flow Rate
.
; ~
Cond2nser Pressure (in Hg) ,
I
I
j . Boiler Ai r Inlet Temp. (oF) .
,;
:
. Bo; ler Flue Gas Exit Te;p-: (OF) I
----'.'.' ..
, FD Fan Pressure Ris~~ qn H OJ Sf) 13 ;). ~3.1 ~ '1,.~ ~g.D ;L B d3 ;z e . .:3 ,;< '? ~ ""
' 2 ~~f);CF .." '.i-~' ,""~' ........~- ,.Q'-._.-f",.-':-.;""-'" ~--;j'-."- -.2'~',1 .:J- i""i--- ._'"~-~
,! .1 f) l/:J6 I,I.:/D l/?O 1../;>(1 0
~ a.-- FD Voltages (V) , 11; I~ il F. , V-f I!. 1'1 ~ i4- .!.-'> 4- /3
Fen . iJ ~j' ! '-1-) c) 'I ').() L/;;.o Y;20 '-/,),lJ II :;'..i)
'-/-;)0 t/;? c> (,. ~.., (,I:2D tj;JO 4/k)
-------
.
Steam-Electric Station:
LV" 0 d. '"R~ Ve.4
1=>0 w ~.. .s" d; 01.-
Date Sheet 3 of 3
i
j
,..
Unit::Il ~
Da te: ::2.. .).. v - , J
..
!
1
Start Time: S: 30 fJ r1'\.-
Electrostatic Precipitator
"
P a ramete r Timo (mi n )
/)...'00 I ,). ~ g tJ :;.: (;) C/ I' :1.1.?O
I,' DO I,' ,30 ;<.~ 0
-
r, (oF)
, Inlet Temp. 61 R /' I J'
/j -
Inlet Pres$u're (in H20) /1/ y ;IIc:.~;"r~ + If /3 I 11 t! D r-I e 4 //
2.S -;).. I ;(.2 .J ~,~
Go /J .s ,,::> w c'2 J /. ~'61'" l~.1 ,,1.8 ;1. / ,,2.fJ ;J,.J u- S r~'! ~
(ur) - r .~--
! Exit Temp.
! 1 1__-
Ex'it Pres S ure J. H20) -1-.---
1 l. 1n .
.. . --- .
, Rapping Cycle Peri od (mi n .) . I
I
----
Controlled Sparking Rate (sparks/min) ..
-
i Operating Voltage (KV) IJ-re r..".c. 7.,.;".. -:; "'I -- /i 3~O /I.~ :,,:, ;\ fI 3-...'>0 14 4.370 /1 370
1-1 .~ U:. ~ 3 hD
: ...,J -
.-- ...
13 30~
c: 3";:;-
!) .3 (..,u
L- '? ..;
. c:. ;;; ~~)
/~ J.: 0
- '1'
f1 ..
. I" '.)
L- ~,~ ,.
j; 36D
. fL .5?O
D 3.5' S
r; 37D
f3 j'-o
(. :p '7 '(j
P 3(;,0
;
- ...' I' --.
.... ." ~....
,- ....
d.300
~. 3 '7 5'
f) jl:.C>
£ 376
135(;,0
L!.. 3 70
P 3 Coo
£. .3 70
fJ :; '" Li
~ 305.
. ()
, I
.\0
;"
r
/1- 3 (Q C:>
(! .3 70
[) .3 Sa
[ j 70 .
..._--..----.._._'~------ -_.....---_.----~
-------
Parameter , Time (mi n.)
3,'.3D L.J. " . 0 0 L/ . ",;J () ~): 0 D 6' ~~D C. . ., '> I " .
, .J . ., t:... { ("."....)~
Gross Load (W~) ,
- -.. . ""--'--r-'--' .-. .
Net Load (MW) I I
.. 1-1
' Fuel Flo'" Rate (lbm/hr) I I
i
1 , I . - ~ L_~-
4 Exccs s Air (%)
I i i ..
~ 02 in Flue Gas (%)
I 1
-
; (%) ! I I i
~ C02 in Flue Gas ' I
I
,
~:l- N S... 'd J\iT' 5'" j~ 2. .s (X J() '0') 2/00# ;]100# ¥ 3 00 -JJo 'I 'J 06 0 ~!- (../:j D (1 'J ~'.. 8 I D 0 .,I i -
Soot 81 O'!d ng-/-; --'(J:..~-' :'.--(:~.:;r-'-:) --_._...._'~-' ...- . ~ . - ..._~ J ........--..-.
l t>c.... ./ (' hi),>, ,. /,('..:>/' 7-j &> 0 -o-21l/c,t () {> 0 J! -s:;oo';'n 0 'ZiT6 c;:;" f! (",7(~C)(l11i
. I
Boiler Feed ~la ter FlC7N Rate (lbm/hr) , I
,
5 Boiler Recirculation .Pump Leakages (lbm/hr) I !
, i
I -
Boiler Inlet Feed Water Temp (oF)
! --
J Boiler Exit Steam Pressure (psig) I
-
\ (oF) I I
Boiler Exit Steam Temp.
. I I
i Reheater Inlet Steam Pressure (ps1g) I
I
--.- ..---...-...-..-..-..... -- "P--...--- - I .' ! .-
Reheater 1n let Steam Temp. (OF) :
I
--....-----. I
, Reheater Exit Steam Pressure (psi g) 6- -r I 9 1./ (C, 'i v~q Y-JO 1/ .. -")
, ,!-70 e.'~) '-170
j !
I -
n ~~heater Exi t Steam Temp. (OF)
;~ !
-
m .
-:
Steam-Electric Station: 10o~d ~'.~e.-r
Unit: ~ ~
Date: ;J.- 2.0- 71
?~WQ-( c-1.:.~~\'o-v-...
Boi l:er
"
,
I
. : I
-. .~...__. ,~---,,,,.,,,,~4"'--- --..--.-._-~--~ """~"'-~'-' ..._...#. .---_..__._.._-"._~._-,
. . - -...'------- !.-. ___1.
Data Sheet 1 of 3
-------
~
- . ..
I"
'.
.tteam-E1~ctr;'c Station: \.J) Dt' ~ ~: \\<2."
Unit: ~r\- c-
- ...;J
Date: J..- 2. t;)-7 t
\yOl..l)oy V \'1Kt
Data Sheet 2 of 3
!
;
"
.!
i
':~
",j
.!
~
'i -
Boiler
'
. f
Parameter Time (mi n . ) . .
, 3: 30 t./ .' 3 D 6-;'t!J D .=;-,. -=3 b (" ',DD t ,:~ 7,'oo~.~
l"",.- b
I I
I :Turb1ne Steam Flow Rate (lbm/hr)
,
j Condenser Pressure (in Hg)' . .
I
I
. . Bol1er Ai r Inlet Temp. (oF) I
'
I --_J }-
, (oF)
i Bo; ler Fl ue .Gas Ex1t Temp. I
'
\ --..--.....
FD Fan Pressure Riser)iI) H20),21)/~ ;Z7.~ ~'f(lf- I ').. 7,. I./- . .18,0 ~ 7.9 ;;"B. t?
"f
-.----.' , .s D I '">1.7 ..?""f:h ;J. f?~ ~"J~ , .--:;--- -
- ;:,~,t ~'t.-.:3 -
~ A ~ II f? -
~/ FD Fan Currents (amp) {j I t1 ,q !:3 ,4- ;'; It- ;.3
1 (/;10 ., 1/.'" lJ'1.0 Y,:;Jn II ,~) I.:) I t/ :.' r:> I.J.~
. -'
ID Fan Pressure Rises (in H20) I !
j I
i
.j ID Fan Currents (amp)
j
1 ID Fan Voltages (V) I
1 '
"
Ambient Air Temp. (OF) i I ! I
.
. i
~ ~~Ambient Air Relative Humidity (%) I
.
;
' Fuel Sample (v) I
i ...... ....--
t
~ -../' Ash Sample (~ ~ I I
!
1 Railer P.eat Rate (BTU/kw-hr) I
!
I I .,.
\D ,
\D .. _...' ,. ._-"--,----~.._-._-,____,,.l. ~_J...~--,_._,
-------
. .
. .
Steam-Electri c Stati on: Wo ~~ '\(~-J.g..y ';Yow...~ 'r" '-:j.)){,. ):- -I--
Unit: :t:r ~
Date: "2. -.2 D - ') I
Date Sheet 3 of 3
;
"
j
t
J
Start Time: B: 30 It m
Electrostatic Precipitator
"
.
Tim:> (min ) "
Parameter I
- 3:~ 0 L./-:oD l../ " 3 0 _':;:'00 $"' ~"O c.,. ',(?(") (,,~O
j (oF) ,
Inlet Temp. ;
1 .
; Inlet Pressure (in H20) /l;y flea-l~~ f1 .(3 ~ 6 N- /6 n 0 I~ (:) II- 1.5
<;,11-5 04..+ :l...} ;2..
E J;?i?
13 .:J 6(!>
C ..3 r?D
e7 -3 bD
E .J 7{)
~ J~o
~ j'?D
D.3t;;,o
E3~-
/} .5 c: .:;- B :3 h 0 & 3. (" S- i.'
f. 3 ~ D y....s-- p '3 G~" J) :3 &~ ~-.)
e. 3 c. J>- . E j.:r:>' £ .5 G,o 3-
(')
I
~
o
o
.~-- '-'--' ,-...
.'~' .." ------.-... - -.....~.-
-.--.._----~------------_..__.
-------
APPEND IX D
-------
. Part 10, p. 3 of 8
. .
. .
FIELD t.10ISTURE DETERj.1INATIOII
. _. . , O'
East Duct Exhaust
Operator C. C. Gonzalez
Location
r
Test
Date
M(',o\ ')-~()
'".--"
.. ') J,:
Preliminary
'.By Absorption:
. Barometric Pressure 29.9
Feb. 16, 1971
Clock I Meter F10\'/ r.1eter ~1ete r
Time (Ft3) Setting (CFH) Temperature, Tm
1.0 0.1 48.
. -
. '-. '. .
--. - -. ..
.. - -
Tube No. Weight, grams
Final In i t i.a 1 Di fference
1 79.7 78.5 1.2
3 87.8 87.5 .3
.
(W) = weight of moistu,'e collected = 1.5
~ r10i sture by Volume = 100.. W
. (375.PB.Vm'r
r + 460 \~
. m
% Hoisture by Volume =' 6.4
By Wet and Dry Bulb Te~perutures:
Wet Bulb Temp. of
Dry Bulb Temp. of
(19/r.7)
% 'Moist'ure From Psychometric Chart
-------
Part 10, p. 2 of 8
PRELIMINARY
VELOCITY TRAVERSE FIELD DATA
Wood River Power Plant
Plant
Test
EDE-1
location
East Duct Exhaust
Date
Feb. 17, 1971
Operator
N. A. Blessing
C10ck Stack Stack JbP]:tnZl~tI~~- I
Time Point liP, in. H20 . T crnp., of Pres., In. Hg It,p x (T +1160'1*;
~ - - - -. .
10.07 IAVQ. - -
Hole 1 1 0.1 0.08~ 280 0.292 I
.--
I :).08~ j
2 O. 09 , Q . 08 - Bar Press 29.9 I
,
i ;
3 0.1 [0.095! 0.09 75 Static Press 1.5 0.312 !
4 0.1 \0.095\ 0.0~ 75 0.312 !
\0.085\ 0.09 75 . .
5 0.1 0.304 '
I I -_J
-6 0.1 I \ Stack'Press 0.308
[0.09 10.095 Avg.
0.09~ 0.0951 0.09~ j
7 In. Hg" 30.01 0.308 I
I
I -..J
, . - I
8 0.10~ 0.105 0.1 )5 . 0.324 I
I
I i
I i j
9 0 . 12 '0. 12 :0.12)
._-~
I
10 0.105 0.12 0.11 0.335 I
J
! I I
11 b;12, 0.13 ,0. 12 0.354
I
I I I
! i
I ---I
.j I . .I
'**
Calculation columns. not Field data
Cor,;men ts :
NCJ\P-29 (12/67)
D-2 - .
-------
Part 10, p. 2 of 8
-...- .. .
PRELIMINARY
VELOCITY Tr~V[RSE FIELD DATA
(CONTINUED)
Plant
Test
Location
Date
Operator
Clock St?ck Stack 16P I
Time Point liP, in. H20 - T crnp., of Pres., In. Hg liP x (T +460 1* x (T +CIGoY:
- - -.. I
~~ -
{9.k. 2 1 ).06 0.06 0.0, 280 0.245 .
2 b.07 0.08 0.0 5 0.274 !
I
;
3 p.075 0.085 0.0 0.283
4 p.075 9.085 0.0 0.283 ;
I
. .
5 ).07 9.08 0.0 5 0.274 !
6 J.07 0.07 0.0' 0.265 I
i
- .----
7 b.07 0.08 0.0 5 0.274 i
I
I
--1
, I
8 b.09 O~095 0.0 25 0.304 f
- I
!
9 ).09 O.ll O.U I
I
10 ).10 0.10 o.lD 0.316 I
11 J.ll. O.ll' 0.1 0.332 \
,
!
I
- _~__-i
. - t
'**
Calculation columns, not Field data
Cor,',ments:
NCfI.P-29 (12/67)
D-3 .
. ') I
'./ ,
-------
Part 10s p. 2 of 8
PRELIMINARY
VELOCITY TPAVERSE FIELD ~ATA (CONTINUED)
Plant
Test
location
Date
Operator
Clock Stack Stack AP x (T+460!* l/AP I
Timc Point liPs in. H20 . Ternp:s _o!_- Pres os In. Hg x (T+t1GOT':
-- I
-
Avg :
flo1e -3 1 0.06 0.05 0.0 55 280 0.235 i
.-
2 D.065 0.065 0.0 )5 0.255 !
,
-
;
3 0.07 0.07 0.07 0.265
4 0.07 0.08 0.0 '5 0.274 '
b.06 0.07 . .
5 0.08 0.265 !
6 0.06 0.07 0.0 >5 0.255 I
I
- -_-!
7 0.08 0.06 I
0.0 0.265 I
I
I
8 0.085 0.08 0.0 25 . 0.288 . I
,
.
i
9 0.08 0.09 0.0 5 0.292 i
~
i
10 0.10 0.10 0.1) 0.316 i
----1
11. b.09. 0.10 0.0 5 - 0.308 I
I
I
- !
- t
'**
Calculation columnss not Field data
COf,',men ts :
NCJ\P-29 (12/67)
D-4 .
-------
Part 10, p. 2 of 8
PRELIMINAJW.
VELOCITY TRAVERSE FIELD DATA (CONTINUED)
Plant
Test
Location '
Date
Operator
Cloc~ Stack Stack (T+460j* Il\p t
Time Point liP, 1 n. H20 - T CIl1P:, of Pres., In. Hg liP x x IT t.60""':
-.. \ 1+' );
nv~ - .
Hole 4 1 0.07 0.07 O.O~ 280 0.265 i
.-- -
2 0.075 0.08 0.0 t775 0.278 ,
,
:
3 0.07 .0.08 0.0 ~5 0.274
-
,
4 0.07 0.08 0.0 5 0.274 !
- .
.
5 0.06 0.07 0.0 5 0.255 I
- - 6 0.065 0.07 0.260 I
0.0 75 !
------
I
7 0.06 0.08 0.0 0.265 I
I
.-----i
8 0.07 0.09 0.0 0.283 - i
I
- I
!
9 0.08 0.09 0.0 5 0.292 i
--------1
10 0.09 0.10 0.0 5 0.308 I
I
--t
11 0.10 - 0.10 0.1 0.316 I
I
i
!
- I
"**
Calculation columns. not Field data
Cor.-,men ts :
NCJ\P-29 (12/67)
D-5 .
-------
Part 10, p. 2 of 8
PRELIMINARY
VELOCITY Tr~VERSE FIELQ DATA
(CONTINUED)
Plant
Test
location
Date
Operator
Clock Stack Stack {t,p I
Time Point LIP, in. H20 - T c~6.~ of Pres., In. Hg LIP x (T+460!* x (T+ftGof*;
- - . -
Avg -
Hole 5 1 D.09 0.08 0.0 $5 280 0.292 '
.
._-
2 D.09 0.09 0.0 0.300 !
I
---
3 .08 0.09 0.0 5 0.292
4 .08 0.09 0.0 5 0.292 ;
!
-
- .
5 .09 0.09 0.0 0.300 !
6 ~.085 0.085 0.0 5 0.292 I
----_.J
I
7 D.07 0.08 0.274 i
0.0 5 I
---1
. I
8 .08 0.09 0.0 5 0.292 I
I
- !
9 .09 0.11 0.1 0.316 I
----~
l
10 .10 0.11. 0.1 5 0.324 I
~
I
11 .10 0.10 0.1 0.316 ~
i
------!
'~I
'**
Calculation colu~ns. not Field data
Cor,;ments:
NCfI.P-29 (12/67)
D-6
-------
Part 10. p. 2 of 8
-
PRELIMINARY
VELOCITY TRAVERSE FIELD. DATA (CONTINUED)
Plant
Test
location
Date
Operator
Clock Stack Stack 16P I
Time Point 6P, in. H20 _Te~.~ of Pres., In. Hg liP (T+460j* '-~ql
x x (T+460) :
- - -.. .- - '
-
Hole 6 1 0.13 0.13 0.13 280 0.36 i
.--
2 0.125 0.130 9.1 75 0.358 t
i
I
-'--
i
3 0.145 0.135 0.1 0.374
4 0.14 0.12 0.1 j 0.361 i
I
-------~
~ I
5 0.11 0.11 0.1 0..332 !
6 0.10 0.10 0.1) 0.316 I
I
- -----
7 0.105 0.095 0.1) 0.316 i
I
I
--- ---!
8 :>.10 0.10 o.~b 0.316 . I
I
I
- i
9 :>.10 0.10 0.1 0.316 I
I i
10 :>.11 0.11 0.1 0.332 I
J
11 ).12 0.12 0.1 0.346 J
I
i
-------!
- I
'**
. Calculation columns, not Field data
Cor,~ments :
NCJ\P-29 (12/G7)
D-7
r;
-------
"--
.._~~
:- c. I C 1 G, fJ. 4 v. 8
Plant
Wood River Power Plant
Run No.
EDE-1
Date
Feb. 18, 1971
locaticn East Duct Exhaust
Op.::rator
N.A. Blessing
I
. I
Poi nt I ~~~;k
_Start i 1HO I
Hole 1-1) 1115 I
2! 1120 i
31 1125 I
41 1130 I
Start I 1156 !
'[701 e -2 -1 J.-11l~
21 1206 I
-" 3 I 1211
!I I 1216
Start I 1300
HOTer:11 1305
2 i . 1310
3 Ll315
41 l320
I
I
Dry G~s
tt.etei, CF
738.20
741. 30
7q.4.20
747.00
750.24
750.2l,
752.76
755.40
758.40
761. 27
761.27
Pi>,;\11CULt"l11:. FIL..u OAT"
VERY IMPORTANT - FILL IN. ALL BLANKS
---.-
Read and record at the start of each
test point or, if single point
. sampling, read and record every 5
mi nutes. "
Sc:.ilpleBox No.
r1eter Box No.
1047
1047
Probe Length
10'
Probe H2ater Setting
130°
Orifice !:.H
in H"O
Des i rcd':'~;ctua 1
1.15
1.05
.05
I 1.35
I 1.50
! ~:;~
I 1.01
I 1.1
I 1.12
I 0 36
c
r
Cc.;;;m~nts :
:~C;"P-37" (12/67)
t::1
I
00
. .
I
Dry Gas Temp.;
of
Inlet ! Out:lct
1 64 I 61
L:72 I 62
: 77 I 62
82 i' 66
H l ~~
! 71
I ~;
\ 72
83
88
93
73
I
A.'J1b;ent Temp of
63°
Bar. Press. "Hg
29.9
Assumed Moisture %
7.5
Hc~ter Box Setting, of 250
. Pl-o~e Tip Dia.. In.~75-
! I St:-.c".
lr.1pi:lger i St\:.ck -- '"
TC1~P' Pr2$S I' r- p
0'- .;.., "'''. -:- ~~.~; "
r ,d. 11~
29.~
A v> -:-TI-80 \
I 0--
A vcr . L.2lill
Ava. 280
_\ ?gOl
I Av""". ! ?R() I
1~,-]-2W--1
lli~.t.1L-J
I I '
l\\lr.. I'" !
: Av~__t 2LO
I A I ~".
\A~~~1 ;~~
--l Avr>,. I /80
I Avf1... i 280
PUmp
I Va:uum
.. In. Hg
lG"uge
I 5.5
5.0
. I 5.0
I 6.0
i 6.0
\ ~:~ 121() I
I 4.5 1250 L
5.Q -1250 I
r 5...D- 21() I
I 3 5 Lz.s~
Box
Temp.
of
0'
68
~o
71
71
I 763.85 i 0.05 I 0.75 Oj7 77 ! 72 U~~250 68
I 766.40 I 0.06 0.90 I 0.9 I 84 I 72' ~ I.. 0 ~o 65
I 769.03 I 0.07 I" 1.1 I 1.1 I 87 73 i? ')() 70
I 4.2
i 772.02 j 0.07 i 1.06 I 1.1 l 91 I 73 I 4.5 1?50 . 80
.
Pi tot
in. H20
~p.
0.075
0.070
0.070
I 0.485
I 0.10
I 0 05
0.05
I 0.065 . 1.0
I 0.07 ~1
I 0.075 1.15
-------
......~
- rUltlv,t-I.~",,8
Plant
Wood River Power Plant-
Run No.
EDE -1 CONTINUED.
Location
East Duct Exhaust
Dz:te
Feb. 18, 1971
N. A. Blessing
Op~rator
Clock
Point I Tir::2
Hole 4-0 1453
1 I 1458
2 1503
3 I 1508
hi 1513
H()le 5-0 I 1545
11 1550
2 I 1555
--31 1600
I+! 1605
Hole 6-0 I 1629
11 1634
2 i 1639
3 I 16Lf4
41 1649
I
I
,
~
~
I
Diy C.:S
f'1etei, CF
772.17
774.55
777.23
780.17
783.25
783.25
786.27
789.27
792.28
795.58
795.73
759.43
803.26
807.12
811.Lf2
Pitot
in. H20
I1P
0.06
0.06
0.06
0.08
0.08
0.07
00075
I 0-~08
I 0.075
O. 100
I 0.115
1 0.120
10.120
I 0.140
i 0.130
I
PH1'.I.LCULt\11.. FII..L..I.J DAl..
.
VERY IMPORTANT - FILL I~.ALL BLANKS
----.-
Read and record at the start of each
test point or, if single point
sampling, read and record every 5
minutes.
A'J1bient Temp of
o
63
St..i1p 1 ~ Box fh.
Bar. Press. IIHg
1047
29.9
~(eter Box No.
Assumed Moisture %
7.5 -
1047
Probe Length
Hc~ter Box Setting. of
250
10'
Probe H2~ter Setting 0 . Pi-o!)e Ii p
130 Di a ., I il. 0.375
I PUii1p
Ori fi ce liH Dry Gas Temp.; Va:::Ul.:m Ir.lpinger St.:ck II"'" - c'<
..) I.. (~ ;
in H,.,O 0,... In. Hg T:::np Pr\:ss I T-."p
r . '';:.:.
lO\:s i rcCi--': ';ctuZll I Out:l et IG.Jug2 0'- in. " of
I . r ;'9
0.85 '
0.85 74 72 4. 0~7L- ')
0.90 0.90 76 72 4.5 250 64 -9..JL-~
0.90 0.91 81 72 I 4.5 250 64 0.70 1280
1.22 !~~ ' 86 73 I 5.0 250 64 -10. 70 J1-~~-i
!
~22 I 1.20 i 88 73 5.2 250 I 64 0.65 i 280 I
I 1.07 I 1.07 I 73 73 4.9 1250 t-:~ I 0,80 ~
,---- I
I LIS , 1.15 76 72 5.0 250 I 0.80 280 I
I 1.25 1.25 80 72 I 5.5 250 66 I 0.70 I 280_-j
1.15 I 1.20 80 73 t 5.5 250 67 0.80 I 280 . I
I 1. 52 I 1.48 i 90 73 6.5 ,250 I 69 !0.90-L?80 1
I 1. 78 [-1.75 I 74 72 I 7.3 [250 I 75 !-g:~r r~g I
1.85 I L85 L78 73 7.8 -'250 ! 67
I 1. 85 I 1.85 I 87 73 1- 7.8 1250 73 10.85 295
! 2.15 I 2.20 I 90 73 9.0 j250 I 74 jO.85 !310 I
I 2.0 I 2.0 90 73 I 8.8 ;250 I 74 10.85 -1310 i
J '
I I I I L
I I !
CC~m2i1t$:
:.:Cr'iP-37' (12/67)
o
,
-------
Part 10, p. 4 of 8
PARTICULATE FIELD DATA
VERY I~PORTANT - FILL IN,ALL BLANKS
---..-
Read and record at the start of each
test point or, if single point
sampling, read and record every 5
minutes.
Pl<:.nt
Wood River Power Plant'
Run No.
WDE - 1
Location
West Duct Exhaust
D~te
FFbruary 18} 1971
Cp~rc.to\'"
j
I
\ Clock
P-'''"!'''I..r.. T';..,"":)
'-' ; i. I.. I . Ii.,',.
1?tart ---_! nos I
1iole 7 -111 1110 1
------101 1115 I
91 1120 I
. 8 i 1125 I
! 71 1130 !
~~-c;U:-t-1 12 05 ~
fr!~i;le 8 -11'I-ulol
I 10: 1215 I
: 9! 1220 i
Diy Gas
1';2 t(; j'" ) CF
Pi tot
in. H20
tI P ,
537.51
0.10
0.08
I 0.07
I 0.07
C08
I 0.07.
I 0.05
I 0 OS
S(i..i1ple ,Box No.
r''IcteT Bo~ No.
Reston
Reston
Piobe Length
30'
: .
Probe H2pt(;, Setting
Orifice 6H
in H"O
D\:s i rccr-.:.: .';ctuill
1.2
1.0,
O~ 90
0.9b
1.0
1.2
1.0
1.0
0.9
0.9
Cor.:;ncnts:
:,:CAP-37' (12/67)
t::I
I
......
o
0.90
0.65
o 65
1300
Ambient Temp of
63
29.9
Bar. Press. "Hy
7.5 ,
Assumed Moisture %
Hez.tcr Box S2tti ng. of 250
Ir.1pinger
T:::~p ,
o~
r
0.375
Sted I St2.CK
Press \ Tc~:~p
\.", 11" Or-
11... i1~, r
. Probe Tip Dia.. In.
I ' Pump
Dry G~~ Temp. .\ ~a:u~m
I ;- 1 il. r.g
1 Inlet ! Ou'clct 1 G~uge
I l
1 I
I I
I
: i
I
I I
Box
Temp.
I of
1.5 I 250 70
1.5 250 70
1.5 250 70
1.5 250 1 70
1.5 250 70
~.~ 250 0
I 1. 5 250 70
1.5 250 70
1 5 250 I 70
i 2-80
I 280
280
I 280
i ~80
I 0 I
I 28
-------
Part 10, p. 4 of 8
Plant
Wood River Power Plant
Run No.
WDE-1 (Continued)
Locaticn
West Duct Exhaust
D~te
February 18, 1971
Oin:r~to:--
I Clock
I
i I
I Point T;..''''
i- i ' ,I..'~..
81 1320
I 7) 1325
>-- I
; Start I 1L~05
! Hol e lO-nl 1L~10
I lOi 1415
I
91 1420
i 81 1425
71 1430
, I 1445
i Stdrt
,
Dry G~s
!~ei:ei, CF
Pi tot
in. H20
AP -
0.06
0.06
0.07
0.06
0.06
PARTICULATE FIELD DATA
VERY IMPORTANT - FILL IN. ALL BLANKS
---.-
Read and- record at the start of each
test point or, if single point
sampling, read and record every 5
minutes. .
Sc:.i1ple ,Box No.
i-ktZT Box 1'\0.
P,obe Lengih
Reston
Reston
30'
1300
P\-obe H21~tei'" Setting
0.8
0.8'
0.75
I 0.75
I 0.90
F~:~~
Dry Gas Temp.
0,-
r
I Outlet
86
86
80
82
82
82
82
Ambient Temp of
63
8ar. Press. "Hg
29.9
Assumed Moisture r.
He~ter Box Setting, of
Probe Tip Cia., In.
I
PUiil~
Va:uL;m
I i1. Hg
G~U92
1.5
1.5
1.5
1.5
1.5
1. 5 I
1.5 I
1.5
1.5
7.5
250
0.375
Stt:ck I Stuck
Press I TC~::;J
. 'H I 0..
1:1. . 0 ..
29.98 280
29.98 280
I 29.98 I 280
. 29.93! 280
~9.Y3 I 280
I 29.98 1 2&11
29.98 I 2JO I
I .
i-101", 11-1J 14-50 I 0.06 I 0.75 0.75 I 80 78 1.5 250 70 29.98! 280 I
i 101 1455 I I 0.06 I 0.75 I 0.75 I 80 i 76 I 1. 5 I 250 70 I 29.98 I 280 I
, 91 1500 I I 0.06 I 0.75 I 0.75 I 82 I 80 I 1.5 I 250 70 I 29.93 280 I
,
81 1505 I I 0.05 I 0.65 I 0.72-) 82 k~H 1.5 i 250 70 29.98 280
L '
; 71 1510 I I 0.06 " 0.75 I 0.75 I 82 I 78 1.5 I 250 70 29.98 230 I
,
'Start I 1625 i I - I - I - ! - I - I 1.5 I 250! 70 29.98 280 '
,
~ole 12-11 1630 I 0.08 I 1.0 I 1.0 I 75 I 75 I 1.5 I 250 I 70 29.98 I 280
lo:::mCilts:
:':CP.?-37' (12/67)
o
I
t-'
t-'
lfilpii1ger
Tc:::np
o-
r
Box
TCi:ip.
I of
I
I
70
70
-------
,
Part 10, p. 4 of 8
PARTICULATE FIELD DATA
VERY I~PORTANT - FILL IN.ALL BLANKS
--- -
Plant
Wood River Power Plant
Read and record at the start of each
test point or, if single point
sampling, read and record every 5
minutes.
A:nbi ent Temp of
63
Run No.
WDE-1
CONTINUED
S~i1p 1 e ,Box No.
Reston
Bar. Press. "Hg
29.9
7.5.
Location
West Duct Exhaust
I-2cter Bo~ No.
Reston
Assumed Moisture %
February 18, 1971
Probe Length
30'
Hc~ter Box Setting. of
250
Dc:tc
Cp~rGtor
Probe M2,utev- Setting
o
130
. Pi~obe Tip Oia.. In.
0.375
I I I : ! PUii1~
Pitot Ori fi ce l1H Dry Gas Temp. I Va::ucm Box Ir.1pinger S"" ~~I. St~ck
! \,. (..L "'" f-..
, I r" i- DIY Gas in. H20 ---~ j) H?O I o~ . Iil. Hg Temp. :::::np Press Tc~;p
I p ..... I "IOC,~ r I
I , ",'"-:\ H~te;-, CF ~P D2sircd I Actu~ Ir.1et I Ou'c let Gi;:uge I of o~ in. Hg 0'- I
i .OHh i . I'. .'~'.. r r
I
1--nfI 1635 I I 0.07~ 0.90 I 0.90 I 76 T 72 1.5 250 70 29.98 280
I :
I
-------
1 '~
" ~.;
-."1
Part 10, p. 4 of 8
PARTICULATE FIELD DATA
VERY IMPORTANT - FILL IN. ALL BLANKS
--- -
Plant
Wood River Power Plant
Read and. record at the start of each
test point or, if single point
sampling, read and record every 5
minutes.
Ambient Temp of
.60 .
Run No.
EDE-2
Sc:..llple Box No.
1047
Bar. Press. "Hg
29.9
1047
Assumed Moisture %
7.27
location East Duct Exhaust
Hc:ter Box No.
FebLuary 19, 1971
Probe length
30'
Hc~ter Box S::tting, of 250
D"te
Op~rator-
N. A. Blessing
Probe H~~ter Setting 130'
Pi"obe Tip Di a., Iii. 0.375
I I . I PU;I1;J
. .
i Pitot Orifice lIH Dry Gas Temp. I Va::uL:m Box Ir.lp;i1ger Stt:ck St<:ck
\ I Clock DIY G~s in. H20 ~-----,--i~')O I of . In. Hg Tcmp. TE::r.p Press Tc::::p
Paint Ti,::~ r(~ete., CF liP Dcsired I Actu~l In1ct IOutl::t G~uge of 0- in. :19 or-
, I r r
I I I
; Start I 12h5 t 81.3.64 0.08'i 1.3 I. 1.3 I 63 62 5.5 250 58 1.1 280
I
~Ho1e 1-1 I 1250 I 816.88 I 0.085 1 1.3; 1 1.35 69 ! 64 6.0 250 59 1.0 280
I
;- 2 I 12~5 I 819.08 0.085 1.3 1.3 t 71+ 64 4.8 250 59 1.2 I 280
i I J
I 3 I 1300 I 822.90 i 0.070 1.02 I 1.02 ' 78 6'i I 5.0 ?'i11 ~ ~:~ ~ ~~g i
I 59
r {~I 1305 I 826.28 0.100 1.5 I 1.5 80 65 6 5 250 I 59
;Start I 1337 ! 826.28 0.060 I 0.9 I 0.9 67 66 4.5 250 60 11'.2. I 28
iHole 2-1 I 1342 I 828.47 0.060 0.9 ! 0.9 j 90 66 4.5 250 61 I 1.3 28H
I 2 I 1347 I 831. 23 I 0.070 1.1 I 1.1 i 75 r 68 ! 5.0 250 L 62 I 1.1 i 280
J j I 52 I 834.00 0.060 0.9 I 0.9 I 77 67 I 4.5 250 65 1.1 230.
, I
I 4 I 57 I 836.38 0.075 I 1.02 I 1.05 i 78 I 66 ! 5.0 250 he; IT? ')RO
, '
!Start I 1421 j 836.88 I ~:~;; I g:~ I O! I 70 I 1'11'1 L.. Q ?e;n 6~ 1 ~ ')Qf"\
IHole 3-1 I 1421 I 839.56 I I ! 73 67 4.5 250 65 I 1.0 280
I I ~:~1
i 2 i 1431 I 842.25 0.070 1.01 I I 77 hh L.. Q ?e;n he; 1 1 ?An
, 3 I 1436 I 845.28 0.080 1.18 I 1.20 I 82 67 5.5 250 65 1.0 280
i 4 I 1441 i 848.60 I 0.100 I 1.45 I 1.45 I 86 67 6.5 250 . 65 1.1 280 ,
I ! I r I I
!
Cor.;ii1~i1ts:
~CAP-37' (12/67)
t:I
,
......
-------
. .
, Part 10, p. 4 of 8
PARTICULATE FIELD DATA
VERY IMPORTANT - FILL IN.ALL BLANKS
-----,-
Plant
Read and record at the start of each
test point or, if single point
sampling, read and record every 5
rni nutes . '
Wood River Power Plant
Run No.
EDE-2 CONTINUED
SC;.I1P 1 ~ .Box No.
1047
1047
Location
East Duct Exhaust
~,eteT Bo~ No.
Dz:te
February 19, 1971
Probe Length
30'
Op2rator
N. A. Blessing
Pl~obe H2,il tevo Setti ng 130'
ftmbient Temp of
60
Bar. Press. IIHg
29.9
Assumed Moisture %
7.27
Hc~ter Box Setting, of
250
. Probe Tip Dia., In.
\ I
I P -, ~ Clock
! 0111 t.: I T i J:;~
(St:Jrt L 1540
i tIde 4-1 j 151.5
: 2! 1550 j
I 3 I 1555 !
i 4 I 1600 I
: S tart I 163L, !
i Hole 5-1 I 1639 _J
I 2 I 16Lf4 I
I 3 i l61f9 I
: 4! 1654 I
! I I
I I I
! i I
, I I
I I i
! ! I
.
Pitot Ori ii ~e l:IH I Dry Gas Temp.
, DI'y G~s i 1'1. H20 ---,,_jn.--li?O I of
!';2tei, CF bP Desired I Actuill i Inlet IOu'clet
I
8Lf8.fiO 0.085 1.30! 1.35 I 66 1'.6 0.0
RS1.80 i 0.080 1.25.1 1.25 1---1.0 I 67 6.0
8~(L.90 I 0.090 1.3:;=J 1.30 L-LCJ 66 6.0
858.20 10.100 1.50! 1.5 I 82 I 671 6.0
[.61.32 I 0.100 1.50 I 1.5 i 85 . 67 i 6.5
861.32 I 0.090 I 1.40 I 1.4 78 67 I 6.0
[;64.62 i 6.090 1.40! 1.45 73 67 6.0
868.00 10.105 1.60 I 1.6 76 67~.5
871.66 I 0.105 1.60 I 1.55 I 77 67 I 6.5
874.92 I 0.120 1.83 I 1.85 I 78 67 7.2
Hole 6 not 1tested duel to hig\> Wi.a.. 1 I I
I I. : -1 I I-
Ii. : I :
/
Ccr.:mCilts:
NCAP-37, (12/67)
t:::I
,
.....
~
PUin;:>
Va:ut;m
I i1. Hg
G~uge
Box.
Temp.
I of
17<;0
I? <;()
12')0
1250
~o
250
250
250
2?0
j250
J
L--L.
0.375
I~pinger St~ck St~ck \
TG:1p Pr2SS Tc;~:,p.
:: ~n~ Hg L~~
(,() 1 ':\ I ?9.0
6' 1 ':\ I 7RO
6~- . ..LJ__L2J~()
67 1.3 1270
67. 1.3' '260
68 11.3 1250
68 11. 3 J 250
69 T:"~i 250
69 11~4 250
I
I
I
-------
Part 10, p. 4 of 8
PlantWood River Power Plant
Run No.
WDE-2
locati en West Duct Exhaust
Oz;te
February 19, 1971
Op~iz.ter
C.Gonza1ez
\ Point I ~~~~k 11':~~~r:'~F
!Start I 1245 I 623.60
jHo1e 7-111 1250 i
I 101 1255 j
! 91 1300 I
~ ~i i;~~ ~
iStart J 1340--'
ITk)le 8-11\ 1345 I
t 101 1350 I
~ 9! 1355 i
i 8!1"400--'
I 71 1405 I
!Start I 1420 I
;Ho1e 9-11 1425 I
I 10 1430 i
r 9. 1435 I
Comments:
NCAP-37" (12/67)
t:1
I
.....
V1
Pi tot
in. H20
6p.
-
I 0.10
0.12
0.11
I 0.11
i 0.11
-
! 0.08
i 0.07
0.06
I 0.07
i 0.07
\--
0.07
0.07
0.07
PARTICULATE FIELD DATA
VERY IMPORTANT - FILL IN,ALL BLANKS
---;-
Read and record at the start of each
test point or, if single point
sampling, read and record every 5
minutes. .
Ambient Temp of
65
Reston
Bar. Press. "Hg
29.9
SC1.i1p 1 e'Box No.
"'Ct2T Sex No.
Probe Length
II
Assumed Moisture %
7.5
30'
Hc~ter Box Setting. of 250
130°
0.375
. P~obe Tip Cia.. In.
Probe H~uter Setting
, I plj;j)p
Orifice 6H Dry Gas Temp. Va~u~m Box Ir.:pinger Stuck St~ck
~~£1_J:i-,)O I of In. Hg Temp. T~;np' Press T.::;:p
D2sircd ~ .;ctu~l J in1et ! Outlet Ge:uge of of in. ;'-:J I °FI
- I - I - '- 25~0 29.98 I 285
1.20 1 70 I 68 2.0 250 70 29.98. I 285
1.50 '76 I 70 2.0 250 I 10 2~.98 I 285
! 1.30 \ 80 ! 741 2.0 250 70 29.98 I 285
j 1.40 i 84 I 74 2.0 250 I 70 I 29.93 ! 285
1.40 I 86 I 76 2.0 250 70 ,29.98 \ 285
\ - I - L - l-=- 2~ I 29.93 - 2R5 I
1.0 i 76 [76-! 2.0--250 T 70 1-29.98j 285 I
! 0.90 I 73 I 76 2.0 250 70 I 29.98 I 2\3s-j
I 0.75 80 I 76 . 2.0 250 70 2~.98 ! 282--1
I 0.90 I 78 I 74 L.1.:...0 1250 I 70 I 29.98 I 285 I
I 0.90 I 82 I 74 ~~-1250 70 I 29.98 i 2351
I - I - I - I - 250 70 29.98 I 285 . 1
I 0..90 I 76 74 115' 250. 70 29.98 I 285 !
I 0.90 I 78 I 75. I 1.5 250 70 29.1j3 I 20S ;
i 0.90 I 78 I 75 I 1.5. ~ 29.98 I 285 I
-
1.20;
1.50'
1.40
1.4d
1.40
-
1.0
0.90
I 0.75
I 0.90
0.90
-
I 0.90
I . 0.90
-------
Part 10, p. 4 of 8
Plant
Wood River Power Plant
Run No.
WDE-2 CONTINUED
Locatici1
West Duct Exhaust
Dc:te
February 19, 1971
Op~rator
C. Gonzalez
j
I
i I Cl ad
I Point j Tij:;~
! I I
i 8i 1440 I
I
i 71 14/+5 I
,
!Start I 15401
Ino1e W-1l1 I
! 101 I
: 91 !
I
, 81 '
I I
L 7! I
:5 tar t I 1630 I
,
;Hole 11-11.! I
I 10j I
I
L. 91 !
' 81
, I
j 71 t
,
: I i
I I I
. I
...
Dry G~s
Hete" CF
Cc;r:m~nts:
;XAP-37' (12/67)
t:I
I
......
0\
Pitot
in. H20
LlP
0.06
0.05
I
I
: -
i 0.06
I 0.07
! 0.08
~ ~:g~
I 0.07
I 0.08
I 0.05
I 0.06
I 0.05
I
PARTICULATE FIELD DATA
VERY IMPORTANT - FILL IN.ALL BLANKS
---.-
Read a~d record at the start of each
test point or, if single point
sampling, read and record every 5
mi nutes. .
Sz..ilp 1 ~ Box No.
Ambient Temp of
65
r-1<:teT Box No.
"
Bar. Press. "Hg
29.9
Reston
Probe Length
30'
7.5
130°
HCilter Box Setting, OF 250
Assumed Moisture %
. Probe Tip Cia., In.
Probe H2~ter Setting
r . I PUiirJ
I Orifice LlH Dry Gas Temp. Va:u~m Box
h in H"O I of Iil. Hg /Temp.
I D2sir2cr-j .~ctui}1 I Inlet ! Ou"c1et I G\::uge of
. 0.75 10.75 178 174 11.5 250
0.05 'I 0.65 I 78 I 74 I 1.5 250
-, I - ! - - - 250
0.15 I 0.75 ! 70 i 68 11.5 250
0.90; I 0.40 j 76 70 I 1.5 250
1.0 I 1.0 I "18 70 I 1.5 2jO
0.90 ~5 I 80 70 1.5 2'10
0.65 LM2-i 80 70 I 1.5 250
- I - I - - - 2.50
0.90 i 0.90 i 70 j 70 1.5 1250
1. 0 I 1. 0 I 70 I 66 I 1. 5 250
0.65 I 0.65 I 70 66 1.5 -.-1250
0.75 I 0.75 -' 68 64 1.5 250
'" 0.65 I 0.65 i 68 I 64 I 1. 5 I 250
I
I
I
l
I
llilpinger
T:.:::-np
o-
r
70
70
70
70
I 70
70
70
70
70
I 70
70
70
70
70
0.375
Sti:ck
Pr(;ss
Ii n. :-19
St~ck
T <:::1p .
0.-
r
29.98 i 285
29.98 285
29.93 I 285
29.98 I 285
29.98 ! 285
29.1J~ ! 285
?q qq 235 I
I 29.98 J~-
29.Q8 2~')
I 29.98 285
29.98 235
I 29.98 285
29.98 285
29.98 285
j
I
-------
Part 10, p. 4 of 8
Plant
. Wood River Power Plant.
~un No. EDE-3
location
East Duct Exhaust
D c:..~ e:
February 20, 1971
Op;:iator'
!
N. A. Blessing
Clock
Point i T1.::2
3tart ! 1347 I
~ole 1-1~ 1352 I
1q 1357 I
9, 1402 I
-~ 14071
~ 1412 I
Start J 1430 I
Hole 2-1lj 1435 I
1Q 1440 I
9; 14L.5 I
B 1450 /
,'1 14Lf5 I
Start I 1540 I
Hole 3-1~ 1545 I
1Q 1550 i
9. 155')
:cmm.:nts:
'!CA?-37' (12/67)
1::1.
I
I-'
....,
Pi tot
Dry Gas i~. H20
r';8i:(?i, CF bP
876.18 I 0.11
878.59 L-Q..10
8~81.35 I 0.10
885.2r-j. 0.12
888.78 I 0.15
892.98 I' 0.20 I
892.98 0.07
895.70 I 0.07
898.51 0.07
901.00 0.075 I
Y03.63 I 0.07
906.48 I 0.055
918.25 ! 0.07
921.13 0.08
924.00 0.05
926.60 0.07 I
PARTICULATE FIELD DATA
VERY IMPORTANT - FILL IN.ALL BLANKS
--- -
Read and record at the start of each
test point or, if single point
sampling, read and record every 5
minutes.
Sc:.i1p 1 e Box No.
1047
r-ieter Box No.
Probe length
30'
, .
Probe H2~ter Setting
Orifi ce bH II Dry Gas Temp.
. H 0 or
--=----.1~') ~ r
D2sir~d ~j P..ctu21l J inlet ! Outlet
1.65 . - I 43 44
i:~~ .j i:~~ 1 ~: I ~~
1~.8,0 ! 1.80 : 65 j 48
2.is I 2.20 I 67 L-2o
3.0 I 3.0 I 73 50
1. 05 I 1.1 I 48 50
1.05 I 1.1 1 53 50
1.05 I 1.4 I 59 50
1.13 I 1.15 i 60 I 50
1.05 I 1.01 r 60 I so
0.8 I 0.84 I 60 j 50
1.1 I 1.1 ~ 56 I 50
1.22 I 1.27 I 62 50
0.75 I 0.75 I 64 50
1. 05 I 1.1 I 65 I 50
I
Ambient Temp of 45
Bar. Press. "Hg 29.9
Assumed Moisture % 5.35.
!iNter Box Setting, of 250
Pi~obc Ti P Di a .. I~. 0.375
PUjj1;:> Box I Impinger
Va::uum S"~~J, I S"~ck
Iwu,,-'" L..c.,
In. Hg Temp. T<:::r.p. Press I TE~:;P
G~uge of 0- ii1. Hg of I
r
6.0 250 46 1.5 1280 I
7.0 I 250 48 1.0 1280
I
6.5 250 95 I 1.0 i 280 I
1
I 6.5 250 I 70 1.1 ! 280
8.0 250 I 65 1.0 ~
15.0 250 60 1.0 1280
I 250 49 I 1.0. 280
~9
! 4.0 250 48 I 1.1 128Q-
4.9 250 48 1.2 280
4.5 I 250 I 46 I 1.1 280
I 4.8 i 250 : 45 I 1.0 280
4.0 250 45 I 1.0 1230
~ 5.0 250 50 I 1.0 1280
5.0 250 50 1.1 280. I
3.5 250 50 1.0 1280 :
I 3.0. 250 50 1.2 1280 I
-------
Part 10, p. 4 of 8
PARTICULATE FIELD DATA
VERY IMPORTANT - FILL IN.ALL BLANKS
---.-
Read an9 record at the start of each
test point or, if single point
sampling, read and record every 5
minutes.
Pl2.nt
Wood River Power Plant
Run No. EDE-3 CONTINUED
S~ilpl~ Box No.
1047
Location East Duct Exhaust
~tetcr Box No.
Dc:te
February 20, 1971
Probe Length
30'
N.A. Blessing
Op2i~ato:"
Probe H2~te~ Setting
Pitot Orifice AH I Dry G~: Temp.
in. H20 L-~!]- H')O I r
liP~- D2sircd ~ t\ctu~l ; inlet ! Out12t
I O'~H 1.05 1.10 I 66 I 50
I 0.05 I 0.7:5 0.751 62 I 50
I g:g~ I ~:g ~:i~ i ~g i ;~
I 0.06 1 0.90 0.93 I 64 I 58
0.06 10..90 0.94 I 66 I 57
0.055 I 0.84 0.87 j 65 [ 58
I 0.06 _0.90 0.92 j 671 57
I 0.10 I 1. 55 1. 55 I 54 .. 57
I 1.130 I 2.0 2.0 i 61 I 56
I 0.07 1.05 1.07-1 66 I 57
0.075 1.15 1.10 67 I 57
I 0.08 1.25 1.25~ 70 58
0.07 1.05 1.05 71 57
I
I
i I Clock
I Poi i1 tiT i r::.~
I 31 1600
i 71 160S
i Start I 1618
! Hole 4-1~ 167.3
r 19 1628
! ':J I 1633
8J1638
~tart 71 i~;~
I Hole 5-11 1701
! 1\1} 1706
I ~fI 1711
L
. 81 1716
7 I 1721
,
Ccr.:ir.cnts:
tKAP-37- (12/67)
o
I
....
00
DiA'y G~s
I }12t2iA, CF
I 929.42
I S31.93
j 931.93
I 934.75
I 937.20
939.96
%2.50
945.11
945.11
948.57
951.42
954.22
952.23
960.19
;
Ambient Temp of
45
Bar. Press. "Hg
29.9
Assumed r~oisture %
5.35
Hc~ter Box Setting, of
250
. P~obe Tip Dia., In.
0.375
S"~c,,'ls"'~c!'
LV. f.. l.u.'
Prcss IT:::;::>
;:1 'j" Go=J0r- '
lI.i~! r
I 1.0 i "'1
') .! I
PUii1;J I
I
Va::uum IBOX
. I~. Hg Tc~p.
i Ge:uge I OF
I==t0 I 250 I
4.U 250
. 5.0 250
I 3.5 250 I
i 4.5 [I?o I
R.5 I 250 I
4.5 250 I
I 4.8 250
6.0 250
. 8.0 250 I
5.0 250
5.0 250
5~5 250
5.0 250
Ir.1pinger
Tcnp'
o-
r
5
50
50
55
56
_56
50
60
60
60
60
60
-------
Part 10, p. 4 of 8
PARTICULATE fIELD DATA
VERY IMPORTANT - FILL IN.ALL BLANKS
---.-
: Plant
-
Wood River Power Plant
Read and record at the start of each
test point or, if single point. .
sampling, read and ,record every 5
minutes.
Run No.
WDE-3
Sz..l1pl~ Box No.
Reston
Location
West Du~t Exhaust
f4etcr Box No. .
Reston
Dc:te
February 20, 1971
Probe Lengih
10'
Op~rator .
Probe H2atcr Setting
1300
C. Gonzalez
I
I
I
~
I
I
r
i
I
t
I
~
I
I
I
I
. i
I
: L
Ambient Te;np of
44
Bar. Press. "Hg
29.9
9.75
Assumed Moi$ture %
!!c~te; Box Setting, of
250
P;~obc Tip Dia.. In. 0.375
I I I
I l I
~1 I
I . S"'~"'k' I c"'~ck
PU:;1P
Pitot Orifice ~H Dry Gus Temp. Va:uL.:m Box Ir.1pinger ~"''- oJl.t.
Clock Diy Gas in. H20 _~n H,;,O 0,... In. Hg T~~p. Tc::p Prcss I T~::~p
I r
Point Tii::~ . r'~etei, CF llP D~sircd i Actuill - 1 + IOutlet G.:::uge L of 0""
I I in ,c.. r ; n. :-1g 1 0 F
I
Start 1335 I 700.45 0.12 1.60 1.60 I 44 42 2.0 I 250 50 I 29.98 I 280
Hole 7-1 i 1340 I 0.11 1.50 I 1.50 1 48 I 42 2.0 I 250 50 29.98 . I 280
2 1345 ! 0.11 1.50 1.50 49 I 42 2.0 250 50 29.98 I 280
I 31 1350 I I 0.11 1.50 I 1.50 . 52 I 42 I 2.0 250 50 r 29.98 I 280
I
i 41 1355 I I 0.10 1.40 1.40 i 52 40 2.0 I 250 I 50 29.98 I 280
!start I
I 1425 I 0.06 0.75 0.75 42 40 2.0 250 I 50. I 29.98 I 280 I
I
I Hole 8-1 I .1430 I 0.06 0.75 0.75 I 48 I 40 ~ Z5U I 50 " --z9. S8 28U
\ .
1====i=!.----.!.435 I 0.05 . 0.65 0.65 48 40 1.5 250 I 50 I 29.98 280
3 I 1440 I I 0.07 0.90 I 0.90 ! 48 42 I 1.5 250 50 29.98 2'80-:-
I I 1445 I 0.06 0.75 I 0.75 i 48 I 42 1.5 250 50 I 29.98 280
! Start I 1505 I 0.04 0.55 I 0.55 I 44 I 40 I 1.5 250 50 I 29.98 i=i=:j
I
I Hole 9-11 1510 0.05 0.65 I 0.65 I 50 , 42 1.5 250 50 I 29.98 280
i 2 I 1515 0.05 0.65 I 0.65 I 50 42. 1.5 250 50 29.98 280
i 3 1520 I 0.05 0.65 I 0,65 I 50 42 1.5 250 50 29.98 280 I
I
I 41 1525 i 0.05 I 0.65 I 0.65 50 42 ~~- 250 i 50 I 29.98 280 :
I i I '
I I I !
I I ! i I .
I '
1 I
I .
-------
Part 10, p. 4 of 8
Pl 0.75 I 54 56
I 0.06 I 0.75 I 54 46 50
I 0.05 ! 0.65 i 46 46 50
I
I 0.05 I 0.65 I 50 46 s'n
1- I
I I. j '"
I i 250 50
I I
21
31
41
i
I
1748
1753
1758
1802
757.46
CCr.::ni?iltS:
;:CAP-37' (12/67)
1:1
I
I\J
-------
RESOURCES RESEARCH. INC,
Personnel
Eutered
. Checked
Plant Conditions, etc~
S02
Plant
Wood River Power Plant, East Alton, Illinois
Date
2/17 - 2/20
Sample Location
EDE - WDE
Meter # GAS METER CONDITIONS PuTrID IF
Sample Cu.Ft.. Cu.Ft.(Vm) Elaps.. (RID) (;.460=Tm) (Ru) Thimble
Time Number Read1n~ Difference Min. C.F.M. Tenn> of VacuU'Dl"lli!: Numbe r
2/17 1600 EDE-1 501. 3 54 6.0
1622 503.3 2.0 22 - 54 6.0
2/17 1645 WDE-1 506.4 60 7.0
1707 508.4 2.0 22 60 7.0
2/18 1730 WDE-2 511.2 64 6.5
1752 513.9 2.7 22 64 6.5
2/20, 920 EDE-3 516.0 37 5.0
942 518.0 2.0 22 37 5.0
2/20 1000 WDE-3 520.6 41 4.0
1022 522.6 2.0 22 41 4.0
-
D-21
-------
. '\;
, .I-e
. : . '
:' .:1
i '
I
i
.,
.. ;...------
. i
,
. !
:'
,.
, :
,
. .
. I
,,".
~ i'
. I.
I ,
. f\.' 1 ' '."
. ..
, ..
NATIO:LA..L CE:rrER FC~ A:!:7\ ?0LLtJ":'ION cm;,~:~oI.'
,
,
SOuTI~::; ,;~:;r_\::-:~ ~';::::'
. ..... ~ '.
No
x
So.."71l?ling r.~-t::.. c..'=: C~.lct:.lJ.ti 0::3
Date . Feb. 17, 1971
-~~B Point Location East Duct
Exhaust
Run No. EDE-1
TiLle
1000
I 1010
I
I 2.125
Flask No.
8
Flask Vol.,
*
VI' a (liters)
2.141
Initial Flas~ Vacu~,
P ("HrT. C'l'al"'e)
fb IJ to u
27.5
27.5
----- 0.5 L O.~
I
I 45
~ 1.68
Nox as N02' ppm (3 std. cond.dl')rCff'!417.0 1440.0
I
bJ 397.0
C I
Nox as N02' ppm @ stack cond., I'h 395.0 1417.0
J 1310.0 i 1390.0 ]
A. No as N02' ppm ~ std. condo (drJ)
x '
Final Flask Vacu~~,
Pfc ("Hg. gase)
. 0
Flask Te~p. Tfd ( F)
45
Weight of N02 (from Lab),
Wfe (mg.)
Nox a~ N02' p~~ @ std. condo dry
. ,~ 12~ C02 C02' Cfg
Nox as N02' lbs/hr, Cf
. 29~63 x W~ x (Tf'd + 460) = C
Ie tf
V.pa x (?_~ -?~ )
.. .o...c
B. Nox as ~{o2' pp:il @ 12j~ C02
( D:-f)
.. Cft x 12 = Crg
Vba
1
I~
: I
I
I
I
I
I
I
LI
I
I
,
'I
I
I
f
I
I
.A.~.&. '" -') &". - - - -.,
!
.,
,
I
I
I
I
I
I
l
]
D-22
. -., " ".. '" .,t/ll ,.. ',~ 'f""" :,',... -:..:.\
I
I
I
!
I
I
i
I
I
i'
-~\~
-------
~ .:1
, I .
I
. , .
I
j
I
'.
I
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. ,
, "
. .
. !
. .
. i
,
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.
;
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. ,
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;.!.'.
.!
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f.
NATION!.LCZ~l'ER FOR 1'.!i1 PO~Lu'?ION COr;'l':~OL'
i
I .
,
,
SOURC~ ~~~r...I:~:J ill;:?
.
, ,
. .. , .
~~ling D.~t~ ~r~ C~lc~~tio~3
"'
No
x
:.
Date February 17, 1971
----
'--Sampling Point Location West Duct
Exhaust
Run No.
WDE -1
TiL1e
I 1030
I 13
2.131 I
27.5 I
1020
Flask No~
4
Flask Vol.,
*
v'ra (liters) .
2.146
Initial Flask Vacu~,
Pfb ("HG. gage)
27.5
Final Flask Vncu~~,
. P fc ("Hg. gage)
Flask Temp. Tfd (OF)
0.5
0.5'
I
I 45
~ 1.90
Nox as N02' ppm @ std. cond.d:rycffl~96.'O j 493.
Nox a~ N02' ppm @ std. cond. dry I. I
. ~ l2~ . C02 C02' Cfg - ~ -'t14.9
NOx as .No2' ppm @ stack cond., Cfh ~-464.0 I
Nox as N02' lbs/hr, C£ ' 420.0 1410.0
A. Nox as N02' ppm ~ std., cond.. (dry)
45
LI
I
I
. I
LI
./
Weight of N02'(fr~~ Lab),
Wre (mg.)
. .. 29.63 x t.,~ x (Trd + 460) '" e
Ie 1'1'
Vra ?' (?:i:"b - Pre) ,
B. NOx as N02' pp:il @ l~ C02
.. Cft x 12 ... erg
Vba
(D:7)
. ,
_..... .0- 0
. ..
.,
o :t.
j:'~.r~ '), p. .l OL c.:
j'O
.. .1._.,.1....
i
I
I
i
I
I
I i
I !
:---1
I I
I I
I I
I I
I i
;
r
i
I
I
r
.
~
\
~
,
.
1
. i
. "
D-23
I
i
.~~~'5
-------
.7:
. -.
. '.
NATIO~t\L Cr::;'l'E~ FO~ A!l{ POLLlJ?ION Cm;<:':~OL'
: .:1
i <
j.
,
,
SbURC~ ':':S:]-':::~ 0:'~~
I
, .
i
. I
:.
. I
I
...."
No
x
&:t.:1I~ling D.),:t~" ;;:.r":: C:.lct:.btio;:3
Date February 18, 1971
. -~~8 Point Location East Duct
Exhaust
T:we
"
Flask No.
. I
*
Vra (liters)
. I
Flzsk Vol.,
Initial Flask Vacu~,
Prb ("Hg. gage)
Final Flask Vo.CUQ~,
Pre ("He;. gage)
Flask Temp. Tfd (oF)
Run No.
EDE-2
LI
I
I
,
LI
I .
U
. i
Weight of N02 (fro~ Lab),
Wfe (mg.)
, ,
std. cond.dry C I . I
ff; .
, .
LJ' ,-- '
',,:"'. --.
. I
I
\
Nox as N02' pp~ ~
Nox a~ N02' pp~ ~ std. _c~nd. dry
~ l2~ CD2 C02' Cr~
NOx as N02' pp~ @ stack cond., Crh
NOx as N02' lbs/br, Cf .
A.
NOX as N02' ppm ~ std. condo (dry)
"
, c: 29.63 x 'olre ?C (Trd + 460) = Coff
Via x (? ~ - P". )
:tD ",C
B.
No as No pp~ G lc~ CO
X 2'''' .,. 2
IS Crr x 12 = Cfg
Vba
(D:,y)
.
, i
,
..
. .
.
. I:
i I
i I
I \
I I
, ,
I I
i~
I
I
I
1
NOT'RUN DUE TO PLANT CHANGING
TO HIGH LOAD.APPROVED BY
JERRY ROM.
D-24
''7 ."
': '.V' \_...
-------
. ..
. -a
. .
. t .
r . ;~,
!
.
. ,
'.
.,
. ,
I
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. ,
. .
; i
;
.' '
. . .
. .
,.j', '
. j
. t.
:1 :
: .1 ~
..', "
.'...". .
NATION.'.r, CE'rl'Zn FOR JI.ra P()LLt.i'~ION cOr;:':~OI.'
,
,
. ...,'
so"tmc::: ,;~:;r....\::~:.J \fl::C~
No
X
s"'1.1i1pli ng 1;.~~.::.. ~,..:: C::l~\;~.tiol'~3
Date Februa~ 18. lq71
------
--Sompl1ns Point Location West Duct
Exhaust
TiLle
Flask No.
Flask Vol.,
*
Vra (liters)
Initial Flas~ Vacu~,
Prb ("Hg. gage)
Final Flask VacuQ~, .
. Pre ("HS. gage)
Flask Te~p. Trd (OF)
NOx as N02' pp~ @ std.
""
. v",'
l2t' C02 C02' CfP;
Run No. WDE-2
1800 I 1810 I
1 I 8 i I
2.1251 2.141 I I
27.5 I
27.5 I
I
0.5 I 0.5
58 I 58
1.53 1. 78
I
I
I
LJ
NOx as N02' lbs/br, Cr ' 1210.0 1390.0
A. Nox as N02' ppm ~ std. condo (dry)
, . 29.63 x Wfe x (Tfd + 460) = Crr
via x (?:i~D - Prc)
Weight of N02 (rro~ Lab),
Wre (mg.)
NOx as N02' ppm @ std. cond.dryCfff09.0' 1472.0
cond. dry 1....,.,,, I
~4-D4.q
NOx as.No2' ppm @ s~ack cond., Cfh ~75.0 1433.0
B.
NOx as N02' pp:;J. @ lc.~ C02
(D:'Y )
..
crf x 12 = Crg
Voa.
",
. ,
I'
I
I
l
i
!
I
I
I
I
I
I
L_i
. .
D-25
..--.
.- ,"
..
-------
. ..
..; ..: . -a
'\ -: .:1
I .
" j
NATIONAL cr:::-l'ER FOR A!li POLLtli'ION Cori':':~OL'
i
"
o
,
,
SOUR~~ ~:::~t_'!~:: u:,~r~
. ...,' '. .
:.
, i.
I
J
,
No
X
~~l~ng D~t~ cr~ C~lc~1J,t1o~3
, ,
Date February 20, 1971
.-~s Point Location East Duct
Exhaust
. I
Flask Vol.,
*
Vfa (liters)
0900 I
I 1 I
12.125 I
Run No. EDE-3
0910 I I '
I
i I I
8
2.141 \' , I I
27.0 I I
1
Time
Flask No.
. \
Initial Flask Vacu~,
Pfb ("Hg. gage)
27.0
. I
i
I 0.5 I 0.5
140 140 I .
_~1.91. I
Nox as N02' ppm @ std. cond.dryC I 'I LI
ffr75.0 500.0
Nox as N02' pp:n @ std. cond. dry I I
G 12% C02 C02' Cfg' - ~ .448.0
NOx asNo2' ppm ~ stack cond., C I
. fh ~57.0 481.0
Final Flask VQCU~~, .
PfC ("Hg. gage)
, ,
° .
Flask Te~p. Tfd ( F)
I
i
I
I
I
I
I
I
, ,
. i
Weight of N02 (from Lab),
Wre (mg.)
, ;
,
I
, :
,
No as No Ths/hr, Cr'
x 2'
A. NOx as N02' ppm @ std.
cond..
1,540.
(dry)
1,620.0
.. . .
.. '29.63 x ~vfe x (Tfd + 460) .. Cff
Vf x (?_--- - P ~ )
a 4'" 4C
, .
B.
NOx as N02' pp~ @ 12-~ C02 (D.:-y)
.. Cft x 1.2 :0 Crg
Vba
.. ,
"! ,: ~.
, ,
, ,
" ,
, '
"
.. .
,..,
I
'.
, .,
, .
D-26
"
........., ~
a"" .'. .
. .'.' .'
. ,
.,
-------
.. ,:'. .-.
. , . "'.
: . =,
i '
j
NA'rIO~p.L CS!'l'E~ FOR AI] P0LLu'?ION cor;':':~OL'
,
,
SO~JBC:;; ';'S.~;...I:~:: ~:'~':'
t '
,I
-... I
. I,
I
No
x
5.!1.."11plin:; !;.1.;::'~. ;;;.,~ C~,"!.~~l.:J.t1 <:,.:;3
. I
:.
Date February 20, 1971
...;.---
-~omplin8 Point Location West Duct
~xhaust
.Run No.
WDE -3
!
I
I
1
1
I
I
I
LI
I I
I
I
I
L
I
I
.
I
I
" I
i
l
I I
I I
/'
Time I 8: 30
" Flask No. I 4
,* (liters) I 2.146 t
' . Flask Vol., V1'a
I I
. I
'. Initial Flas~ Vecu~,
Pfb ("He. ea:;e) 127.0
Final Flask Vucu~~,
Pfe ("Hg. gage) 0.5
8:40 I
-'
I
13 i
2.1311
27.0 I
0.5
, ,
Weight of N02 (1'ro~ Lab),
Wfe (mg.),
I
" I
i 1.70 J
Nox as N02' PP,r.l@std.eond.dryCI, I
. 1'1'i 441.0
I ,
No as !\02' pp:n @ s'td. cond. dry r
x G 12~ C0 CO C . -' I 381.Q
(J 2' 2' 1'15, '
38
38
, ,
Flask Temp. Tfd (oF)
1.71
I
I
I
L!
.1
; i
,
446.0
1.185.0
Nox as'N02' ppn@stackcond.,cl
fh 403.0 j 408.0
. j 1220.0 \1230.0 I
A. NOx as N02' ppm @ std. eor~. (dry)
NOx a.s N02' lbs/br, Cf .
, '
.
. ... 29.63 x '-lie x (Tfd + 460) = Cff
Via x (Pro - ? ic)
B.
NOx as N02' pp:u @ 12% C02 (~.r)
.. Cfr x 12 = Crg
Vba '
" ~ . ;
I.
I
"
D-27
-
. .
"
---\ ...
.7'" . ~:
'. ~'.
-------
,
',.
Part 10, p. 7 of 8
ORSAT FIELD DATA
location
Wood River Power Plant
Comments:
Date
Feb. 18, 1971
Time
Operator
1110-1649
N. A. Blessing
- ---,--.- --
--- - -.a
Test (C02) (02) (CO)
Reading 1 Reading 2 Reading 3
. .
EDE~l A 1:3.4 ~ 5.6 0.0
B . 13.2 5.7 0.0
I
,
,
I
! -
NCAP-31 (12/G7)
D-28
-------
Part 10, p. 7 of 8
..
ORSAT FIELD DATA
Location
Wood River Power Plant
Comments:
Date
~ebruary 18, 1971.
Time
1110-1650
Operator
..-.-- --
Test (C02) (02) (CO)
Reading 1 Reading 2 Reading 3
-
WDE.-l A 14.3 . 4.9 0.0
B 14.3 4.9 0.0
-" . - 7 --"
- - I
--
.
I .
I
,
NCAP-31 (12/G7)
-------
Part 10, p. 7 of 8
ORSAT FIELD DATA
location Wood River Power Plant
Comments:
Date
February 19, 1971
Time
1110-1649
Operator
N. A. Blessing
_._-,- - ~-
Test (C02) (02) (CO)
Reading 1 Reading 2 Reading 3
EDE-2 A 13.6 5.4 0.0
-
B 13.7 5.6 0".0
- .-. . :'" - - -:-" ---
-" I
,
.
l\CAP-31 (12/67)
-------
Part 10, p. 7 of 8
ORSAT FIELD DATA
Location Wood River Power Plant Comments:
Date February 19, 1971
Time 1245 -1655
Opel~ator C. Gonzalez
-.--- -" .-
Test (C02) (°2) (CO)
Reading 1 Reading 2 Reading 3
WDE.,,2 A 14.1 ;, 5.1 0.0
B 14.0 5.2 . 0.0
-
- ... ,-
--. I
- -
,
NCAP-31 (12/G7)
-------
Part 10, p. 7 of 8
ORSAT FIELD DATA
Location
Wood River Power Plant
Comments:
Date
February 20, 1970
Time
1347-1721
Op~rator N. A. Blessing
~. --- -_. --.
Test (C02) (02) (CO)
Reading 1 Reading 2 Reading 3
EDE~3 A 13.3 - 5.8 0.0
B 13.4 5.7 0.0
- -
- .. . - .. -_.
- I
- -
,
.
',-. :>;.7
NCAP-31 (12/67)
-------
Part 10, p. 7 of 8
ORSAT FIELD DATA
Location Wood River Power Plant
Comments:
Date
~ebruary 20, 1971
Time
1335 -1803
Operator
Gonzalez
..--- --- --
Test (C02) (02) (CO)
Reading 1 Reading 2 Reading 3
WDE-3 . A 13.8 . 5.4 0.0
B 14.0 5.2 0.0'
- -
- .. - - .. --. I
. I
..
I ,
i
: .
.~. 'l./
KCAP-31 (12/0'1)
-------
RESOURCES RESEARCH, INC,
Personnel
Schroeder
PAGE 1 01" 2
Entered
Checked
\.
Plant Conditions~ etc~
ASME TEST
Plant
East Alton, Ill. Power Plant
Date
2-19-71
Sample Location
East Duct
Test In
Sheet H
2
Meter # GAS METER CONDITIONS Pumn If
S amp ile Cu.Ft. Cu.Ft.(Vm) E1aps~ (Rm) (+460=Tm) (Bu) Thimble
Time Number Readin<> Difference Min. C.F.M. Temn of Vacuum"HQ: IMP Number
1300 82.92 63 3.0 65 Al
116
1305 86.24 3.32 5 .66 70 3.0 70
1310 89.40 3.16 5 .62 71 2.4 71
1315 92.13 2.73 5 .55 71 2.4 71
1320 94.85 2.72 5 .54 71 2.2 71
1325 97.56 2.71 5 .54 71 2.2 71
1330 100.32 2.76 5 .56 69 2.2 70
1335 03.12 2.80 5 .56 70 2.2 69
1340 05.84 2.72 5 .54 69 2.2 71
1345 08.40 2.56 5 .52 68 2.8 69
1350 11.50 3.10 5 .62 68 3.0 69
1355 15.10 3.60 5 .72 70 3.4 70
1400 18.50 3.40 5 .68 71 3.0 72
1405 22.18 3.68 5 .74 70 3.4 70
1410 26.70 4.52 5 .90 68 3.2 68
1415 30.15 3.45 5 .69 67 3.2 65
14?0 ~.4? 2.27 5 .46 67 3.0 67
Stack/Duct Measurement
Stack Diameter. inches
Stack Area., Ft2, (A)
Final Gas Temp 300
Starting Gas Temp 300
24' x 24'
Estimated Mc-
.94
Actual - .99
.635
.668
3/8
3
4
5
(D) _?712-,.___- Estimated Rm(Corrected)
576 Calculated Rro(Corrected)
og
+-
Sample Nozzle Dia~~In. (d)
oR % Moisttre o'f Gas 4.91
Avg,Gas Velocity.fpm(Vsx60)
Vs=(2.9 xFs) xJHxff
or
2.46 x .278 x 27.6 =
°F+460=Ts
760
Barometric Pressure,"Hg,(Pb) 29.9
Stai::k Static Pressure, In,~ 0
Condensate,ml (Vw) (+24)
Flue Gas Volume, as is (Vo) 653,184
Flue Gas Volume. dry, std.
1134 . 0
18.9
431,560
CFM
CF'M
Type Pi tot: Standard Type S-1L--
PITOT READINC'p- (1250 A.M. P.M.)
In. from side n, (In. H2~ ..rH
Hole 1 Hole 2 Hole 3
1 .07 .265 1 .07 .265 1 .06 .245
2 .06 .245 2 .06 .265 2 .06 .245
3 .06 .245 3 .06 .245 3 .06 .245
4 .06 .245 4 .06 .245 4 .06 .245
Hole 4
1 .08 .283
2 .08 .283
3 .085 .292
4 .08 .283
Hole 5
1 .08 .283
2 .08 .283
3 .08 .283
4 .085.292
Hole 6
1 .11 .332
2 .12.346
3 .14 .374
4 .13 .361
------~~--
-------
RESOURCES RESEARCH, INC,
Personnel
EnteTeCI
Checked
Plant Conditions~ etc~
ASME TEST
Plant
Date
Sample Location
East Duct Test # 1
CONTINUED
6
Meter # GAS METER CONDITIONS Pumn If
Sample Cu.Ft. Cu.Ft.(Vm) E1aps~ (Rm) (+460=Tm) (Ita) ThimblE
Time Number Reading Difference Min. C.F.M. Temp of Vacuum"Hs! IMP Number
1515 136.24 3.82 5 . 76 63 3.6 63
1520 140.10 3.86 5 .78 64 3.8 64
1525 144.52 4.42 5 .88 65 4.5 65
1530 148.75 4.23 5 .84 65 4.1 66
1535 152.00 3.25 5 .65 67 2.4 67
1540 154.75 2.75 5 .56 67 2.2 67
1545 157.40 2.65 5 .54 62 2.2 62
1550 160.21 2.81 5 .56 62 2.2 62
77 .29 77.29 120 60 2.9 67
,
Shee t If2
1
Stack/Duct Measurement
Stack Diameter~ inches (D)
Stack Area.. Ft2, (A)
Estimated Mc-
Estimated P~(Corrected)
Calculated Rm(Corrected)
Sample Nozzle Dia...ln. (d)
oR '7. Moisttre of Gas
Actual -
Final Gas Temp or
S:tarting Gas Temp 0F+460=Ts
Barometric Pressure. "Hg, (Ph)
Stack Static Pressure, In,12'O
Condensate.ml (V\J)
Flue Gas Volume.as is (Vo)
Flue Gas Volume, dry, std.
+-
Avg,Gas Velocity,fpm(Vsx60)
Vs=(2.9 x Fs) x.JH x {T
or
2.46
CFM
CFM
Type Pitot: Standard
PITOT READINGS (
In. from side H, (In. H2!D.-
Type S-
A.M. P.M.)
..fH
---._--
-------
RESOURCES RESEARCH, INC,
Personnel
Schroeder
EnteTed
Checked
Plant Conditions~ etc~
ASME TEST
Plant East Alton, Ill.
Power Plant
Date
2-20-71
Sample Location
West Duct
Test 1#2
Sheet If!
7
Meter 11 GAS METER CONDITIONS Pumn 1#
Sample Cu.Ft. Cu.Ft.(Vm) Elaps~ (Rm) (+460=Tm) (Rn) Thimble
- Time Number Readin2: Difference Min. C.F.H. T emn 0 F Vacuum"H!! IMP Number
1415 60.70 40 2.4 41 Al 93
-
1420 63.58 2.88 5 .58 41 2.4 41
1425 65.98 2.40 5 .48 41 2.0 41
1430 68.51 2.53 5 .51 41 2.2 41
1435 71.32 2.81 5 .56 41 2.4 41
1440 73.95 2.63 5 .53 41 2.2 41
1445 76.68 2.73 5 .55 41 2.4 41
1450 79.14 2.46 5 .50 41 2.2 41
1455 81. 90 2.76 5 .56 41 2.4 41
1520 85.82 3.92 5 .78 41 3.0 41
1525 89.95 4.13 5 .84 41 4.0 41
1530 93.62 3.67 5 .73 41 3.4 41
1535 97.57 3.95 5 .80 41 3.8 41
-
1625 100.65 3.08 5 .62 42 2.8 42
1630 103.25 2.60 5 .52 41 2.2 41
1635 106.18 2.93 5 .59 41 2.7 41
1640 108.78 2.60 5 .52 41 2.6 41
I
Stack/Duct Measurement
Stack Diameterb inches
Stack Area.. Ft2, (A)
Final Gas Temp 300
Starting Gas Temp 280
24' x 24'
Estimated Mc-
.98
Actual -
12
11
8
(D)
576
576
Estimated Rm(Corrected)
Calculated Rm(Corrected)
Sample Nozzle Dia~.In. (d)
oR % Moistu:e o.f Gas
'?
°F+460=Ts
3/8
740
Barometric Pressure,"Hgb(Pb)
Stack Ststic Pressure, In'120
Condensatebml (Vw)
Flue Gas Volumebas is (Vo)
Flue Gas Volume, dry, std.
29.9
+-
Avg.Gas Velocity,fpm(Vsx60)1002.0
Vs=(2.9 x F s) x Jif x {T 2 .46x. 250x27. 2=16.7
or
2.46
+ 62
CFM
CFH
Type PI tot: Standard Type S--K-
PIT~r READINGS ( 11 A.M. P.M.)
In. from side H, (In. H2~ - vii
Hole 7 Hole 8 Hole 9
1 .10 .316 1 .06 .245 1 .05
2 .13 .361 2 .05 .224 2 .06
3 .11 .332 3 .065 .255 3 .05
4 .12 .346 4 .06 .245 4 .05
Hole 10 Hole 11 Hole 12
.224 1 .04 .200 1 .06 .245 1 .06 .245
.245 2 .05 .224 2 .06 .245 2 .04 .200
.224 3 .05 .224 3 .05 .244 3 .05 .224
.224 4 .06 .245 4 .06 .245 4 .06 .245
--
------~'~-'-'
---'
-------
RESOURCES RESEARCH, INC,
Personnel
Schroeder
EnteTed
Checked
Plant Conditions~ etc~
ASME TEST
Plant
East Alton, Ill. Power Plant
Date
2/20/71
Sample Location
West Duct Test #2
CONTINUED
Sheet #2
9
Meter I GAS METER CONDITIONS Pumn If.
Sample Cu.Ft. Cu. Ft. (Vm) Elaps~ (Rm) (~60=Tm) (Rn) Thimble
Time Number Readinl! Difference Min. C.F.M. Temt> of Vacuum"H2: Number
1640 111. 40 2.62 5 .52 39 2.4 39
1645 113 . 94 2.54 5 .52 39 2.6 39
116.55 2.61 5 .52 39 2.6 39
ll~ .Llj.- L.tJ~ J .:>q. j~ ./:.0 J;1
121. 60 2.36 5 .48 39 2.0 39
124.40 2.80 5 .56 40 2.6 40
126.95 2.55 5 .52 40 2.4 40
66.25 66.25 115 .58 41 2.6 41
-
10
Stack/Duct Measurement
Stack Diameter. inches (D)
Stack Area., Ft2, (A)
Final Gas Temp or
Starting Gas Temp 0F+460=Ts
Barometric Pressure,"Hg,(Pb)
Sl:3ck Static Pressure, In,lIz0
Condensate.ml (Vw)
Flue Gas Volume.as .1s (Vo)
Flue Gas Volume, dry, std.
Estimated Mc-
Estimated Rm(Corrected)
Calculated Rm(Corrected)
Actual -
Sample Nozzle Dia~~In.(d)
oR % Moisttre of Gas
+-
Avg.Gas Velocity,fpm(Vsx60)
Vs=(2.9 xFs) xJHx.JT
or
2.46
Type Pitot: Standard
PITOT READINGS (
In. from side .!!...-l1!!.!..ti2~
CFM
CFM
Type S-
A.M. P.M.)
Vii
---.-
6_.._.._--
-------
APPENDIX E
1.
STANDARD SAMPLING PROCEDURES
2.
-------
APPENDIX E-1
STANDARD SAMPLING PROCEDURES
PARTICULATE SAMPLING
With an unstable plant operation a trial run is often conducted.
If
the trial turns out to be satisfactory it may be considered a part of the
final testing.
Preliminary data is obtained for gas velocity, temperature,
moisture content and other variables which might affect the isokinetic
sampling rate.
Each sample port traverse is divided into a number of
equal areas for each location.
Each test run is designed to obtain simu1-
taneous. samples at each location, for such a period of time that plant
.
operation will be representative, and that sufficient material will have
been obtained for accurate analysis.
Particulate samples are obtained using the equipment and test
procedures as stipulated in "Sample Collection Procedures," published
by OAP.
The sampling train is basically the same as that designed
by the Control Development Program of OAP (formerly the Air Pollution
Control Office), "Gas Stack Sampling Improved and Simplified with
New Equipment," and described in PaperNo. 67-119, presented at the
Air Pollution Control Association meeting at Cleveland, Ohio, in June,
1967.
The above sample equipment is referred to in this report as the
EPA train.
It is essentially the same as that recently described in
Federal Register, Volume 36, Number 159, August 17, 1971, Part II as
Test Method 5.
Its operation, briefly, is as follows:
-------
Sample gases are drawn into an all-glass sampling train through
a button-hook stainless steel nozzle with the proper diameter for
isokinetic sampling.
A pyrex glass probe is fitted inside the stainless
steel sheath with a probe heating element.
The glass probe is connected
to a glass cyclone with an Erlenmeyer flask to collect the solids from
the cyclone'~ The sampled gases flow from the cyclone through a tared
MSA 1106 BH glass fiber filter. This filter, and the cyclone assembly,
heated box which 0
are enclosed in a is maintained near 250 F. The fi 1 ter
holder is connected to an impinger train consisting of four Greenburg-
Smith impingers with the high velocity tip removed from the first impinger.
The second impinger is used with the tip while the third and fourth
impingers' are modified as the first.
These first two impingers each
contain a measured volume (100 ml) of distilled, deionized water, while
the third impinger is used dry, and the fourth impinger contains approx-
imately 175 grams of silica gel.
A sampling train exit is connected,
in 'line, to a vacuum gauge, a leakless vacuum pump, a dry gas meter, and
a calibrated orifice.
This calibrated orifice differential is measured
with an inclined-vertical manometer.
Velocity variations at the sampling
point are constantly monitored by a pitottube attached to the probe
sheath.
Prior to each test, the sampling train, with probe and nozzle
attached, is leak tested.
Isokinetic sampling is maintained by appropriate adjustment of the
sampling rate, as indicated by the pressure drop across the orifice follow-
ing the dry gas meter.
The necessary orifice pressure differential is
-------
determined by using the nomographs presented in APCA Paper No. 67-119.
This nomograph relates stack gas. velocity, temperature, and moisture
content to the flow rate required for isokinetic sampling.
The ASME train, run in parallel with the EPA train, consists of a
. stainless steel filter holder containing a pre-weighed alundum filter.
Its operation, briefly, is as tollows,:
Sample gases are drawn through a stainless steel nozzle and filter
holder, placed within the stack, into a set of water filled Greenburg-
. Smith impingers.
Isokinetic sampling rates are not determined during
the test but are precalculated from initial pitot and temperature
readings.
Only the material collected by the alundum filt~r is normally
c- ------------ ~--':""''''-'-'~-----,
considered as particulate.
~~~~---...
~-----,.=,-
SULFUR DIOXIDE SAMPLING
Sulfur dioxide emission tests are normally conducted at the same
location as the exhaust particulate tests.
Sample gas is drawn through
a glass wool filter into an electrically heated glass probe, followed
by a coarse frit midget impinger and a second glass wool filter.
The
filter leads to three midget impingers in an ice bath, followed in turn
by a silica gel tube drier, vacuum gauge, dry gas meter and vacuum pump.
The midget bubbler contains 15 milliliters of 80 percent isopropyl
alcohol.' The first two impingers contain 15 milliliters of three percent
hydrogen peroxide solution and the third is operated dry.
Equipment is
leak tested before each run.
The three percent hydrogen peroxide is
prepared the day of the test by dilluting 10 milliliters of 30 percent
reagent grade hydrogen peroxide with 90 milliliters of distilled water.
-------
Part 10, p. 7 of 8
ORSAT FIELD DATA
location
Wood River Power Plant
Comments:
Date
February 20, 1970
Time
1347-1721
Op~rator N. A. Blessing
-- --- -_. u-
Test (C02) (02) (CO)
Reading 1 Reading 2 Reading 3
EDE~3 A 13.3 ~ 5.8 0.0
B 13.4 5.7 0.0
-
- .-. ~ - -- -_.
-. I
,
.
NCAP-31 (12/67)
-------
Part 10, p. 7 of 8
..
ORSAT FIELD DATA
Location Wood River Power Plant
Comments:
Date
~ebruary 20, 1971
Time
1335 -1803
Operator
Gonzalez
.. --- ._- .-
Test (C02) (°2) (CO)
Reading 1 Reading 2 Reading 3
WDE-3. A 13.8 . 5.4 0.0
B 14.0 5.2 0.0.
- -
- .. - - - --. ,
- - I
I ,
i
: .
K(~\P-31 (12/Crl)
-------
RESOURCES RESEARCH, INC,
Personnel
Schroeder
PAGE 1 O~ 2
EnteTed
. Checked
t. .
Plant Conditions, etc~
ASME TEST
Plant
East Alton, Ill. Power Plant
Date
2-19-71
Sample Location
East Duct
Test In
Sheet n
2
Meter # GAS METER CONDITIONS 1\lTl1t1 If
Sampil.e Cu.Ft. Cu.Ft.(Vm) Elaps~ (Rm) (+460=I'm) (Irn) Thimble
Time Number Read in!!; Difference Hin. C.F.M. TelDP of Vacuum"RJ:!: IMP Number
1300 82.92 63 3.0 65 Al
116
1305 86.24 3.32 5 .66 70 3.0 70
1310 89.40 3.16 5 .62 71 2.4 71
1315 92.13 2.73 5 .55 71 2.4 71
1320 94.85 2.72 5 .54 71 2.2 71
1325 97.56 2.71 5 .54 71 2.2 71
1330 100.32 2.76 5 .56 69 2.2 70
1335 03.12 2.80 5 .56 70 2.2 69
1340 ~05.84 2.72 5 .54 69 2.2 71
1345 1108.40 2.56 5 .52 68 2.8 69
1350 1111.50 3.10 5 .62 68 3.0 69
1355 1115.10 3.60 5 .72 70 3.4 70
1400 18.50 3.40 5 .68 71 3.0 72
1405 22.18 3.68 5 .74 70 3.4 70
1410 26.70 4.52 5 .90 68 3.2 68
1415 30.15 3.45 5 .69 67 3.2 65
1 L..?() 32.42 2.27 5 .46 67 3.0 67
-.
3
4
5
Stack/Duct Measurement
Stack Diameter~ inches
Stack Area., Ft2, (A)
Final Gas Temp 300
Starting Gas Temp 300
24' x 24'
Estimated Mc-
.94
Actual- .99
.635
.668
3/8
(D) _'?~L-,,---- Estimated Rm(Corrected)
576 Calculated Rm(Corrected)
Sample Nozzle Dia~~In. (d)
oR % Moistlre o.f Gas 4.91
'1'
°F+460=Ts
760
Barometric Pressure,"Hg,(Pb) 29.9
Sta~k Static Pressure.ln,~O
Condensate,ml (Vw) (+24)
Flue Gas Volume,as is (Va) 653,184 CFM
Flue Gas Volume, dry, std. 431,560 CF'M
Type Pi tot: Standard Type S.1L--
PITOT READINGi'. (1250 A.M. P.H.)
In. from side H, (In. H291- ..JH
Hole 1 Hole 2 Hole 3
1 .07 .265 1 .07 .265 1 .06 .245
2 .06 .245 2 .06 .265 2 .06 .245
3 .06 .245 3 .06 .245 3 .06 .245
4 .06 .245 4 .06 .245 4 .06 .245
+-
Avg,Gas Velocity,fpm(Vsx60)
Vs.-=(2.9 xFs) xJHx.ff
or
2.46 x .278 x 27.6 =
1134 . 0
18.9
Hole 4
1 .08 .283
2 .08 .283
3 .085 .292
4 .08 .283
Hole 5
1 .08 .283
2 .08 .283
3 .08.283
4 .085.292
Hole 6
1 .11 .332
2 .12 .346
3 .14 .374
4 .13 .361
--~_w.._- ---
-------
RESOURCES RESEARCH. INC,
Personnel
Entered
Checked
Plant Conditionsb ete,
ASME TEST
Plant
Date
Sample Location
East Duct Test # 1
CONTINUED
6
Meter #~ GAS HETER CONDITIONS Pumn If
Sample Cu.Ft. Cu.Ft.(Vm) Elaps, (Rn!) (-+460=Tm) (Rn) Thimble
Time Number Readinl! Difference Hin. C.F.H. Temn of Vacuum"HI! IMP Number
1515 136.24 3.82 5 .76 63 3.6 63
1520 140.10 3.86 5 .78 64 3.8 64
1525 144.52 4.42 5 .88 65 4.5 65
1530 148.75 4.23 5 .84 65 4.1 66
1535 152.00 3.25 5 .65 67 2.4 67
1540 154.75 2.75 5 .56 67 2.2 67
1545 157.40 2.65 :, .54 62 2.2 62
1550 160.21 2.81 5 .56 62 2.2 62
77 .29 77.29 120 68 2.9 67
Sheet #2
1
Stack/Duct Measurement
Stack Diameterb inches (D)
Stack Area., Ft2, (A)
Final Gas Temp
Es timated Mc-
Estimated Pun(Corrected)
Calculated Rm(Corrected)
Sample Nozzle Dia..,In. (d)
oR % Hoist\.re of Gas
Actual -
~
Starting Gas Temp
°F+460=Ts
Barometric Pressure,"Hg~(Pb)
Stack Static Pressure, In_12'O
Condensate.m1 (V\J)
Flue Gas Volume. as is (Vo)
+-
Avg.Gas Ve1ocity,fpm(Vsx60)
Vs=(2.9 xFs) x.JHx..ff
or
2.46
Flue Gas Volume, dry, std.
Type Pitot: Standard
CFM
CFM
PITOT READINGS (
In. from s3-de H. (In. H2~
Type S-
A.M. P.M.)
VIi
--..-.- .-
-------
RESOURCES RESEARCH, INC,
Personnel
Schroeder
Entered
Checked
Plant Conditions~ etc~
ASME TEST
Plant East Alton, Ill.
Power Plant
Date' 2-20-71
Sample Location
West Duct
Test 1#2
7
Meter 11 GAS METER CONDITIONS Pullin If
Sample Cu.Ft. Cu.Ft.(Vm) E1aps~ (Rm) (+460:fu) (1m) Thimb1~
- Time Number Readinl! Difference Min. C.F.M. TeDID of vacuum"Hp' IMP Number
1415 60.70 40 2.4 41 Al 93
-
1420 63.58 2.88 5 .58 41 2.4 41
1425 65.98 2.40 5 .48 41 2.0 41
1430 68.51 2.53 5 .51 41 2.2 41
1435 71.32 2.81 5 .56 41 2.4 41
1440 73.95 2.63 5 .53 41 2.2 41
1445 76.68 2.73 5 .55 41 2.4 41
1450 79.14 2.46 5 .50 41 2.2 41
1455 81. 90 2.76 5 .56 41 2.4 41
1520 85.82 3.92 5 .78 41 3.0 41
1525 89.95 4.13 5 .84 41 4.0 41
1530 93.62 3.67 5 .73 41 3.4 41
1535 97.57 3.95 5 .80 41 3.8 41
1625 100.65 3.08 5 .62 42 2.8 42
1630 103.25 2.60 5 .52 41 2.2 41
1635 106.18 2.93 5 .59 41 2.7 41
1640 108.78 2.60 5 .52 41 2.6 41
Sheet ff1
12
11
8
Stack/Duct Measurement
Stack Diameterb inches
Stack Area, Ft2, (A)
Final Gas Temp 300
Starting Gas Temp 280
24' X 24'
Estimated Mc-
.98
Actual -
(D)
576
'?
576
Estimated Rm(Corrected)
Calculated P.m(Corrected)
Sample Nozzle Dia~.In.(d)
oR % Moistu:e o,f Gas
3/8
°F+460=Ts
740
Barometric Pressure,"Hg,(l'b)
Stack Static Pressure, In'12'O
Condensate,ml (Vw)
Flue Gas Volume, as is (Vo)
Flue Gas Volume, dry, std.
29.9
+-
Avg.Gas Velocity,fpm(Vsx60)1002.0
Vs=(2.9 x F s) x JH x ..ff 2 .46x. 250x27. 2=16.7
or
2.46
+ 62
CFM
CFM
Type PI tot: Standard Type S-1L-
PIT~r READINGS ( 11 A.M. P.M.)
In. from side H. (In. H2~ - ..JH
Hole 7 Hole 8 Hole 9
1 .10 .316 1 .06 .245 1 .05
2 .13 .361 2 .05 .224 2 .06
3 .11 .332 3 .065 .255 3 .05
4 .12 .346 4 .06 .245 4 .05
HolE! 10 Hole 11 Hole 12
.224 1 .04 .200 1 .06 .245 1 .06 .245
.245 2 .224 - 2 .06 .245 2 .04 .200
.05
.224 3 .05 .224 3 .05 .244 3 .05 .224
.224 4 .06 .245 4 .06 .245 4 .06 .245
--
-----~.~-'_.
-------
RESOURCES RESEARCH, INC,
Personnel
Schroeder
Entered
Checked
Plant Conditions~ etc~
ASME TEST
Plant
East Alton, Ill. Power Plant
Date
2/20/71
Sample Location
West Duct Test #2
CONTINUED
Sheet 1f2
9
Meter # GAS METER CONDITIONS Pumn If.
Sample Cu.E't. Cu.Ft.(Vm) E1sps, (Rn!) (+460=rm) (Rn) Thimb IE
Time Number Readin!!: Difference Min. C.F.M. Te!IID of Vacuum"HQ Number
1640 111. 40 2.62 5 .52 39 2.4 39
1645 113 . 94 2.54 5 .52 39 2.6 39
116.55 2.61 5 .52 39 2.6 39
1.1.~.1.4 L.O~ :J .:JLfo .:>~ ./:.0 ':>';1
121. 60 2.36 5 .48 39 2.0 39
124.40 2.80 5 .56 40 2.6 40
126.95 2.55 5 .52 40 2.4 40
66.25 66.25 115 .58 41 2.6 41
-
10
Stack/Duct Measurement
Stack Diameterb inches (D)
Stack Area~ Ft2, (A)
Final Gas Temp ~
Starting Gas Temp 0F+460=Ts
Barometric Pressure."Hg,(Pb)
Stack Static Pressure,In,HZO
Condensate.m1 (Vw)
Flue Gas Volume,as .is (Vo)
Estimated Mc-
Estimated Rm(Corrected)
Calculated Rm(Corrected)
Actual-
Sample Nozzle Dia~~In.(d)
oR % Moisttre of Gas
+-
Avg.Gas Velocity,fpm(Vsx60)
Vs=(2.9 xFs) x.JHx.ff
or
2.46
Flue Gas Volume,dry,std.
Type Pitot: Standard
CFM
CFM
PITOT READINGS (
In. from side .!:!.-J1!!.J!291-
Type S-
A.M. P.M.)
Vii
---
--..--..---
-------
APPENDIX E
1.
STANDARD SAMPLING PROCEDURES
2.
-------
APPENDIX E-l
STANDARD SAMPLING PROCEDURES
PARTICULATE SAMPLING
With an unstable plant operation a trial run is often conducted.
If
the trial turns out to be satisfactory it may be considered a part of the
final testing.
Preliminary data is obtained for gas velocity, temperature,
moisture content and other variables which might affect the isokinetic
sampling rate.
Each sample port traverse is divided into a number of
equal areas for each location.
Each test run is designed to obtain simu1-
taneous. samples at each location, for such a period of time that plant
.
operation will be representative, and that sufficient material will have
been obtained for accurate analysis.
Particulate samples are obtained using the equipment and test
procedures as stipulated in "Sample Collection Procedures," published
by OAP.
The sampling train is basically the same as that designed
by the Control Development Program of OAP (formerly the Air Pollution
Control Office), "Gas Stack Sampling Improved and Simplified with
New Equipment," and described in PaperNo. 67-119, presented at the
Air Pollution Control Association meeting at Cleveland, Ohio, in June,
1967.
The above sample equipment is referred to in this report as the
EPA train.
It is essentially the same as that recently described in
Federal Register, Volume 36, Number 159, August 17, 1971, Part II as
Test Method 5.
Its operation, briefly, is as follows:
-------
Sample gases are drawn into an all-glass sampling train through
a button-hook stainless ste~l nozzle with the proper diameter for
isokinetic sampling.
A pyrex glass probe is fitted inside the stainless
steel sheath with a probe heating element.
The glass probe is connected
to a glass cyclone with an Erlenmeyer flask to collect the solids from
~e~cl~~ The sampled gases flow from the cyclone through a tared
MSA 1106 BH glass fiber filter. This filter, and the cyclone assembly,
o
are enclosed in a heated box which is maintained near 250 F. The filter
holder is connected to an impinger train consisting of four Greenburg-
Smith impingers with the high velocity tip removed from the first impinger.
The second impinger is used with the tip while the third and fourth
impingers' are modified as the first.
These first two impingers each
contain a measured volume (100 m1) of distilled, deionized water, while
the third impinger is used dry, and the fourth impinger contains approx-
imately 175 grams of silica gel.
A sampling train exit is connected,
in .line, to a vacuum gauge, a leakless vacuum pump, a dry gas meter, and
a calibrated orifice.
This calibrated orifice differential is measured
with an inclined-vertical manometer.
Velocity variations at the sampling
point are constantly monitored by a pi tot tube attached to the probe
sheath.
Prior to each test, the sampling train, with probe and nozzle
attached, is leak tested.
Isokinetic sampling is maintained by appropriate adjustment of the
sampling rate, as indicated by the pressure drop across the orifice fol1ow-
ing the dry gas meter.
The necessary orifice pressure differential is
-------
determined by using the nomographs presented in APCA Paper No. 67-119.
This nomograph relates stack gas, velocity, temperature, and moisture
content to the flow rate required for isokinetic sampling.
The ASHE train, run in parallel with the EPA train, consists of a
. stainless steel filter holder containing a pre-weighed alundum filter.
Its operation, briefly, is as tollows:
Sample gases are drawn through a stainless steel nozzle and filter
holder, placed within the stack,into a set of water filled Greenburg-
. Smith impingers.
Isokinetic sampling rates are not determined during
the test but are precalculated from initial pitot and temperature
readings.
Only the material collected by the alundum filter is normally
considered as particulate.
SULFUR DIOXIDE SAMPLING
Sulfur dioxide emission tests are normally conducted at the same
location as the exhaust particulate tests.
Sample gas is drawn through
a glass wool filter into an electrically heated glass probe, followed
by a coarse frit midget impinger and a second glass wool filter.
The
filter leads to three midget impingers in an ice bath, followed in turn
by a silica gel tube drier, vacuum gauge, dry gas meter and vacuum pump.
The midget bubbler contains 15 milliliters of 80 percent isopropyl
alcohol.' The first two impingers contain 15 milliliters of three percent
hydrogen peroxide solution and the third is operated dry.
Equipment is
leak tested before each run.
The three percent hydrogen peroxide is
prepa~d the day of the test by dilluting 10 milliliters of 30 percent
reagent grade hydrogen peroxide with 90 milliliters of distilled water.
-------
Temperatures, vacuum and gas meter readings are taken and tabulated
in order to calculate standard volumes.
After sampling, the train is
purged with clean air in order to carryover any 502 trapped in the
isopropyl alcohol.
.NITROGEN OXIDES SAMPLING
Nitrogen oxides sampling is normally carried out at the same exhaust
location as the sulfur dioxide and particulate tests.
The sample gas is
pulled through a glass wool filter and a glass probe into an evacuated
. two-liter flask containing dilute sulfuric acid-hydrogen peroxide solution.
This is prepared according to EPA directions for nitrogen oxides sampling.
The flask is fitted with a three-way stopcock and a pump is employed to
evacuate the flask and purge the probe lines.
Vacuum present in the flask
is measured by a vacuum gauge and the sampling train is leak tested by
pulling a vacuum of 27 inches Hg and observing the pressure gauge.
Initial
readings of pressure, flask temperature and atmospheric pressure are re-
corded after the probe is purged.
After collecting the sample the f1a~k
is sealed and shaken for 15 minutes, then allowed to stand overnight,
before being washed into sample containers for transfer to the laboratory.
ORSAT SAMPLING
An integrated gas sample is obtained with a mylar bag and a peristaltic
pump with adjustable flow rate.
The gases are filtered and cooled prior to
reaching an all plastic and glass flow meter where the sampling rate is
monitored.
Gas samples are taken during the same period during which ve1oc-
ities, temperatures, and particulate samples are obtained.
Analyses are per-
formed at the site immediately after each sample is collected.
-------
APPENDIX E.2
CLEANUP AND ~ALYTICAL PROCEDURES
CLEANUP (EPA PARTICULATE TRAIN)
Probe, Nozzle, Cyclone, and Front Half of Filter Holder
The nozzle, probe, cyclone, flask, and front half of the filter
holder are washed with reagent grade acetone, the washings collected
in a container and transported to the laboratory for analysis.
A
brush and/or rubber policeman is used with the acetone to remove any
particles adhering to the cyclone walls or the flask.
The reagent
acetone used for washing is tested to determine the blank or residue
upon evaporation.
,
Filter
The tared circular MSA type 1106BH filter paper is carefully
removed from the fritted glass support and transferred to a glass
petri dish for later weighing.
Impingers
Water in the first three imping~rs (the original water plus the
condensate) is measured, then emptied into a polyethylene container.
The impingers are then water washed and the washings combined with the
condensate and original water.
Acetone Train Wash
The rear half of the filter holder, including the fritted glass
support, the impingers, and impinger connections up to but excluding the
-------
fourth impinger, are washed with acetone.
These washings are collected
in a polyethylene (since changed. to glass) bottle and sealed for later
analysis.
Silica Gel
Silica gel is transferred (dry) from the fourth impinger to an air-
tight container and sealed.
The impinger is then washed with acetone,
the
acetone being discarded because it contains fine silica gel particles.
CLEANUP (S02 TRAIN)
The impinger containing 80 percent isopropyl alcohol is discarded and
the impingers containing three percent hydrogen peroxide are saved.
These
latter {~pingers contain S02 gas in the form of H2S04'
A glass jar is used
as a sample container for transportation to the laboratory.
CLEANUP (NOx TRAIN)
After storage overnight and shaking for another two minutes the con-
tents are rinsed into glass containers for ~hipment to the laboratory.
ANALYTICAL PROCEDURES (EPA PARTICULATE TRAIN)
Acetone Washings
The acetone washings from the nozzle, probe, cyclone, flask, and filter
front; from the fritted glass, filter back and impinger train; are analyzed
separately by evaporation and drying at ambient temperatures.
Filter Particulate
The filter and particulate collected thereon are dried for 24 hours in
a desiccator at ambient temperature and weighed.
Tare weight of the filter
is then deducted.
-------
Impinger Water
Water collected in the impingers, along with the water washings of the
impingers, is extracted with ether and chloroform.
The extracts are trans-
ferred to a tared dish and evaporated to dryness at room temperature.
After
extraction, the remaining water and solvent are evaporated to dryness on a
steam bath and this additional net weight is added to the total weight of
particulate matter.
SPECIAL NOTE
All samples are now dried in 200 ml beakers to a constant weight.
ANALYSIS (ORSAT MEASUREMENTS)
Orsat measurements for determination of carbon dioxide, oxygen and
carbon monoxide are made using a Burrell Industrial Gas Analyzer or
equivalent.
ANALYSIS (S02 TRAIN)
S02 samples are analyzed by the modified Shell Development method.
Barium perchlorate is used instead of barium chloride (as in the new EPA
source testing Method 6) because of the sharper titration end point obtain-
able with the former reagent.
ANALYSIS (NOv TRAIN)
Samples are analyzed by the standard phenold~sulfonic acid method.
This is now incorporated in the new EPA source testing Method 7.
-------
APPENDIX F
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Analysi8 Date
,;;. /1' - 2. g /., I
-------
COAL AND ASH ANALYSES
-------
DR. WM. B. C. PENNIMAN
laG6'19~B
ESTAi3~ISH~O
1896
CR. ARTHUR LEE BRO'NNE
I BG7019~3'
PENl'-II1vIAN & EROWNE, INC.
CH EM ISTS-ENG IN EE:RS -I NS PECTORS
6252 FALLS ROAD
CAB~E AC:>"ESS
EXECUTIVE: STAFF
GEOI;GE C. PENNIMAN, JR.
CANTE G. BERETTA
PH'~IP M. AIOT
A~~EN W, THOMPSON
HARRY M. BURKHO~OER
GEORGE W, FIE~OS
"BA~TEST"
BALTIMORE. MARYLAND 2t209
TE~o;;PHONE
825.4131
AREA COOE 301
t-~~~~'~."'~~
'." - ~ .~
Iljf~ ~
';10\~ ..:::;''",.l
~"'(".II\t\"
COMBUSTION ENGINEERING DIVISION
REPORT OF A.NALYSIS
March 16, 1971
No.
71-8276
Sample representing.
Bituminous Coal
Client
Resources Res~arch, Inc., Reston, Va.
_. - -..
Source of sample
Client, on TRIll SysteI:'oS P.O. 110-. l/)4 'Wl
Marks or other data
Ill. El~ct.Uo. 1
As Received
Dry Basis
r. Moisture. . . . . . . . . . . . .
14.7
34.5
Fusibility of Ash of.
r. Volatile Matter. . . . . . . .
40.4
Initial Deformation Temperature,
r. Fixed Carbon. . . . . . . . .
39.4
ll.4
46.2
Softening TemPerature,
r. Ash, . . . . . . . . . . . . . . . .
13.4
Fluid Temperature,
r. Total. . . . . . . . .
. . . . . .
100.0
100.0
r. Total Sulfur. . . . . . '. . . .
2.94
3.45
A.S.T.M. Free Swelling Index No. 4 1/2
B.t.u. per pound. . . . . . . . . .
10,3(35
12,175
Ash, Moisture-Free B.t.u. per pound
14.059
Hardgrove grindability index,
PENNIMAN & BROWNE, Inc.
~i{./~~
F-10
OM "CRM 23 1/ea ~MBCO.
cr. t'
-------
CII. WM. 8. C. "'NNIMAN
'888.'."
ESTA8LUU:;:D
CII. AwrHUII LEE BIIOWNE
...7.18U
PENNIMAN
&
BROWNE, INC.
'898
--'
CH EM I STS-ENGI N EERS-I NS PECTORS
82152 FALLS ROAD
CA8LE AD0i1E~8
"SALTl!n"
IIXECUTIYII .TA""
OIlORl S:rste:::s P.O. :10. 164 LU1
. I 11.-.- E1e~j;.. 11
ULTH1ATE NIAI.YSIS
As P.~c~i v~d Dry Besis,
-
% Moisture, es H20 14.72
% Carbcn, &t C 61.64 72.28
% Hydrcg~n, asH 4.02 4.n
% Nitrogen, esll 1.13 1.32
% Sul.fur. 8!;S 2.94 3.45
% Ash 11.39 13.36
% OJeY gen. as 0, by di fr. ~.16 h.8Q
100.00 100.00
..E:NNIMAN 8: BROWNE. INC.
~..4A.v&' ~ /j;,' . ~ fT
~~..,,
-------
r
CR. WM. B. C. PENN!MAN
IG6£~1932
ESTADLISHEO
DR. ARn,UR LEE BROWNE
1887.1933
1896
PENNI1,,1AN
&
13 RO~YJl.!E, Ii-IC.
IXECUTIVIL STAFF
GEOROIL C. PENNIMAN. 'JR.
CANTE G. BERILTTA
PHILIP M. AIDT
ALLEN W. THOMPSON
HARRY M. BURKHOLDER
GEOROE W. F:IELDS
CH EM r STS-ENG 1 N EERS -I NS PECTOF:S
6252 FALLS ROAD
CABL.E A:JDRESS
"BALTEST"
BALTIMORE. MARYLAND 21209
TELEPHONE
82:1.4131
AREA CODE 301
;. ~~.~"<
~~_..~"".
" '.. .
it ~h )~
;;I:.,\'~l
~;'''tt;;;.:).~\t.,."",
COMBUSTION ENGINEERING DIVISION
REPORT OF ANALYSIS
March 16. 1971.
No.
71-8279
Sample representing
31 tuminous Coal.
Client
Resources Rese~ch, Inc., Reston. Va.
Source of sample
Client. on TR~T-Syst-ei1S P.O. Nc.tG4 .LUl
Marks or other data
Ill. Elect. No.2
As Received
Dry Basis
% Moisture. . . 0 . . . . 0 0 0 0 0
16.3
Fusibility of Ash of.
% Fixed Carbon. . . . . 0 0 0 .
33.6
39.4
40.1
Initial Deformation Temperature.
% Volatile Matter 0 . . . 0 0 0 .
Softening Temperattlre.
~7 .1.
%Ash,. 0000000. 0 0 . 0 . o.
Fluid Temperature,
10.7
1.2.8
% Total. 0 . . 0
. . . . . . . . . .
100.0
100.0
2.6~
3.1.5
A.S. ToM. Free Swelling Index N°'4 1/2
% Total Sulfur. 0 . . ; 0 0 . . .
B.tou. per pOtlnd 0 . 0 . 0 0 0 0 . .
10.274
Ash, !troisture.Free 8.t.lI. per pound
12,275
14,077
Hardgrove gr;'ldnbility in de x,
-
PENNIMAN & BROWNE, Inc.
~~ClI. 6~r~%
OM II'ORM 23 1/60 Ht.4BCO.
F-12
emf
D(lnt~... ~.
-------
Oft. WM. B. O. PENNIMAN
lee'.llse
ESTA8L.ISHZO
Oft. ARTHUR LEE BftOWNE
1887..8SS
PENNIl'>'iAN
&
BROV/NE, INC.
18ge
EXECUTIVE ITA""
GEOftGE D. PENNIMAN, Jft.
DANTE G. BERETTA
PHIL'I' M. AIDT
ALLEN W. THOMPSON
HARRY M. BURKHOLDEft
GEOftClIt W. FIELD'
CH EM ISTS-ENC I N EERS-I NS PECTORS
82!S2 FALI.5 ROAD
CAIILE ADDR£SI
'BAL TEST'
BALTIMORE. MARYLAND 21209
~,'III",,11
~ ~1;J' .~
i i,'j "',U- ~
., . -.' ~
~, . '. - :::
~,,""~~';
~('z.t..\r\"
TELEPHONZ
301.8215.4131
COMBUSTION ENGINEERING DIVISION
REPORT OF ANALYSIS
:Iarch
16, 1971
No.
71-8279
Sample 01
Bi t u1':l1 n ::nIS Co al
Clienl
Resources Research, Inc., Reston, Va.
Source of Sample
Mar},s or Olber Dill.
Client t on TR:.! Syster.:.> P.O. !To. 164 LU1
I11~--:.a'!!ctr.~ Ho. 2
ULTn!J\TE ft:'!l'LYSIS.-
As P.e(:~i v.~d
Dry Ba~
% Hoiat ure , as H20
16.29
% Carbon, as C
% HydroGen, f\3 H
59.76
4.09
71.39
4.83
% Ni trogen. as II
% Sulfur, ns S
1.12
1.34
2.64
3.15
% A.'Jh
10. 71
% Oxygen, as 0, by di if.
5.32
12.79
6.45
100.00
100.00
PENNIMAN 8t BROWNE. INC.
,'~ r-/~ /.! ~-
ftJ~v(t "7. /UA.;::,it."
------
1000 "-OR.... .a.A It...
cr.!
F-13
-------
DR. WM. e. D. PCt";'MAN
IfJGGal'if:1c3
ESTAOLI"H~D
1836
D... ARTHUR LEE BROWNE
1887.1933
PENNlbi-\~N Ct :BROWNE:, INC.
CH EM I STS-E:NG I N E:E:?S -I NS PECTORS
6252 FALLS ROAD.
C.'BLE ADDRESS
EXECUTIVE STAFF
GEORGE D. PENNIMAN. JR.
DANTE G. BERETTA
PHILIP M. AIDT
ALLEN W. THOMPSON
HARRY M. BURKHOLDER
GEORG! W. FIELDS
"eAL TEST"
BALTIMORE, MARYLAND 21209
TELEPHONE
825.4131
AilEA CODE 301
; , II,.,
f~t'!'=~~'"'
~'1,':...', E
a '>of .. .
;\ ~- ;...,:. S
;.,\.. '. ' .:
#'if:.;;;:~."t\~"'"
COMBUSTION ENGINEERING DIVISION
REPORT OF A.NALYSIS
Harch 16, 1971
No,
71-8280
Sample representing,
Bi twnnoU5 Coal
Client
Resources Research, Inc., Re3ton, Va.
Source of sample
Client, on'TmrSyste!'i..s p.O. No-- 164 .LUl
Marks or other data
Ill. Elect. no. 3
As Received
Dry Basis
% Moisture. , . . . . . . . . . . .
16.0
Fusibility of Ash of.
% Volatile Matter. . . . . . . .
34.5
41.1
Initial Deformation Temperature.
% Fixed Carbon. . . . . . . . .
39.7
47.2
Softening TemPerature.
%Ash.. . . '.' .. . . . . . . . . .
9.8
11.7
Fluid Temperature.
% Total. . . . . . . . . . . . . . .
100.0
100.0
% Total Sulfur. . . . . . . . . .
2.56
3.05
A.S. T.M. Free Swelling Index No.4 1/2
B./.u. per pound. . . . . . . . . .
10.387
12,365
Ash. Moisture-Free B.t.u. per pound
14,00 3
Hardgrove grindability index.
8
PENNIMAN & BROWNE, Inc.
~",£lI. 44//,4,'
OM rORM 23 1{8& HM8CO.
en!"
F-14
D~~te G. Ber~ttn
-------
DR. WM. B. D. PENNIMAN
1888.'.38
ISTA8L.ISI-tI::D
DII. AIITHUII LEE ellOWNIt
'887.1.33
PE~INI~IAN
&
BRO'\1VNE, INC.
10110
aXO:CUTIVO: .TA~~
OItOIlOE D. PItNNIMAN. JII.
DANTE G. BItRItTTA
PHILIP M. AIDT
ALLEN W, THOMPSON
HAIIRY M. ElURKHOLDItR
OItOIlOE W, FIELD.
CH EM I STS-ENG I N EERS-I NSPECTORS
e2:52 FALLS ROAD
CA8LE ADDi1&:S.
. eAL TEST"
BAL. TIMORE. MARYLAND 21209
~~~-:'Yd~I""( '"
.! - .
R" ",'" E
I' -<., -
, ::. \-j., i=
~.,~, ...
~.(['r.:.\"'i.'~
TaLEPHONI:
301.8211.41:;1
COMBUSTION ENGINC:ERING DIVISION
REPORT OF ANALYSIS
March 16, 1971
No.
71-82 eo
Sam,le 01
Bi tur'Jinou3 CoaJ.
Clienl
ReGources Resear~~. Inc., Re3ton. Va.
Sour~e 01 Sample
Client, on TR'1l Systet..s P.O. 1io. 164 WI
Maris Of" Olbet' Dill.
-I llr- E:te c1;" 13
ULTni.-\TE~'}LYSIS-
As Rec,,:iY~'i
Dry Bg.';is
% }.~olsture, as H20
16.01
% Carbo::, as C
% Hydro.::;en. a.<; H
% Nitrog~n, as N
% Sulfur, S3 S
60.14
71.60
4.13 .
4.92
1.10
1.31
% A3h
2.56
9.82
3.05
11.69,
% Oxygen, as 0, by ditt.
6.~4
7.113
100.00
100.00
e
PENNIMAN e. BROWNE. INC.
-z;: 1 -
, ;1 ..,oJ
~wG . ~;;f..AirJ.,-<~
1000 "O"M 'U.A ".88 Cr.lf
Dante G. Beretta
-------
APPENDIX G
-------
2-15-71 (Monday)
2-16-71 (Tuesday)
2-17-71 (Wednesday)
2-18-71 (Thursday)
2-19-71 (Friday)
2-20-71 (Saturday)
2-21-71 (Sunday)
APPENDIX G
TEST LOG
Arrive, begin unpacking.
Unpack, set up equipment, take velocity and
temperature traverses and run a moisture test.
2 S02 tests (1 per duct)
4 NO tests (2 per duct)
x
l S02 test West duct only
2 NO tests West duct only
x
1
simultaneous particulate test
(East and West duct)
2
Orsat test
(1 per duct)
1
simultaneous particulate test
(East and West duct)
2 Orsat tests (1 per duct)
2 S02 tests (1 per duct)
4 NO tests (2 per duct)
x
1
simultaneous particulate test
(East and West duct)
2
(1 per duct)
Orsat tests
Pack equipment.
Depart.
-------
APPENDIX H
-------
APPENDIX H
See power plant emission survey conducted
at Trenton, Michigan under same contract.
-------
APPENDIX I
-------
N. A. Blessing, Chemist, Project Leader
R. N. Allen, Chemical Engineer
C. C. Gonzalez, Chemist
W. E. Schroeder, Chemist
Herb Dancey, Technician
-------
APPENDIX J
-------
APPENDIX J
STOICHIOMETRIC CALCULATIONS
An attempt was made to relate fuel input to gas flow and determine
measured flows with Stoichiometric determinations of flow.
The results
for the first set of samples were not as close as would be desired.
The first sample calculated to be a little less than 15 percent
below measured volume, whereas the second and third samples were
approximately 5 percent and 3 percent low, respectively.
It is felt that these differences are due to a number of small
errors and problems.
As discussed previously in the report, the sampling
and traverse points were limited to approximately one-third of the total
duct area.
The very basis of the measured flow was therefore not
completely representative.
In addition, the data on operating parameters
.of the plant covers a broad time span, and not necessarily
that
particular time during which the traverse was performed.
The (informal) request for this information was not received until
some time after the sampling was completed.
Required data was apparently
not as carefully gathered and recorded as needed for these calculations.
The calculations and results are given in the following pages, and
1
were made with reference to several recognized sources.
1.
Combustion Engineering, Glenn.R. Fryling, M.E~ Editor, revised edition,
published by Combustion Engineering, Inc.,. New York, N. Y.
Hauck Industrial Combustion Data, third edition, published by Hauck
Manufacturing Company, New York, N. Y.
North American Combustion Handbook, first edition, published by
North American ~anufacturing Company, Cleveland, Ohio.
-------
MEASURED FLOWS VS STOICHIOMETRIC
Air Volume Air Volume
Test Number Measured CFM Stoichiometric CFM
1 829,000 712,000
2 846,000 805,000
3 825,000 804,000
-------
EXAMPLE CALCULATIONS
Test No.1
Constituent % X Factor = cu ft/1b Fuel
C 61.64 x 1. 505 = 92.7
H 4.02 x 5.46 = 22.0
S 2.94 x 0.557 = 1.64
H20 14.72 x 0.21 = 3.1
N 1.13 x 0.135 = 0.15
119.59
-0 4.16 x 0.448 -1. 87
117.72 cu ft/1b fuel
@ 100% theoretical air
35.5%
excess air
135.5% x 117.72 cu ft/1b fuel
=
159.2 cu ft/1b fuel
fuel consumption:
134.1 tons/hour
134.1 tons/hour x 2000 1bs/ton ~
60 min/hour = 4,470 1bs/min
4,470 1bs/min x 159.2 cu ft/1b =.712,000 cu ft/min
measured volume from summary:
829,000
------- |