MIDWEST RESEARCH INSTITUTE
MRI
EPORT
SULFURIC ACID EMISSION TESTING OF A POWER PLANT
at
Shawnee Power Station
Paducah, Kentucky
EPA Project Report No. 74-SPP9
by
William H. Maxwell
Midwest Research Institute
EPA Contract No. 68-02-0228
MRI Project No. 3585-C, Task 41
For
Emission Measurements Branch
Office of Air Quality Planning and Standards
Environmental Protection Agency
Research Triangle Park, North Carolina 27711
Attn: Mr. Peter R. Westlin
MIDWEST RESEARCH INSTITUTE 425 VOLKER BOULEVARD, KANSAS CITY, MISSOURI 64110 • 816561-0202
-------
DISCLAIMER
This report was furnished to the Environmental Protection
Agency by Midwest Research Institute, Kansas City, Missouri,
in fulfillment of Contract No. 68-02-0228, Task No. 24. The
contents of this report are reproduced herein as received
from the Midwest Research Institute. The opinions, findings,
and conclusions expressed are those of the author and not
necessarily those of the Environmental Protection Agency.
Mention of company or product names is not to be considered
as an endorsement by the Environmental Protection Agency.
MRI WASHINGTON, D.C. 20005-1522 K STREET, N.W. • 202 293-3800
-------
SULFURIC ACID EMISSION TESTING OF A POWER PLANT
at
Shawnee Power Station
Paducah, Kentucky
EPA Project Report No. 74-SPP9
by
William H. Maxwell
Midwest Research Institute
EPA Contract No. 68-02-0228
MRI Project No. 3585-C, Task 41
For
Emission Measurements Branch
Office of Air Quality Planning and Standards
Environmental Protection Agency
Research Triangle Park, North Carolina 27711
Attn: Mr. Peter R. Westlin
MIDWEST RESEARCH INSTITUTE 425 VOLKER BOULEVARD, KANSAS CITY, MISSOURI 64110 • 816561-0202
-------
SULFURIC ACID EMISSION TESTING OF A POWER PLANT
at
Shawnee Power Station
Paducah, Kentucky
EPA Project Report No. 74-SPP9
by
William H. Maxwell
Midwest Research Institute
EPA Contract No. 68-02-0228
MRI Project No. 3585-C, Task 41
For
Emission Measurements Branch
Office of Air Quality Planning and Standards
Environmental Protection Agency
Research Triangle Park, North Carolina 27711
Attn: Mr. Peter R. Westlin
MIDWEST RESEARCH INSTITUTE 425 VOLKER BOULEVARD, KANSAS CITY, MISSOURI 64110 • 816561-0202
-------
PREFACE
The work reported herein was conducted by Midwest Research In-
stitute (MRI) under Environmental Protection Agency (EPA) Contract No.
68-02-0228, Task No. 37, Change No. 1.
The project was under the technical supervision of Mr. Paul C.
Constant, Jr., Head, Environmental Measurements Section of the Physical
Sciences Division. Mr. William Maxwell served as Crew Chief and was
assisted by Messrs. Emile Baladi, George Cobb, Bruce DaRos, and John Kitko.
Miss Christine Guenther was responsible for the data reduction and computer
analysis. The analysis of the samples was done by Mr. Thurmon Oliver.
Approved for:
MIDWEST RESEARCH INSTITUTE
Paul C. Constant, Jr.,
Program Manager
21 May 1974
ii
-------
TABLE OF CONTENTS
I. Introduction 1
II. Summary of Results 1
III. Process Description 3
IV. Location of Sampling Ports . 4
V. Sampling and Analytical Procedures 4
VI. Discussion 5
Appendix A - Results of Analysis - Printout of Computer
Calculations 7
Appendix B - Sample Calculations 21
Appendix C - Field Data Sheets 26
iii
-------
I. INTRODUCTION
This report presents the results of source testing performed by
Midwest Research Institute on a pilot-plant scale wet scrubber at the
Shawnee Power Station, Paducah, Kentucky. Three tests each for I^SO, mist
and S02 were run on the inlet and outlet ducts to the scrubber.
The purpose of the testing was to determine the efficiency of a
wet scrubber in removing l^SO, . The data were to be used in conjunction
with comparison tests of in-stack and EPA Method 5 particulate sampling
methods.
The scope of work for this project specified: three simultaneous
tests on the inlet and outlet of the scrubber to be completed in accordance
with the Federal Register, Vol, 36, No. 159, Part II, 17 August 1971. Sam-
pling was completed with one test being run on 19 February 1974 and two tests
on 20 February 1974.
The following sections of this report present: (1) the summary
of results, (2) the process description, (3) the location of sampling ports,
(4) sampling and analytical procedures, and (5) a discussion.
II. SUMMARY OF RESULTS
Table I contains a summary of results for this testing. A com-
plete listing of the data and computer printout of the calculations is
found in Appendix A. Sample calculations are found in Appendix B.
The 02 data used in the determination of the stack-gas molecular
weight were obtained from the plant process information by EPA. The COo
and CO data are representative of values obtained at other coal-fired power
plants tested. Orsat analyses were not run during this testing.
The values listed on the computer printout for the amount of water
collected are assumed values computed from moisture concentrations of 7% and
20% by volumes for the inlet and outlet ducts, respectively.
-------
N>
Concentration of HjSO, - Ib/dscf
- mg/ncm
-.ppni
- Ib/hr
- kg/hr
. - g/dscf
- g/acf
Percent efficiency
of removal—'
Concentration of SOj
(total)
Percent efficiency
of removal—
TABLE I
SUMMARY OF RESULTS
Run Number
1-Inlet
0.00000082
13.1
3.2
0.7
0.3
0.0057
0.0037
1 -Out let
0.00000043 .
7.0
1.7
0.3
0.2
0.0030
0.0024
2-Inlet
0.00000352
56.4
13.9
3.2
1-5
0.0247
0.0168
2-Outlet
0.00003170
507.7
125.1
26.6
12.1
0.2219
0.1764
3-Inlet
0.00017006
2,724.1
671.0
150.8
68.4
1.1904
0.8017
3-Outlet
0.0000082?
132.1
32.5
7.5
3.4
0.0577
0.0457
46.875
- Ib/dscf
- mg/ncm .
- ppm
- Ib/hr
- kg/hr
- g/dscf.
- g/acf
0.00019421
3,110.8
1,173.3
167.8
76.1
1.3594
0.8801
0.00005993
959.9
362.0
48.1
21.8
0.4194
0.3287
0.00037
51.8
2,244.7
339.1
153.8
2.6010
1.7675
0.00011591
1,856.6
700.2
97.1
44.1
0.8114
0.6451
95.156
0.00030421
4,872.9
1,837.9
269.8
122.4
2.1295
1.4341
0.00004210
674.4
254.3
38.4
17.4
0.2948
0.2332
69.146
68.807
86.164
aj Obtained from ppm values
-------
III. PROCESS DESCRIPTION
The Shawnee Power Station, operated by The Tennessee Valley
Authority (TVA), is a coal-fired, steam-generation station, having 10
turbines, each served by a boiler and stack. A portion of the exhaust
gases from one of these stacks is diverted for use with three pilot-plant
scale wet scrubber systems. It was on one of these wet scrubber systems
that the current testing was done. Figure 1 presents a flow diagram of
the operation, showing the inlet and outlet sampling sites.
Outlet
Sampling
Site ——
Reheater
Scrubber
Stack
Main
Stack
Fan
Inlet
Sampling
Site
Boiler
Turbine
Figure 1 - Flow Diagram of Plant Operation
The scrubber tested was a Bechtel Turbulent contact absorber de-
signed to handle approximately 30,000 cfm of exhaust gas. Water was the
scrubbing medium flowing concurrently over plastic spheres in the scrubber
.main chamber. Downstream of the scrubber were a demister and a reheater.
-------
IV. LOCATION OF SAMPLING PORTS
Both sampling locations were sited in enclosed sheds as protec-
tion against the weather. Existing 4 in. ID ports were utilized. Due to
the proximity of the shed wall to one of the outlet ports, complete traversing
on that port could not be accomplished. It was decided on-site by EPA and
MRI personnel to run two traverses in the accessible port instead of only
partially traversing in the blocked port. It was indicated that the sites
had been selected to comply with EPA guidelines so the minimum number of
points, 12, was used for the 2-hr tests. Figure 2 shows a schematic layout
of the sampling sites and ports used.
West
Outlet Site
Insufficient
North
•Shed Wall-
Figure 2 - Schematic of Sampling Sites
V. SAMPLING AND ANALYTICAL PROCEDURES
The samples were taken with Research Appliance Company (RAG)
Model 2243 "StacksampIr" equipment, as modified by MRI. Sampling train ,
specifications were in accordance with the Federal Register. "Method 8 -
Determination of Sulfuric Acid Mist and Sulfur Dioxide Emissions from
Stationary Sources," Vol. 36, No. 159, 17 August 1971, with the following
exceptions:
1. An additional Greenburg-Smith impinger containing 100 ml of
80% isopropanol was placed in front of the filter between the isopropanol
and hydrogen peroxide. This gave a total of five impingers: two isopropanol,
two hydrogen peroxide, and one silica gel.
-------
2. Due to the ash content of the inlet duct, a cyclone and a
filter were placed in front of the first isopropanol impinger. After the
first run, this was also done for the outlet duct.
3. The system was purged for 30 min following each test. These
exceptions were done upon the suggestion and approval of EPA.
Sample recovery was done in the field in accordance with the
Federal Register except that the filters were not added to the isopropanol
wash of the probe and cyclone or the contents of the first two impingers
until they were returned to the lab at MRI.
The analytical procedures were those described in the Federal
Register. Due to the presence of the fly-ash material, in addition to the
filter material in the isopropanol solution, this solution was filtered
prior to analysis to observe the end point more easily.
VI. DISCUSSION
Sampling was done simultaneously on both sites over a 2-hr period.
There were two, six-point traverses per run, with each point sampled for
10 min. Data were recorded every 5 min. During the first run, it was discovered
that a 4-min timer was being used on the outlet duct, resulting in 8-min
points on the first traverse. As the second traverse consisted merely of a
retracing of the first in the same port, the same tinier was used but for
12-min points on the second traverse to get the 2-hr total sample time.
Large meter vacuum readings were encountered during the sampling
periods on both ducts. This resulted partially from the high stack vacuum,
reported as being 14 in. of water, the increased number of impingers and
filters over that normally used for particulate sampling,and the high stack
grain loading which tended to plug the first filters. At the higher vacuum
readings, the silica gel, on occasion, tended to boil, i.e., be physically
lifted by the gas flow in the impinger. Due to the higher vacuums, it be-
came necessary to replace the first filter on the inlet train in order to
maintain isokinetic sampling conditions. This was done once for runs 1
and 2 and twice on run 3.
Complete traversing could be effected on the inlet duct but the
train could not be removed from the stack without first disconnecting the
probe. Due to the high stack vacuum, this resulted in the loss of any
sample contained in the probe. However, due to the large amount of mass
collected by the cyclone and filter, the loss is believed to be negligible.
-------
During run 3, on the inlet duct, it was observed that the hydrogen
peroxide from the last impinger of the train was spilling over into the silica
gel impinger due to the large amount of froth resulting from the bubbling
action of the gas on the liquid. This did not cease even when the first
filter was replaced. No determination could be made as to how much was lost
but the resulting SC>2 data could be biased.
When the samples were opened at MRI, it was noticed that all of the
hydrogen peroxide samples smelled of isopropanol indicating the perhaps some
of the isopropanol was carried over through the filter to the hydrogen per-
oxide. This was not physically observed in the field.
At least one reference (Industrial Source Sampling, Brenchley,
Turley, and Yarmac) states that Method 8 sampling should not be used on any
source having a high particulate load which could cause interferences with
the wet chemical analysis. It is not known how this particulate load would
affect the sampling under study or if filtering the sample will remove the
interferences.
-------
APPENDIX A
RESULTS OF ANALYSIS - PRINTOUT OF COMPUTER CALCULATIONS
-------
DATA,AND CALCULATED VALUES
RUN-
1-1 DATE- 02-19-74
ATMOS ATMOS STACK
TEMP PRES VAC COND
(06.F) (I.HG) (I.H20) (ML)
45.0 29.15 14.00 102.1
STACK INIT PERC PERC PERC PITOT
WT-PTL KT-TTL AREA VOL 02 C02 CO TUBE
(M6) (H6) (FT2) (DCF) DRY DRY DRY COEF
8.73 758.74 3.5 11.0 0.0 .850
00
PORT-
POINT
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
1
1
2
2
3
3
4
4
5
5
6
6
6
6
5
5
4
4'
3
3
.2
2
i
1
SAMP
TIME
(MIN)
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
METER
VOL
(DCF) (
761.36
763.93
766.67
769.47
772.26
775.02
777.84
780.64
783.47
786.33
789.29
792.29
795.05
797.95
800.82
803.67
806.52
809.33
812.02
814.71
817.55
820.38
823.12
825.80
DELTA
P
I.H20)
.350
.360
.440
.450
.410
.410
.420
.420
.460
.450
.480
.470
.490
.490
.450
.450
.410
.410
.340
.325
.440
.440
.360
.360
DELTA
H
(I.H20)
.910
.930
1.140
1.160
1.080
1.080
1.090
1.090
1.180
1.150
1.230
1.210
1.260
1.260
1.160
1.160
1.080
1.080
.890
.840
1.140
1.140"
.930
.930
TEMP
IN
(D.F)
60.0
70.0
81.0
86.0
90.0
92.0
94.0
95.0
96.0
97.0
98.0
99.0
65.0
78.0
87.0
91.0
94.0
95.0
96.0
95.0
97.0
96.0
98.0
98.0
TEMP
OUT
(D.F)
47.0
46.0
51.0
53.0
57.0
59.0
62.0
63.0
64.0
66.0
67.0
68.0
61.0
61.0
62.0
63.0
64.0
65.0
66.0
67.0
68.0
68.0
69.0
70.0
TRAIN
VAC
(I.HG)
8.0
8.0
8.0
9.0
9.0
9.5
9.5
9.5
10.0
10.0
11.0
11.0
8.0
9.5
9.5
9.5
8.5
8.5
8.0
9.0
9.0
9.0
8.5
8.0
STACK
TEMP
(D.F)
310.0
309.0
320.0
316.0
315.0
314.0
316.0
315.0
312.0
314.0
315.0
315.0
314.0
311.0
310.0
312.0
309.0
305.0
301.0
300.0
300.0
299.0
29S.O
295.0
BOX PROBE
TEMP T 01A VEL
(D.F) (IN) (FPM)
60.0
65.0
75.0
65.0
75.0
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
2502.2
2536.1
2823.7
2848.3
2717.0
2715.3
2751.7
2750.0
2872.4
2844.6
2939.8
2909.0
2968.4
2962.6
2837.3
2841.0
2706.5
2699.4
2451.8
2395.5
2787.3
2785.5
2512.9
2512.9
-------
AND CALCOEATED~VA'LUE5~
RUN-
1-0 DATE- 02-19-74
ATHOS
TEMP
DQ.F)
45.0
PORT-
POINT
E
e
E
E
E
E
E
E
E
E
.E
E
E
E
E
E
E
E
E
E
E
E
E
E
E
E
.E
E
E
E
1
1
2
2
3
3
4
4
5
5
6
6
6
6
6
5
5
5
4
4
4
3
3
3
2
2
2
1
1
1
ATMOS
PRES
(I.H6)
29.15
SAMP
TIME
(MIN)
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4*00
4,00
4.00
4.00
4.00
4.00
STACK
VAC
(I.H20)
14.00
METER
VOL
(OCF) (
299.69
301.69
303.78
305.61
307.93
310.17
312.36
314.57
316.77
318.96
321.01
322.96
324.89
326.59
328.43
330.20
331.92
333.66
335.40
337.15
338.85
340.90
343.00
345.07
347.11
349.13
351.10
352.95
354.72
356*47
H20
CONO
(ML)
300.5
DELTA
P
I.H20)
.420
.420
.450
.450
.470
.470
.480
.480
.440
.440
.360
.360
.360
.250
.250
.300
.300
.300
.300
.300
.300
.450
.450
.450
.440
.440
.440
.350
.350
.350
STACK INIT PERC PERC PERC PI TOT
WT-PTL WT-TTL AREA VOL 02 C02 CO TUBE
(MG) (M6) (FT2) (DCF) DRY DRY DRY COEF
8.73 297.54 3.5 11.0 0.0 .850
DELTA TEMP TEMP TRAIN STACK BOX PROBE
H
(I.H20)
.850
.850
.940
.940
.950
.950
.960
.960
.880
.880
.730
.730
.730
.530
.530
.610
.610
.610
.610
.610
.610
.930
.930
.930
.890
.890
.890
.710
.710
.710
IN
(D.F)
45.0
60.0
76.0
80.0
84.0
87.0
90.0
92.0
94.0
94.0
94.0
94.0
94.0
93.0
91.0
90.0
90.0
89.0
88.0
88.0
87.0
87.0
89.0
91.0
92.0
93.0
93.0
94.0
95.0
95.0
OUT
(D.F)
45.0
50.0
54.0
57.0
59.0
60.0
61.0
62.0
64.0
64.0
65.0
65.0
65.0
62.0
60.0
58.0
58.0
59.0
59.0
62.0
61.0
62.0
64.0
66.0
67.0
68.0
69.0
70.0
70.0
71.0
VAC
(I.HG)
11.0
11.0
11.0
12.0
13.0
13.0
13.0
13.0
13.0
12.5
12.0
12.0
12.0
12.0
12.0
11.0
11.0
11.0
11.0
11.0
11.0
17.0
20.0
21.0
23.0
23.0
23.0
23.0
23.0
23.0
TEMP TEMP
(D.F) (D.F)
150.0 50.0
150.0
160.0
160.0
170.0
170.0
170.0
170.0
170.0
170.0
200.0
200.0
200.0
200.0
200.0
180.0 75.0
180.0
180.0
180.0
180.0
180.0
175.0 80.0
175.0
175.0
180.0 80.0
180.0
180.0
160.0 75.0
160.0
160.0
T DIA
(IN)
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
,250
.250
.250
.250
.250
.250
.250
VEL
(FPM)
2507.6
2507.6
2616.8
2616.8
2695.8
2695.8
2724.3
2724.3
2608.3
2608.3
2414.8
2414.8
2414.3
2012.4
2012.4
2170.8
2170.8
2170.8
2170.8
2170.8
2170.8
2648.2
2648.2
2648.2
2628.9
2628.9
2628.9
2307.8
2307.8
2307.8
-------
DATA AND CALCULATED VALUES
RUN-
2-1 DATE- 02-20-74
ATMOS
TEMP
(D0.F)
40.0
ATMOS
PRES
(I.HG)
STACK H20
VAC COND
(I.H20) (ML)
29.84 14.00 102.7
WT-PTL
(M6)
WT-TTL
(M6)
STACK
AREA
(FT2)
INIT
VOL
(DCF)
PERC PERC PERC PITOT
02
DRY
C02
DRY
CO
DRY
TUBE
COEF
8.73 839.55 3.5 11.0 0.0 .850
PORT-
POINT
S
S
S
S
S
S
S
S
S
s
S
S
S
S
S
S
S
S
S
S
S
S
S
S
1
1
2
2
3
3
4
4
5
5
6
6
6
6
5
5
4
4-
3
3
2
2
I
1
SAMP
TIME
(MIN)
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
METER
VOL
(DCF) (
842.32
844.94
847.73
850.51
853.26
856.02
858.81
861.57
864.46
867.27
869.99
872.57
875.49
878.47
881.40
884.35
887.18
890.03
892.83
895.54
898.37
901.12-
903.78
906.44
DELTA
P
I.H20)
.370
.370
.450
.450
.410
.420
.430
.430
.480
.460
.500
.510
.500
.500
.490
.490
.430
.440
• 430
.440
.460
.460
.390
.390
DELTA
H
(I.H20)
.950
.950
1.180
1.180
1.080
1.100
1.130
1.130
1.230
1.230
1.000
.970
1.300
1.300
1.280
1.280
1.130
1.140
1.130
1.140
1.190
1,190
1.000
1.000
TEMP
IN
(D.F)
72.0
77.0
88.0
94.0
97.0
99.0
100.0
101.0
102.0
103.0
102.0
102.0
93.0
102.0
108.0
109.0
110.0
110.0
110.0
110.0
109.0
108.0
108.0
108.0
TEMP
OUT
(D.F)
56.0
64.0
66.0
67.0
68.0
70.0
71.0
72.0
74.0
74.0
76.0
76.0
76.0
76.0
78.0
79.0
79.0
80.0
81.0
81.0
82.0
82.0
83.0
83.0
TRAIN
VAC
(I.HG)
10.0
10.0
7.0
8.0
8.5
9.5
11.5
13.0
17.0
19.0
23.0
24.0
7.5
7.5
8.5
9.5
10.5
12.0
14.0
16.0
18.0
20.0
21.0
23.0
STACK
TEMP
(D.F)
290.0
284.0
290.0
29 1 . 0
291.0
294.0
291.0
293.0
293.0
293.0
290.0
291.0
293.0
295.0
300.0
291.0
291.0
294.0
290.0
290.0
290.0
291.0
279.0
285.0
BOX PROBE
TEMP T 01A VEL
(D.F) (IN) (FPM)
50.0
50.0
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
,250
.250
.250
.250
.250
.250
2508.8
2498.7
2766.7
2768.6
2642.7
2680.0
2706.3
2709.9
2863.2
2863.2
2916.4
2947.4
2922.2
2926.1
2906.3
2889.0
2706.3
2743.1
2704.5
2735.8
2797.3
2799.2
2556.7
2567.1
-------
DATA AND CALCULATED VALUES
RUN-
2-0 DATE- 02-20-74
ATMOS ATMOS STACK
TEMP PRES VAC COND WT-PTL WT-TTL
(D6.F) (I.HG) (I.H20) (ML) (MO) (M6)
40.0
29.84 14.00 316.0
STACK INIT PERC PERC PERC PITOT
AREA VOL 02 C02 CO TUBE
-------
DATA AND CALCULATED VALUES
RUN-
3-1 DATE- Oa-20-74
ATMOS ATMOS STACK H20
TEMP PRES VAC COND
(OG»F) (I.HG) (I.H20) (ML)
50.0 29.90 14.00 101.3
STACK IMT PERC PERC PERC PITOT
WT-PTL WT-TTL AREA VOL 02 C02 CO TUBE
-------
DATA AND CALCULATED VALUES
RUN-
3-0 DATE- 03-20-74
ATMOS ATMOS STACK H20
TEMP PRES VAC COND
(DG.F) (I.HG) (I.H20) (ML)
50.0 29.90 14.00 341.2
STACK INIT PERC PERC PERC PITOT
HT-PTL KT-TTL AREA VOL 02 C02 CO TUBE
(M0) (MG) (FT2) (DCF) DRY DRY DRY COEF
8.73 443.44 3.5 11.0 0.0 .850
u>
PORT-
POINT
E
E
E
E
E
E
••«.
E
E
-m
•E.
E
E
E
••'ft
E
E
E
-E
E
E
E
EV
E
1
1
2
2
3
3
4
4
5
5
6
6
6
6
5
5
4
. 4-
3
3
2
2
1
1
SAMP
TIME
(MIN)
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
METER
VOL
(DCF) (I
446.34
448.91
451.58
454.25
456.09
459.57
462.46
465.55
468.42
471.30
473.97
476.60
479.09
481.59
484.30
487.14
490.05
493,97
495.79
498.74
501.64
504.46
50*. 18
509.82
DELTA
P
• H20)
.470
.470
.520
.520
.470
.470
.500
.500
.520
.520
.450
.450
.400
.400
.510
.510
.570
.570
.510
.510
.520
.520
.450
.450
DELTA
H
(I.H20)
.930
.930
1.020
1.020
.930
.930
1*020
1.020
1.050
1.050
.910
.910
.810
.810
1.010
1.010
1.140
1.140
1.010
1.010
1.050
1.050
.910
.910
TEMP
IN
(D.F)
64.0
72.0
80.0
85.0
90.0
87.0
84.0
91.0
99.0
96.0
92.0
93.0
100.0
102.0
104.0
106.0
108.0
108.0
108.0
106.0
105.0
108.0
110.0
111.0
TEMP
OUT
(D.F*
62.0
62.0
63.0
64.0
65.0
66.0
68.0
69.0
70.0
71.0
72.0
73.0
74.0
75.0
77.0
78.0
79.0
79,0
78.0
79.0
80.0
81.0
82.0
83.0
TRAIN
VAC
(I.HG)
10.0
10.0
10.0
10.0
10.0
11.0
12.0
12.5
13.0
13.0
13.0
13.0
12.0
13.0
14.0
14.5
15.0
15.0
15.0
15.5
16.0
16.0
16*0
16.0
STACK
TEMP
(D.F)
195.0
195.0
195.0
195.0
195.0
195.0
195.0
195.0
180.0
180.0
180.0
180.0
180.0
180.0
185.0
185.0
185.0
185.0
185.0
185.0
180.0
180.0
180.0
180.0
BOX
TEMP
(D.F)
60.0
75.0
75.0
75.0
75.0
75.0
75.0
75.0
75.0
80.0
80.0
80.0
PROBE
T DIA
(IN)
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
.250
VEL
(FPM)
2712.6
2712.8
2853.5
2853.5
2712.8
2712.8
2798.1
2798.1
2820.6
2820.6
2623.9
2623.9
2473.8
2473.8
2804.2
2804.2
2964.6
2964.6
2804.2
2804.2
2820.6
2820.6
2623.9
2623.9
-------
EMISSION DATA
NAME DESCRIPTION UNITS
DATE OF RUN
ON PROBE TIP DIAMETER IN
tt NET TIME OF RUN MIN
PB BAROMETRIC PRESSURE IN.HG
PM AV6 ORIFICE PRES DROP IN.H20
VM VOL DRY GAS-METER COND DCF
TM AVG GAS METER TEMP DEG.F
VMSTD VOL DRY 6AS-STD COND DSCF
V* TOTAL H20 COLLECTED ML
VWV VOL H20 VAPOR-STD COND SCF
PMOS PERCENT MOISTURE BY VOL
MO MOLE FRACTION DRY GAS
RC02 PERCENT CQ2 BY VOLt DRY
IP02 PERCENT 02 BY VOL. DRY
PCO PERCENT CO BY VOL » DRY
PN2 PERCENT N2 BY VOL» DRY
HMD MOLECULAR WT-DRY STK GAS
Mt( MOLECULAR HT-STK GAS
CP PITOT TUBE COEFFICIENT
DPS AVG STK VELOCITY HEAD IN.H20
TS AVG STACK TEMPERATURE DEG.F
NP NET SAMPLING POINTS
PST STATIC PRES OF STACK IN.HG
PS STACK PRESSURE, ABSOLUTE IN.HG
VS AVG STACK GAS VELOCITY FPM
AS STACK AREA IN2
QS SfK FLOWRATEt DRY»STD CN DSCFM
OA ACTUAL STACK FLOWRATE ACFM
PfRl _FfRCENT ISDKINET1C
EA" PERCENT EXCESS'AIR !
1-1
02-19-74
.250
120.0
29.15
1.088
67.06
75.8
64.80
102.1
4.84
6.949
.931
11.0
3.5
0.0
85.5
29.90
29.07
.850
.420
309.3
24
-1.03
28.12
2737
1257
14398
23895
95.8
18. "4
1-0
02-19-74
.250
120.0
29.15
.789
58.93
74.8
57.01
300.5
14.24
19.989
.800
11.0
3.5
0.0
85.5
29.90
27.52
.850
.387
175.5
30
-1.03
28.12
2446
1257
13391
21352
90.6
18.4
2-1
02-20-74
.250
120.0
29.84
1.134
66.89
87.8
64.72
102.7
4.87
6.995
.930
11.0
3.5
0.0
85.5
29.90
29.07
.850
.447
290.8
24
-1.03
28.81
2756
1257
15210
24060
90.5
18.4
2-0
02-20-74
.250
120.0
29.84
.834
61.43
82.9
59.93
316.0
14.98
19.995
.600
11.0
3.5
0.0
85.5
29.90
27.52
.850
.413
181.7
24
-1.03
26.81
2515
1257
13971
21955
91.3
18.4
-------
EMISSION DATA
NAME
DN
TT
PB
PM
VN
TM
VMSTD
V»
VWV
PMOS
MD
PC02
P02
PCO
PN2
MttD
K%
CP
DPS
TS
MP
PST
PS
VS
AS
QS
QA
DESCRIPTION UNITS
DATE OF RUN
PROBE TIP DIAMETER IN
NET TIME OF RUN MIN
BAROMETRIC PRESSURE IN.HG
AVG ORIFICE PRES DROP IN.H20
VOL DRY GAS-METER COND DCF
AVG GAS METER TEMP DEG.F
VOL DRY GAS-STD COND DSCF
TOTAL H20 COLLECTED ML
VOL H20 VAPOR-STO COND SCF
PERCENT MOISTURE BY VOL
MOLE FRACTION DRY GAS
PERCENT C02 BY VOL* DRY
PERCENT 02 BY VOL. DRV
PERCENT CO BY VOL» DRY
PERCENT N2 BY VOL» DRY
MOLECULAR WT-DRY STK GAS
MOLECULAR WT-STK GAS
PITOT TUBE COEFFICIENT
AVG STK VELOCITY MEAD IN.H20
AV0 STACK TEMPERATURE DEG.F
NET SAMPLING POINTS
STATIC PRES OF STACK IN.HG
STACK PRESSURE, ABSOLUTE IN.HG
AVG STACK GAS VELOCITY FPM
STACK AREA IN2
STK FLOWRATE* DRY.STD CN DSCFM
ACTUAL STACK FLOWRATE ACFM
J50KINETJLC: ,
EA
PERCENT EXCESS AIR
3*1
02-20-74
.250
120.0
29.90
1.096
66.77
95.9
63.79
101.3
4.80
7.000
.930
11.0
3.5
0.0
85.5
29.90
29.07
.850
.426
299.2
24
-1.03
28.87
2704
1257
14789
23606
91.8
18.4
3-0
02-20-74
.250
120.0
29.90
.982
66.38
84.6
64.72
341.2
16.17
19.994
.800
11.0
3.5
0.0
85.5
29.90
27.52
.650
.491
186.3
24
-1.03
28.87
2752
1257
15211
24024
90.5
18.4
-------
EMISSION DATA
(METRIC RESULTS)
NAME DESCRIPTION
DATE OF RUN
ON PROBE TIP DIAMETER
TT NET TIME OF RUN
PB BAROMETRIC PRESSURE
PM AVG ORIFICE PRES DROP
VM VOL DRY GAS-METER COND
TM AVG GAS METER TEMP
VMSTM VOL DRY GAS-STD COND
V« TOTAL H2O COLLECTED
VWM VOL H20 VAPOR-STD COND
PMOS PERCENT MOISTURE BY VOL
MD MOLE FRACTION DRY GAS
PC02 PERCENT C02 BY VOL» DRY
P02 PERCENT 02 BY VOL* DRY
PCO PERCENT CO BY VOL* DRY
PNE PERCENT NZ BY VOL* DRY
HMD MOLECULAR WT-DRY STK GAS
MM MOLECULAR WT-STK GAS
CP PITOT TUBE COEFFICIENT
DPS AVG STK VELOCITY HEAD
TSM AVG STACK TEMPERATURE
NP NET SAMPLING POINTS
PST STATIC PRES OF STACK
PS STACK PRESSURE* ABSOLUTE
VSM AVG STACK GAS VELOCITY
AS STACK AREA
QSM STK FLOWRATE* DRY»STD CN
0AM ACTUAL STACK FLOURATE
PERI PERCENT ISDKINET1C
UNITS
IN
MIN
IN.HG
IN.H20
DCF
DEG.F
NCM
ML
NM3
IN.H20
DEG.C
IN.HG
IN.HG
M/MIN
IN2
NM3/MIN
M3/MIN
1-1
02-19-7*
.250
120.0
29.15
1 . 088
67.06
75.8
1.84
102.1
.14
6.949
.931
11.0
3.5
0.0
85.5
29.90
29.07
.850
.420
154.0
24
-1.03
28.12
834.4
1257
407.71
676.64
95*8
1-0
02-19-74
.250
120.0
29.15
.789
58.93
74.8
1.61
300.5
.40
19.989
.800
11.0
3.5
0.0
85.5
29.90
27.52
.850
.387
79.7
30
-1.03
28.12
745.6
1257
379.20
604.64
90.6
2-1
02-20-74
.250
120.0
29.84
1.134
66.89
87.8
1.83
102.7
.14
6.995
.930
11.0
3.5
0.0
85.5
29.90
29.07
.850
.447
143.8
24
-1.03
28.81
840.1
1257
430.70
681.32
90.5
2-0
02-20-74
.250
120.0
29.84
.834
61.43
82.9
1.70
316.0
.42
19.995
.800
11.0
3.5
0.0
85.5
29.90
27.52
.850
.413
83.1
24
-1.03
28.81
766.6
1257
395.61
621.71
91.3
-------
EMISSION DATA
(METRIC RESULTS)
NAME DESCRIPTION
DATE OF RUN
ON PROBE TIP DIAMETER
TT NET TIME OF RUN
PB BAROMETRIC PRESSURE
PM AVG ORIFICE PRES DROP
VM VOL DRY GAS-METER COND
TM AVG GAS METER TEMP
VMSTM VOL DRY GAS-STD COND
y« TOTAL H20 COLLECTED
VMM VOL H20 VAPOR-STD COND
PMOS PERCENT MOISTURE BY VOL
MD MOLE FRACTION DRY GAS
PC02 PERCENT C02 BY VOL* DRY
P02 PERCENT 02 BY VOL. DRY
PCO PERCENT CO BY VOL. DRY
PH8 PERCENT N2 BY VOLt DRY
MWD MOLECULAR MT-DRY STK GAS
Mil MOLECULAR WT-STK GAS
CP PITOT TUBE COEFFICIENT
DPS AVG STK VELOCITY HEAD
TSM AVG STACK TEMPERATURE
NP NET SAMPLING POINTS
PST STATIC PRES OF STACK
PS STACK PRESSURE. ABSOLUTE
VSM AVG STACK GAS VELOCITY
AS STACK AREA
OSM STK FLOWRATE. DRYfSTD CN
QAM ACTUAL STACK FLOWRATE
PERI PERCENT .ISOKINETIC
UNITS
IN
MIN
IN.HG
IN.H20
DCF
DEG.F
NCM
ML
NM3
IN.H20
DEG.C
IN.HG
IN.HG
M/MIN
IN2
NM3/MIN
M3/MIN
3-1
02-20-74
.250
120.0
29.90
1.096
66.77
95.9
1.81
101.3
.14
7.000
.930
11. 0
3.5
0.0
85.5
29.90
29.07
.650
.426
148.4
24
-1.03
28.87
824,3
1257
418.78
668.46
91.8
3-0
02^20-74
.250
120.0
29.90
.982
66.38
84.6
1.83
341.2
.46
19.994
.800
11.0
3.5
0.0
85.5
29.90
27.52
.850
.491
85.7
24
-1.03
28.87
838.9
1257
430.72
680.30
90.5
-------
AMAI YSTS DATA
oo
NAME
VM
TM
PM
VMSTD
QT
VT
VTB
N
VSOLN
VA
CS02
DESCRIPTION
DATE
PORT
POINT
SAMPLE
VOL OF DRY GAS-METER CN
AVG DRY GAS METER TEMP
AVfi ARS METER PRES
VOL OF DRY GAS-STD CN
STK FLOWRATEt DRYtSTD CN
VOL OF TITRANT-SAMPLE
VOL OF TITRANT-ABS BLANK
NORMAI ITY OF TTTRANT
TOTAL SOLUTION VOLUME
VOL SAMP ALIQUOT TITRD
CQNC OF SAMPLE-STD CN L
UNITS
CU.FT
DEG.R
IN.Hfi
CU.FT
DSCFM
ML
ML
G-FQ/L
ML
ML
fl/DSCF
PPM
L8/HR
GR/DSCF
GR/ACF
MG/NM3
KG/HR
1-1
02-19-74
S02 -
67.06
535.80
Zfl.12
64.80
14398.0
283.00
.10
.10050
230.0
40.0
1074.5
153.7
L.Z450
.8060
2849.0
69.69
02-19-74
s
1 S02 -2
67.06
535.80
64.80
14398.0
26.10
.10
_ -.11)050.
230.0
40.0
^o.aaoi635_
98.8
14.1
.1144
.0741
261.8
. . 16...A.1 -
1-T
02-19-74
s
H2S04'
67.06
535.80
64.80
14398.0
.40
.10
.10050
650.0
40.0
,00000082
1-0
02-19-74
W
S02 -1
58.93
534.80
57.01
13391.0
66.00
.10
T10050
290.0
40.0
.0000591ft ,
3.2 358.7
.7 47.7
.0057 .415ft
.0037
13.1
.3257
951.1
l-o
02-19-74
w
S02 -2
58.93
534.80
57.01
13391.0
1.63
.10
115.0
40.0
• 0 Q-Q 0 Ou.33 — «
3.3
.4
.0038
.0030
8.8
- .20.-:
1-0
02-19-74
W
H2S04
58.93
534.80
57.01
13391.0
.35
.10
.10050
365.0
40.0
* 1.7
.3
.0030
.0024
7.0
_ - -._. .16
-------
ANALYSTS DATA
NAME
\l»
TM
PM
VMSTD
QT
VT
VTB
N
VSOLN
VA
CS02
DESCRIPTION
DATE
PORT
POINT
SAMPLE
VOL OF DHY GAS-METER CN
AVG DRY GAS METER TEMP
AVG ABS METER PRES
VOL OF DRY GAS-STD CN
STK FLOWRATEt DRY,STD CN
VOL OF TITRANT-SAMPLE
VOL OF TITRANT-ABS BLANK
NORMALITY OF TITRANT
TOTAL SOLUTION VOLUME
VOL SAMP ALIQUOT TITRD
CONC OF SAMPLE-STD CN
UNITS
CU.FT
DEG.R
IN^Hfi
CU.FT
DSCFM
ML
ML
G-E.Q/L.
ML
ML
LB/DSCF
PPM
LB/HR
GR/D§£F
GR/ACF
MG/NM3
KG/HR
2-1
02-20-74
S
S02 -1
66.89
547.80
28. Bl
64.72
15210.0
322.00
.05
*JJL050
210.0
40.0
^0 001 85 04
1117.9
168.9
1.2953
.8802
2964 . 0
76,60
2-1
02-20-74
5
S02 -2
66.89
547.80
28.81
64.72
15210.0
426.00
.05
.10050
160.0
40.0
.00018652
1126.8
170.2
1.3057
.8873
2987.8
77.21
2-1
02-20-74
S
H2S04
66.89
547.80
28.81
64.72
15210.0
1.60
.10
.10050
560.0
40.0
.00000352 .
13.9
3.2
.0247
.0168
56.4
1.46
2-0
02-20-74
w
S02 -1
61.43
542.90
28.81
59.93
13971.0
8.20
.05
.10050
170.0
40.0
00000410
24.7
3.4
.0287
.0228
65.6
1 .56
2-0
02-20-74
y
S02 -2
61.43
542.90
28,81
59.93
13971.0
176.00
.05
.JJLa50_
215.0
40.0
.OOOUL8J
675.5
93.7
,7827
.6223
1791.0
42..51_
02-20-74
W
H2S04
61.43
542.90
28.81
59.93
13971.0
18.00
.05
.10050
390.0
40.0
...QOO 03 .1.7.0
125.1
26.6
__.2219
.1764
507.7
12.05
-------
AL-YSLS-DAIA
t-o
O
NAME
VM
TM
PM
VMSTD
QT
VT
VTB
N
VSOLN
VA
CS02
DESCRIPTION
DATE
PORT
POINT
SAMPLE
VOL OF DRY GAS-METER CN
AVG DRY GAS METER TEMP
AVG ARS MFTFR PRES
VOL OF DRY GAS-STD CN
STK FLOWRATE» DRY.STD CN
VOL OF TITRANT-SAMPLE
VOL OF TITRANT-ABS BLANK
NORMAI TTY OF TT.TRANT
TOTAL SOLUTION VOLUME
VOL SAMP ALIQUOT TITRD
CONG OF SAMPLE-STD CN {
UNITS
CU.FT
OEG.R
IN,HG
CU.FT
DSCFM
ML
ML
G-FQ/I
ML
ML
.B/DSCF
PPM
LB/HR
GR/DSCF -
GR/ACF
MG/NM3
KG/HR
3-1
02-20-74
S02 -1
66.77
555.90
?ft,fl7
63.79
14781.0
380.00
.04
.10050
270.0
40.0
1721.0
252.6
... L._9941_
1.3429
4563.1
114.59
3-T
02-20-74
s
S02 -2
66.77
555.90
?fl,A7
63.79
14781.0
31.00
.04
,10050
225.0
40.0
,00001934
116.9
17.2
.13*4
.0912
309.8
7.78
3-T
02-20-74
H2S04
66,77
555.90
?fl.ft7
63.79
14781.0
90.90
.04
.10050
440.0
40.0
,00017006
671.0
150.8
1.1904
.8017
2724.1
68.41
3-0
02-20-74
w
S02 -1
66.38
544.60
64.72
15211.0
70.00
.04
,100*0
200.0
40.0
,00003829
231.3
34.9
.2121
6.13.4
15.85
02-20-74
y
S02 -2
66.38
544.60
28.87
64.72
15211.0
7.00
.04
.100*0
200.0
40.0
. 000003ft!
23.0
3.5
.0267
.0211
61.0
1.58
3-0
02-20-74
H2S04
66.36
544.60
28.87
64.72
15211.0
6.00
.04
•1.0050
330.0
40.0
,J)Q 0.0.0 825
32.5
7.5
,0*77
.0457
132.1,
3.411
-------
APPENDIX B
SAMPLE CALCULATIONS
21
-------
EXAMPLE CALCULATIONS
1. VOLUME OF DRY GAS SAMPLED AT STANDARD CONDITIONS
17.71*VM«(PB * PM/13.b)
VMSTD *
TM*460.
17.71* 67.06*(29.1b* 1.068/13.6)
c •--.—.«—•«—•—-—--«•—•--—---- s
75.8*460.
VMSTM * VMSTD«0.028317= 64.80«0.028317=
2. VOLUME OF WATER VAPOR AT STANDARD CONDITIONS
VWV = 0.0474*VW « 0.0474* 102.1 =
VWM * VWV«0.028317 = 4.840*0.028317 =
3. PERCENT MOISTURE IN STACK GAS
100.»VWV 100.* 4.84
PMOS o • — * — *
VMSTD+VWV 64.eo* 4.8*
4. MOLE FRACTION OF DRY STACK GAS
100.-PMOS 100.- 6.949
MD » •««•««--•— s -.._.._..-___.. -c
100. 100.
5. AVERAGE MOLECULAR WEIGHT OF DRY STACK GAS
MWD » (PC02 « 44/100) * (P02 * 32/100)
*(PN2*PCO * 28/100)
.» (11.0 * 44/100) * ( 3.5 * 32/100)
+(85.5 » 28/100)
c
6. MOLECULAR WEIGHT OF STACK GAS
MW « MWD*MD + 18*(1-MD)
» 29.9» .931 + 18*(1- .931) »
S4.80 DSCF
1.84 ONH3
4.64 SCF
.1370 NM3
6.9*9 PERCENT
.931
29.90
29.07
22
-------
7. STACK GAS VELOCITY AT STACK CONDITIONS
VS
4360*AVG SQRT(DPS«)
4360* 17,952
»SQRT(1/<28.12«
VSH «• VS«0.3048 •
29.07))
2737*0.3048
2737 FPM
834 METERS/MIN
8. STACK GAS VOLUMETRIC FLOW AT STANDARD CONDITIONS* DRY BASIS
0.123*VS*AS»MO»PS
OS B ....... .....
TS*460
0.123* 2737* 1257* .931*28.12
309.3 +460
= 14398 DSCFM
OSM « QS*0.028317 » 14398*0.028317 '» 407.71 NM3/MIN
9. STACK GAS VOLUMETRIC FLOW AT STACK CONDITIONS
OS * »VMSTO
PERI »•• —
VS*TT»PS*MD*(DN*DN)
1032»( 309.3*460)* 64.80
a . ...... ... . a 95.8 PERCENT
2737* 120.0*28.12* .931* .250
* .250
23
-------
11. PERCENT EXCESS AIR AT SAMPLING POINT
100. •
-------
1. Concentration of Sulfur Dioxide at Standard Conditions
CS02 = (0.0000705) RvT-VTB) (N) (VSOLN/VA)]
L VMSTD J
230
[(26.10-0.10) (0.1005) -7^
(0.0000705)
64.8
= 0.00001635 Ib/dscf
CPPM = (387) (CS02) (1.000.000)
64.06
B (387) (16.35)
64.06
= 98.8 ppm
2. Concentration of H2S04 Mist at Standard Conditions
-1
• ["(VT-VTB) (N) (VSOLN/VA)
CH2S04 = (0.000108) -
CPPM
VMSTD
"(0.40-0.10) (0.1005)
(0.000108)
L 64.8
0.00000082 Ib/dscf
(387) (CH2S04) (1.000,000)
98.08
_ (387) (0.82)
98.08
=3.2 ppm
25
-------
APPENDIX C
FIELD DATA SHEETS
26
-------
MIDWEST RESEARCH INSTITUTE
RUN I—*
MRI Project Number "5^7^ ~ C& \^
Field Dates
Plant
Sampling Location ^^/riAbbgr. "^X^Ve. f"
Sampling Date |c> f
Testing Engineer 1 /yfcy/^^ //
Engr. Technician 1
3_
Lab Technician 1
Process Engineer 1
2.
Other 1
FIELD CREW
i1
Crew Chief
MRI - Form PO (10/72) 2?
-------
TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
Vn
PLANT __
DATE Jj
SAMPLING LOCATION
INSIDE OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A) _
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B) _
STACK I.D., (DISTANCE A - DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE _
CALCULATOR.
<\Q"
SCHEMATIC OF SAMPLING LOCATION
TRAVERSE
POINT
NUMBER
(
z
5
1
6
Co
FRACTION
OF STACK I.D.
STACK I.D.
PRODUCT OF
COLUMNS 2 AND 3
(TO NEAREST 1/8 INCH)
H
5?
HI
3?>4
w&
la 4
DISTANCE B
^>6
TRAVERSE POINT LOCATION
FROM OUTSIDE OF NIPPLE
(SUM OF COLUMNS 4 & 5)
\&£ "7^
HN* // \
2*% IVfc
^^ W i
*CZ^\ ^^
<\t*rl 41±
V
EPA (Dur) 232
4/72 •
28
-------
PRELIMINARY VELOCITY TRAVERSE ,
PLANT jkatJAee VovA^er-
DATE |<3 l-e ^ "7^
LOCATION ^nA^ttf*- - ^Via.'V-
STACK I.D. 1o"
BAROMETRIC PRES
STACK GAUGE PRE
OPERATORS WAi
SURE in. Hp ^29'/"!>
SSURE. in. H-,0 ~" W . O
t
TRAVERSE
POINT
NUMBER
l-l
1_
•^
A
^
G
AVERAGE
VELOCITY
HEAD
(Aps),in.H20
.%£•
^T)
• *\v
At
A(s
A(s
v\ \
40
A*
STACK
TEMPERATURE
(Ts), 8F
3\^
*)1~L
*>1~l
*5~l~^
^~L\
*>1L\
t'R^
^to
"5^
EPA (Our) 233
4/72
SCHEMATIC OF TRAVERSE POINT LAYOUT
TRAVERSE
POINT
NUMBER
AVERAGE
VELOCITY
HEAD
(Aps), in.H20
STACK
TEMPERATURE
(Ts), °F
t-i. -
29
-------
_ MIDWEST RESEARCH INSTITUTE
Run Number [ - 1 PRELIMINARY Recorded by
Date /<=? 7^«lb 7*f MOISTURE DETERMINATION Assisted by
.A.
NOTE: Same as Run No.
Condensor and/or Silica Gel Method
Barometric Pressure, Pg =
D Barometer Location
Reading Time
Q Elevation
in. Hg
by
Final
Initial
Difference
Clock
Time
Dry Gas
Meter
Reading(cf)
Vm =
Flowmeter
Setting
Dry Gas
Meter
Temp (°F)
Impinger
Water Volume
(ml)
Wc =
Tube No.
Weight (Grams)
Final
Initial
Total Moisture Adsorbed'.
Di fference
Wa =
Meter Pressure, Pg ** Pm
Average Meter Temperature, Tm
Total Weight of Moisture
Collected, We + Wa = Wm
in. Hg
OF
Moisture Content =
100
gm
% by Volume
I + 375
PmVm
(Tm+460) Wm
B. Wet/Dry Bulb Method
Dry Bulb Temperature
Wet Bulb Temperature
Moisture Content (from Ref. Table)
C. Predetermined Value
% Moisture /
°F
°F
% by Volume
Basis
MRI - Form P4 (10/72)
30
-------
NOMOGRAPH DATA
I IsO
PLANT.
DATE_
SAMPLING LOCATION
t/ 6 r"Vt fc> C?
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE IVIETER TEMPERATURE (AMBIENT + 20 °F),°F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hg
STATIC PRESSURE IN STACK, in. Hg
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE VELOCITY HEAD, in. H20
MAXIMUM VELOCITY HEAD, in. H20
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap, in. H20
AH@
T|navg.
Bwo
V
ps
PVP
/rm
savg.
APavg.
APmax.
I,M
10
1
29,1^
-Wu1
\°>(^
^0
AO
4 1/
, vz
,rc)
.75
w
EPA (Our) 234
4/72
31
-------
DRY MOLECULAR WEIGHT DETERMINATION
PLANT.
DATE
V;
COMMENTS:
SAMPLING TIME (24-hr CLOCK).
SAMPLING LOCATION
SAMPLE TYPE (BAG, INTEGRATED, CONTINUOUS).
ANALYTICAL METHOD
AMBIENT TEMPERATURE ,
OPERATOR
\^ RUN
GAS ^^\
C02
02 (NET IS ACTUAL 02
READING MINUS ACTUAL
C02 READING)
CO(NET IS ACTUAL CO
READING MINUS ACTUAL
02 READING)
N£ (NET IS 100 MINUS
ACTUAL CO READING)
1
.ACTUAL
READING
NET
2
ACTUAL
READING
NET
3
ACTUAL
READING
NET
AVERAGE
NET
VOLUME
Vi
MULTIPLIER
44/100
1 ~
32/100
. i
a/ioo
a/MO
MOLECULAR WEIGHT OF
STACK GAS (DRY BASIS)
Md, Ib/lb-mole
TOTAL
CO
ro
EPA (Dur) 230
4/72
-------
FIELD DATA
u>
TRAVERSE
POINT
NUMBER
•5-1
~
•
A
I
1
,2
^
*M
/9
^
4
5
*f
£,
to
PLANT ^/K«LiM**» KX-UO-
DATE K9 T=eb ~K
SAMPLING Lf
SAMPLE TYP
RUN NUMBEF
OPERATOR
AMBIENT TEI
BAROMETRIC
STATIC PRE
FILTER HUM
\. CLOCK TIME
75 — — -J332
&*>**>
TCATION 5^-J-lxkbor- J/V leT
F t>0^
j-T
Ad A.
MPFRATURF *\.*59
PRFSSURF "Zl^D. l<3
.SURF (P i — /4.O
RFR U)
PROBE LENGTH AND TYPE J ~4r*TC* &L4S>
NOZZLE ID I 2.
ASSUMED MC
SAMPLE BO
METER BOX
METER AHS
C FACTOR
^* /
1ISTURF «. ~7
K NUMBER II
NUMBER ^>
,e^T_
PROBE HEATER SETTING
HEATER BOX SETTING
SCHEMATIC OF TRAVERSE P
READ AND RECORD ALL DATA EVERY
GAS METER READING
(V ) fp
*"1CT Q. *^ ^L
I ^ C7* 1 »«
"lkO(r
Tip^.^^
"7(^« ^T
ifc^^-j
liz..^
T~lfl",^2,
• l™7 .^ j^l
Tfipi tV^
•7^3.^1
")^.33)
7^.20)
"107.7^
VELOCITY
HEAD
(ApJ, in. HiO
•"55
• V/
,^^H
^<5
A \
•Ml
^1 ^
f\^7
4v
' ^-=>
^j C^.
£\ T
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED
,91
•93
i,i^
/.ic/
!.
i.oa
/.o<9
Lo<)
(>(5
'vi*5
/.ra
l-'Z-l
ACTUAL
DINT LAYOUT
S MINIIT
STACK
TEMPERATURE
(TS).°F
5tZo
Siu»
^i<5
5l^4
3\u»
31**
^ It
5l^\
^HS
Sv5
(
REFERENCE
ES
_|
^*:>
^^//P
£^ *1
^&
"5
51
<^Z.
^"5
64
(*&
G?l
O B
PUMP
VACUUM.
in. Hg
&
g
s
9
«^
?,*5
^)iS
«^^
1^
f«?
M
II
SAMPLE BOX
TEMPERATURE.
°F
3."5o
*3. t*l
J?*51
-2"^H
5lo
2^o
2 VA
Z3o
21-3
,2<5«5
-?&J
^d3
IMPINGER
TEMPERATURE.
°F
Ceo
G»S
TD
COMMENTS:
EPA (Dur> 235
4 72
-------
TRAVERSE
POINT
NUMBER
GAS METER READING
VELOCITY
HEAD
api in. H0
ORIFICE PRESSURE
DIFFERENTIAL
lAHi. in H^O)
DESIRED ACTUAL
STACK
TEMPERATURE
iT$i.0F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in HI
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE
°F
01
S.5
IS
8/ 1 » 65
. a.
&
,6
EPA (Dur) 236
472
-------
MIDWEST RESEARCH INSTITUTE
MRI Project Number
Field Dotes
Sompling Location
Sampling Date \c>>
Crew Chief
Testing Engineer 1
l_
3
Engr. Technician 1
2_
3
Lob Technician
2_
3
Process Engineer J_
2
Other ]_
2
RUN
FIELD CREW
\
MRI - Form PO (10/72)
35
-------
TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
PLANT
DATE . /9
SAMPLING LOCATION
INSIDE OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A) _
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B) _
STACK I.D., (DISTANCE A - DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
CALCULATOR.
-7
SCHEMATIC OF SAMPLING LOCATION
TRAVERSE
POINT
NUMBER
1
z
3
1
1
(/
FRACTION
OF STACK I.D.
,044
i/n
,Z^5
ao-5T
• 6-53
,0^
STACK I.D.
^lo"
PRODUCT OF
COLUMNS 2 AND 3
(TO NEAREST 1/8 INCH)
\^ \\
^•66 ^ 5
ll.&o /li
Zg.eo *?&i
M.lt VI -i
3&.Z^ ^25
DISTANCE B
fri
TRAVERSE POINT LOCATION
FROM OUTSIDE OF NIPPLE
(SUM OF COLUMNS 4 & 5)
IcM
14*
201
^G?^
4Zt
^1(^1
•'
EPA (Dur) 232
4/72
36
-------
PRELIMINARY VELOCITY TRAVERSE
PLANT _J
DATE «2
LOCATION
STACK I.D..
BAROMETRIC PRESSURE, in. Hg.
STACK GAUGE PRESSURE, in. H,0.
OPERATORS.
SCHEMATIC OF TRAVERSE POINT LAYOUT
TRAVERSE
POINT
NUMBER
i .
^
,
4
r
' £'
• . •
AVERAGE
VELOCITY
HEAD
(Aps), in.^O
' 3 (?
3> )
< "^ "7
. c;
r?
, C/v
• y 3
STACK
TEMPERATURE
. °F
^J^
EPA (Out) 233
4/72
TRAVERSE
POINT
NUMBER
AVERAGE
VELOCITY
HEAD
(Aps), in.H20
STACK
TEMPERATURE
(TS). °F
37
-------
Run Number
Dote JO)
MIDWEST RESEARCH INSTITUTE
PRELIMINARY Recorded by
MOISTURE DETERMINATION Assisted by
.A.
NOTE; Same as Run No.
Condenser and/or Silica Gel Method
Barometric Pressure, Pg =
D Barometer Location
Reading Time
P Elevation
in. Hg
by
Final
Initial
Difference
Clock
Time
Dry Gas
Meter
Reading(cf)
Vm =
Flowmeter
Setting
Dry Gas
Meter
Temp(°F)
Impinger
Water Volume
(ml)
Wc =
Tube No.
Weight (Grams)
Fi na 1
Initial
Total Moisture Adsorbed'
Difference
Wa =
Meter Pressure, Pg "*& Pm
Average Meter Temperature, Tm
Total Weight of Moisture
Collected, We + Wa = Wm
in. Hg
OF
Moisture Content =
JOO
gm
% by Volume
I + 375
PmVm
(Tm+460) Wm
B. Wet/Dry Bulb Method
Dry Bulb Temperature :
Wet Bulb Temperature :
Moisture Content (from Ref. Table)
C. Predetermined Value
% Moisture AQ [t) Basis
°F
'°F
% by Volume
iL ^i?X
MRI - Form P4 (10/72)
38
-------
PLANT
DATE
s\<
SAMPLING LOCATION
NOMOGRAPH DATA
*0
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in; H20
AVERAGE METER TEMPERATURE (AMBIENT + 20°F),°F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hg
STATIC PRESSURE IN STACK, in. Hg
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE VELOCITY HEAD, in. H20
MAXIMUM VELOCITY HEAD, in. H20
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap, in. H20
AH@
T|navg.
Bwo
Pm
ps
V
/rm
savg.
APavg.
APmax.
!>?<•/
o
70
^,0 %
^~S? £2 a
'• 1 £-
•*-£-&&.
i>
-------
DRY MOLECULAR WEIGHT DETERMINATION
PLANT.
DATE_
COMMENTS:
7*1
SAMPLING TIME (24-hr CLOCK).
SAMPLING LOCATION
SAMPLE TYPE (BAG, INTEGRATED, CONTINUOUS).
ANALYTICAL METHOD
AMBIENT TEMPERATURE
OPERATOR
^^ RUN
GAS ^^\
C02
02(NET IS ACTUAL 02
READING MINUS ACTUAL
C02 READING)
CO(NET IS ACTUAL CO
READING MINUS ACTUAL
02 READING)
N 2 (NET IS 100 MINUS
ACTUAL CO READING)
1
ACTUAL
READING
NET
2
ACTUAL
READING
NET
3
ACTUAL
READING
NET
AVERAGE
NET
VOLUME
3-5
O.o
MULTIPLIER
44/100
!
32/100
a/ioo
a/ioo
MOLECULAR WEIGHT OF
STACK GAS (DRY BASIS)
Md, Ib/lb-mole
TOTAL
EPA (Dur) 230
4/72
-------
75 9,
FIELD DATA
PLAHT
DATE
SAMPLING LOCATION _^=^
SAMPLE TYPE .
RUN NUMBER _
OPERATOR
PROBE LENGTH AND TYPE
NOZZLE I.D. ' l.,,\-~''
ASSUMED MOISTURE.'.
SAMPLE BOX NUMBER
METER BOX NUMBER
METER
) "
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE _
STATIC PRESSURE, (P^) —
FILTER NUMBER (s)
"g-
CFACTOR.
PROBE HEATER SETTING.
HEATER BOX SETTING
REFERENCE Ap
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA FVFRY *5 MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(V). It3
VELOCITY
HEAD
Ups). in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
STACK
TEMPERATURE
(T$)."F
DRY GAS METER
TEMPERATURE
INLET
OUTLET
PUMP
VACUUM.
in. Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
, •) / .
10
If
-^
XL
^ -
•$><-
. ? 6
0-
/3
i <-/ •
/"
Sol
0.7 3
6 ~
ITL
>
17.
CT"
V
D . S i~>
.
3?/ <7
-------
N3
TRAVERSE
POINT
NUMBER
"*
^L
/
«
\. CLOCK TIME
^'^XcScK,
TIME, mm N^
— ' _
^
£J
£/
t,
<-/
f-i
<-/
£y
<-/
<-/
GAS METER READING
'V «3.
1 7 /?• p. -7
"i V? / /
•j, <_/ ^ . / 3
3x->. //?
-? <,-; «7c"
7 j-c^- . ^^
> c-y» * ^ . in H^Oi
DESIRED
tf, 7 ^
^ i^'?
/^7/
ACTUAL
STACK
TEMPERATURE
iTsi.°F
17 !
^7
^
^>^
c^^>
«¥ LS
O-5'
PUMP
VACUUM.
in H|
M
i*7
•* o
21
*-3
3.^
2."^
^ 3
^%
3^
SAMPLE BOX
TEMPERATURE.
°F
&0
?S)
r c~
IMPINCER
TEMPERATURE
°F
-
EPA (Dm) 236
472
-------
MIDWEST RESEARCH INSTITUTE
MRI Project Number
Field Dat
Plant
Sampling Location
Sampling Date ^
Crew Chief
Testing Engineer 1
Engr. Technician 1_
Lab Technician
Process Engineer 1
2
Other 1
RUN
FjELDCREW
MRI - FormPO (10/72)
43
-------
NOMOGRAPH DATA
PLANT
DATE_
SAMPLING LOCATION
r-7
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE (AMBIENT + 20 °F),°F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hg
STATIC PRESSURE IN STACK, in. Hg
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE VELOCITY HEAD, in. H20
MAXIMUM VELOCITY HEAD, in. H20
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap. in. H20
AH@
Tmavg.
Bwo
Pn,
ps
Ps/Pm
savg.
APavg.
APmax.
EPA (Dur) 234
4/72
44
-------
PLANT.
JX&
V:
DRY MOLECULAR WEIGHT DETERMINATION
COMMENTS:
SAMPLING TIME (24-hr CLOCK).
SAMPLING LOCATION
SAMPLE TYPE (BAG, INTEGRATED, CONTINUOUS).
ANALYTICAL METHOD
AMBIENT TEMPERATURE
OPERATOR
\^ RUN
GAS ^"\^
C02
O£(NET is ACTUAL o2
READING MINUS ACTUAL
C02 READING)
CO(NET IS ACTUAL CO
READING MINUS ACTUAL
02 READING)
^2 (NET IS 100 MINUS
ACTUAL CO READING)
1
ACTUAL
READING
NET
2
ACTUAL
READING
NET
3
ACTUAL
READING
NET
AVERAGE
NET
VOLUME
3.5
0,-a
MULTIPLIER
44/100
I:
32/100
_ i
a/ioo
^/lOO
MOLECULAR WEIGHT OF
STACK GAS (DRY BASIS)
Md, Ib/lb-mole
TOTAL
Ui
EPA (Dur) 230
4/72
-------
yjyt^/wtuc
FIELD DATA
PLANT.
DATE
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER.
OPERATOR _£
PROBE LENGTH AND TYPE
NOZZLE 1.0.
rr
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE, (Ps) __T_
FILTER NUMBER Is)
ASSUMED MOISTURE.'. i
SAMPLE BOX NUMBER A Z-
METER BOX NUMBER "b
METER AHg
C FACTOR
PROBE HEATER SETTING.
HEATER BOX SETTING
REFERENCE An
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA EVERY
MINUTES
TRAVERSE
POINT
NUMBER
SAMPLING 1
TIME.min
CLOCK TIME
2h'
GAS METER READING
og. it3
VELOCITY
HEAD
(APS), in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
STACK
TEMPERATURE
(TS).°F
DRY GAS METER
TEMPERATURE
INLET
(To, jn),°F
OUTLET
PUMP
VACUUM.
in. Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
"F
.37
1(7
1.12,
'S
1.1
(0(7
141
I.Z.S
(oz.
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(6
l.c?
COMMENTS:
EPA (Our) 235
472
U
-------
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i.o
I.C5
f/x 0..4-
1,5 21)
270
63
23-7
«> 3
-------
MIDWEST RESEARCH INSTITUTE
MRI Project Number
Field Dotes
Plant :3
& r^, t -e
Sampling Location /^)JJ
Sampling Date ^L
Crew Chief
Testing Engineer 1
Lab Technician
Process Engineer 1
Other
J_
2
Engr. Technician 1 l^hi I
FIELD CREW
MRI - Form PO (10/72)
' 48
-------
NOMOGRAPH DATA
PLANT.
DATE_
SAMPLING LOCATION
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE (AMBIENT + 20°F),°F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hg
STATIC PRESSURE IN STACK, in. Hg
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE VELOCITY HEAD, in. H20
MAXIMUM VELOCITY HEAD, in. H20
C FACTOR '
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap, in. H20
AH@ •
T|t1avg.
Bwo
rm
PS :'
PS/Pm '
savg.
^Pavg.
^Pniax.
EPA (Our) 234
4/72
49
-------
PLANT.
DATE.
DRY MOLECULAR WEIGHT DETERMINATION
COMMENTS:
SAMPLING TIME (24-hr CLOCK).
SAMPLING LOCATION.
SAMPLE TYPE (BAG, INTEGRATED, CONTINUOUS).
ANALYTICAL METHOD _-
AMBIENT TEMPERATURE :
OPERATOR
\^ RUN
GAS ^\^
C02
02(NET IS ACTUAL 02
READING MINUS ACTUAL
C02 READING)
CO(NET IS ACTUAL CO
READING MINUS ACTUAL
02 READING)
N£ (NET IS 100 MINUS
ACTUAL CO READING)
1
ACTUAL
READING
NET
2
ACTUAL
READING
NET
3
ACTUAL
READING
NET
AVERAGE
NET
VOLUME
^
-
MULTIPLIER
44/100
1
32/100
^/lOO
K/m
MOLECULAR WEIGHT OF
STACK GAS (DRY BASIS)
Md, Ib/lb-mole
TOTAL
Ln
O
EPA (Dur) 230
4/72
-------
FIELD DATA
PLANT 2> na^^tf
DATE _? /JL*/ Tt,/
SAMPLING LOCATION ,-„ ,«-/ W
SAMPLE TYP
RUN NUMBER
OPERATOR
F 7Q*,
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AMBIENT TEMPERATURE **&
TRAVERSE
POINT
NUMBER
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1
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PROBE LEN
NOZZLE I.D
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NUMBER
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NUMBER
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VELOCITY
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ORIFICE PRESSURE
DIFFERENTIAL
(AH), in H^Oi
DESIRED
*..°F
stc
3>o
PUMP
VACUUM.
in H|
iV
\\
SAKtEBOX
TEMPERATURE.
<.—
-
EPA (Dur) 236
4/72
-------
MIDWEST RESEARCH INSTITUTE
MRI Project Number
Field Dates
Plant
^f
Testing Engineer 1 /^/<
Engr. Technician 1
Lab Technician 1
Process Engineer 1
Other 1
2
RUN ,—
Sampling Location
Sampling Date £2.o'7^^ fe,"-?
FIELD CREW
Crew Chief
MRI - Form PO (10/72)
53
-------
PLANT
DATE_
""
NOMOGRAPH DATA
SAMPLING LOCATION
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE (AMBIENT + 20°F), °F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hg
STATIC PRESSURE IN STACK, in. Hg
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE VELOCITY HEAD, in. H20
MAXIMUM VELOCITY HEAD, in. H20
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap, in. H20
AH@
Tmavg.
Bwo
pm
Ps
V
/rm
savg.
A.Pavg.
APmax.
EPA (Dur) 234
4/72
54
-------
DRY MOLECULAR WEIGHT DETERMINATION
PLANT.
DATE.
COMMENTS:
SAMPLING TIME (24-hr CLOCK).
SAMPLING LOCATION
SAMPLE TYPE (BAG, INTEGRATED, CONTINUOUS).
ANALYTICAL METHOD
AMBIENT TEMPERATURE
OPERATOR
^. RUN
GAS ^\
C02
02 (NET IS ACTUAL 02
READING MINUS ACTUAL
C02 READING)
CO(NET IS ACTUAL CO
READING MINUS ACTUAL
02 READING)
N£ (NET IS 100 MINUS
ACTUAL CO READING)
1
ACTUAL
READING
..
NET
2
ACTUAL
READING
NET
3
ACTUAL
READING
NET
AVERAGE
NET
VOLUME
S
4) *?
• v
MULTIPLIER
44/100
f
32/100
_ _ 1
a/iob
a/wo
MOLECULAR WEIGHT OF
STACK GAS (DRY BASIS)
Mj, Ib/lb-mole
-
TOTAL
Ln
Ui
EPA (Dur) 230
4/72
-------
PLANT.
DATE'_
FIELD DATA
TH
PROBE LENGTH AND TYPE
NOZZLE I.D i 2
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
OPERATOR
AMBIENT TEMPERATURE *? •?
BAROMETRIC PRESSURE
STATIC PRESSURE. (Pj^-
FILTER NUMBER (s)
ASSUMED MOISTURE.'. _
SAMPLE BOX NUMBER _
METER BOX NUMBER "b
METER AHg i . *
C FACTOR '_ . O
72-
PROBE HEATER SETTING.
HEATER BOX SETTING
REFERENCE ap (_
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(Vm). 1(3
VELOCITY
HEAD
IAps). in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
STACK
TEMPERATURE
-------
TRAVERSE
POINT
NUMBER
TIME
INLET
OUTLET
CLOCK TIME
GAS METER REAOING
'V ^
VELOCITY
HEAD
ORIFICE PRESSURE
DIFFERENTIAL
IAH). in HOi
STACK
TEMPERATURE
lT$i.°F
DRY GAS METER
TEMPERATURE
PUMP
VACUUM.
in HS
SAMPLE BOX
TEMPERATURE.
•F
IMPINGER
TEMPERATURE
°F
loB
MT
r/c
EPA (Dur) 236
472
,<
-------
MIDWEST RESEARCH INSTITUTE
MRI Project Number
Field Dates
Plant
cj
Sampling Location^
Sampling Date
Crew Chief
Testing Engineer 1
2
3
Engr. Technician 1
2
3
Lab Technician
2.
3
Process Engineer 1
2~
Other ]_
2
RUN
FIELDCREW
MRI - Form PO (10/72)
58
-------
PLANT
NOMOGRAPH DATA
DATE.
SAMPLING LOCATION
/
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE (AMBIENT + 20 °F),°F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in. Hg
STATIC PRESSURE IN STACK, in. Hg
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE VELOCITY HEAD, in. H20
MAXIMUM VELOCITY HEAD, in. H20
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap, in. H20
AH@
Tmavg.
Bwo
Pm
ps
Ps/Pm
savg.
*Pavg.
APmax.
EPA (Our) 234
4/72
59
-------
DRY MOLECULAR WEIGHT DETERMINATION
COMMENTS:
SAMPLING TIME (24-hr CLOCK).
SAMPLING LOCATION
SAMPLE TYPE (BAG, INTEGRATED, CONTINUOUS).
ANALYTICAL METHOD
AMBIENT TEMPERATURE
OPERATOR '
U(j
\«. RUN
GAS >\
C02
02(NET IS ACTUAL 02
READING MINUS ACTUAL
C02 READING)
CO (NET IS ACTUAL CO
READING MINUS ACTUAL
02 READING)
N 2 (NET IS 100 MINUS
ACTUAL CO READING)
1
ACTUAL
READING
NET
2
ACTUAL
READING
NET
3
ACTUAL
READING
NET
AVERAGE
NET
VOLUME
\f
MULTIPLIER
44/100
i "
32/100
— — 1
a/100
a/wo
MOLECULAR WEIGHT OF
STACK GAS (DRY BASIS)
Md, Ib/lb-mole
TOTAL
EPA (Dur) 230
4/72
-------
TRAVERSE
POINT
NUMBER
GAS METER READING
3
Ll
VELOCITY
HEAD
tilpjl in. HjO
ORIFICE PRESSURE
DIFFERENTIAL
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DESIRED ACTUAL
STACK
TEMPERATURE
(T$I.°F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in H|
i£-
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
c
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