United States
Environmental Protection
Agency
Office of Air Quality
Planning and Standards
Research Triangle Park NC 27711
EMB Report 79-MET-1
December 1979
Air
Metallic Minerals
Emission Test Report
Exxon
Casper, Wyoming
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EXXON MINERALS COMPANY, U.S.A.
CONVERSE COUNTY, WYOMING
PROCESS ORE SAMPLES - ANALYTICAL RESULTS
Sample Description
Percent Moisture
Percent Sol ids
Conveyor from Fine Ore Bins
Conveyor Leading to the Crusher
Conveyor Leaving the Crusher
Conveyor Leaving the Screening
Set #2 Conveyor from Screen to
Fine Ore Bin
Set #2 Conveyor Leading from
the Fine Ore Bin
Set #2 Conveyor Leaving Primary
Crusher
Set #2 Conveyor Leading to the
4.99
5.13
5.62
5.73
5.57
6.07
5.66
5.90
95.01
94.87
94.38
94.27
94.43
93.93
94.34
94.10
Crusher
-------
Source Emissions Test Report
Exxon Minerals Company, U.S.A.
Converse County, Wyoming
Primary Crusher, Fine Ore Bins
and Dryer Scrubbers
p. O'fLu/Jb
JeffreyCD. O'Neill
Project Scientist
Barry
Supervisor Air Testing
RFW Report No. 0300-81-11
Contract No. 68-02-2816
Work Assignment No. 10
Prepared by
Weston Designers-Consultants
West Chester, Pennsylvania 19380
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TABLE OF CONTENTS
LIST OF TABLES v
LIST OF FIGURES viii
SUMMARY 1
INTRODUCTION - 5
PROCESS DESCRIPTION . 9
DESCRIPTION OF TEST LOCATIONS 15
Crusher Transfer Point Exhaust Duct 15
Crusher Scrubber Inlet Duct 15
Crusher-Grizzley Exhaust Duct 15
Crusher Scrubber Outlet Duct 15
Fine. Ore Bins Hopper Exhaust Duct 15
Fine Ore Bins Scrubber Inlet Duct 16
Fine Ore Bins Scrubber Outlet Duct 16
Packaging Area Exhaust Duct 16
Dryer Scrubber Outlet Duct 16
Dryer Scrubber Inlet Duct 16
DESCRIPTION OF SAMPLING TRAINS 27
Particulate Sampling Trains 27
Particle Size Distribution Sampling Apparatus 27
TEST PROCEDURES 33
Preliminary Tests 33
Crusher Transfer Point Exhaust Duct 33
Crusher Scrubber Inlet Duct 3^
Crusher-Grizzley Exhaust Duct 3^
Crusher Scrubber Outlet Duct 3^
Fine Ore Bins Scrubber Outlet Duct 3^
Fine Ore Bins Scrubber Inlet Duct 35
Fine Ore Bins Hopper Exhaust Duct 35
Dryer Scrubber Inlet Duct 35
Dryer Scrubber Outlet Duct 36
Packaging Area Exhaust Duct 3°
ANALYTICAL PROCEDURES 37
Particulate Sample Recovery 37
Particulate Analyses 37
Particle Size Sample Recovery and Analyses 38
Trace Element Analysis of Particulate Sample 39
i i i
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TABLE OF CONTENTS
(continued)
Page
DISCUSSION OF TEST RESULTS *»3
APPENDIX A — Raw Test Data A-1
APPENDIX B — Laboratory Reports B-1
APPENDIX C — Sample Calculations C-1
APPENDIX D -- Equipment Calibration Data D-1
APPENDIX E — Project Participants E-1
IV
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LIST OF TABLES
Table No. Title
1 Crusher Transfer Point Exhaust Duct
Summary of Test Data ^5
2 Crusher Scrubber Inlet Duct
Summary of Test Data i£
3 Crusher-Grizzley Exhaust Duct
Summary of Test Data ^
k Crusher Scrubber Outlet Duct
Summary of Test Data i^g
5 Fine Ore Bins Scrubber Outlet Duct
Summary of Test Data 49
6 Fine Ore Bins Scrubber Inlet Duct
Summary of Test Data 59
7 Fine Ore Bins Hopper Exhaust Duct
Summary of Test Data 51
8 Dryer Scrubber Inlet Duct•
Summary of Test Data 52
9 Dryer Scrubber Outlet Duct
Summary of Test Data 53
10 Packaging Area Exhaust Duct
Summary of Test Data 5^
11 Crusher Transfer Point Exhaust Duct
Summary of Test Results 55
12 Crusher Scrubber Inlet Duct
Summary of Test Results 56
13 Crusher-Grizzley Exhaust Duct
Summary of Test Results 57
1^ Crusher Scrubber Outlet Duct
Summary of Test Results 58
15 Fine Ore Bins Scrubber Outlet Duct
Summary of Test Results 59
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LIST OF TABLES
(continued)
Table No. Title Page
16 Fine Ore Bins Scrubber Inlet Duct
Summary of Test Results 60
17 Fine Ore Bins Hopper Exhaust Duct
Summary of Test Results 61
18 Dryer Scrubber Inlet Duct
Summary of Test Results 62
19 Dryer Scrubber Outlet Duct
Summary of Test Results 53
20 Packaging Area Exhaust Duct
Summary of Test Results 6k
21, 22, 23 Crusher Transfer Point Exhaust Duct
Particle Size Distribution Runs 1, 2, 3 65
24, 25,.26 Crusher Scrubber Inlet Duct
Particle Size Distribution Runs 1, 2, 3 71
27 Crusher Scrubber Outlet Duct
Particle Size Distribution Run 1 77
28, 29, 30 Crusher-Grizzley Exhaust Duct
Particle Size Distribution Runs 1, 2, 3 79
31 Fine Ore Bins Scrubber Outlet Duct
Particle Size Distribution Run 1 85
32, 33, 3** Fine Ore Bins Scrubber Inlet Duct
Particle Size Distribution Runs 1, 2, 3 87
35, 36, 37 Fine Ore Bins Hopper Exhaust Duct
Particle Size Distribution Runs 1, 2, 3 93
38 Dryer Scrubber Outlet Duct
Particle Size Distribution Run 1 99
39, 40, 41 Dryer Scrubber Inlet Duct
Particle Size Distribution Runs 1, 2, 3 101
v i
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LIST OF TABLES
(continued)
Table No. Title Page
42, 43, 44 Packaging Area Exhaust Duct
Particle Size Distribution Rurrs 1, 2, 3 1°7
45 Process Hoods TP9 and TP10
Summary of Visible Emissions 113
46 Crusher Transfer Point
Summary of Visible Emissions 115
47 Crusher-Grizzley
Summary of Visible Emissions 117
48 Crusher Scrubber Outlet
Summary of Visible Emissions 119
49 Fine Ore Bins Scrubber Inlet Transfer Point
Summary of Visible Emissions 120
50 - Fine Ore .Bins Hopper Exhaust Duct
Summary of Visible Emissions 121
51 Fine Ore Bins Scrubber Outlet Duct
Summary of Visible Emissions 122
52 Dryer Scrubber Outlet Duct
Summary of Visible Emissions 123
53 Packaging Area Enclosure
Summary of Visible Emissions 12-4
54, 55 EPA Method 22
Summary of Fugitive Emission 125
v i i
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LIST OF FIGURES
Figure
No. Title Page
1 Generalized Flow Diagram 10
2 Crusher Transfer Point Exhaust Duct Port and
Sampling Point Locations 17
3 Crusher Scrubber Inlet Duct Port and Sampling
Point Locations 18
k Crusher-Grizzley Exhaust Duct Port and
Sampling Point Locations 19
5 Crusher Scrubber Outlet Duct Port and Sampling
Point Locations 20
6 Fine Ore Bins Hopper Exhaust Duct Port and
Sampling Point Locations 21
7 Fine Ore Bin Scrubber Inlet Duct Port and
Sampling Point Locations 22
8 Fine Ore Bins Scrubber Outlet Duct Port and
Sampling Point Locations 23
9 Packaging Area Exhaust Duct Port and Sampling
Point Locations 24
10 Dryer Scrubber Outlet Duct Port and Sampling
Point Locations 25
11 Dryer Scrubber Inlet Duct Port and Sampling
Point Locations 26
12 Particulate Sampling Train EPA Method 5 28
13 Particulate Sampling Train EPA Method 5 29
14 Particle Size Distribution Sampling Apparatus -
Andersen 2000, Inc. 31
15 Andersen Sampler Head Plate Assembly 32
v M i
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SUMMARY
The Emission Measurement Branch of the U.S. Environmental Protection
Agency contracted Roy F. Weston, Inc. to conduct a source testing and
analysis program at Exxon Minerals Company, U.S.A.'s Converse County,
Wyoming Uranium Processing Facility.
The primary objective of the testing program was to quantify the par-
ticulate emissions to the atmosphere from three scrubber-controlled
sources at the plant (Primary Crusher, Fine Ore Bins and Dryer). This
objective was achieved by performing a series of three particulate
tests utilizing EPA Method 5^ procedures at each scrubber exhaust stack
location. In addition, visual determinations of plume opacities were
made simultaneously with each particulate test at the three source
discharge points according to EPA Method 9^ protocol. A singular
Anderson" cascade impactor test was conducted at each of the three
exhaust stack locations. Also, three EPA Method 5 particulate and three
Anderson cascade impactor tests were executed at each corresponding
scrubber inlet site. In addition, visual determination of opacities
(by EPA Method 9) and the frequency of fugitive emissions (by EPA Method
223)was monitored at several points in the processing operation.
The particulate matter emission results are summarized below.
CRUSHER TRANSFER POINT EXHAUST DUCT
Test
Number
Date
1 9-27-79
2 9-27-79
3 9-27-79
Series Average
Test
Number Date
1 9-27-79
2 9-27-79
3 9-27-79
Series Average
Particulate Concentration
Grains/DSCF
0.002
0.003
0.013
Particulate Emission Rate
Pounds/Hour
0.021
0.029
0.107
0.052
CRUSHER SCRUBBER INLET DUCT
Particulate Concentration
Gralns/DSCF
0.012
0.009
0.006
Particulate Emission Rate
Pounds/Hour
0.742
0.562
0.3^1
0.548
1
Code of Federal Regulations, Title 40, Part 60, Appendix A, "Standards
of Performance for New Stationary Sources", August 18, 1977-
2Federal Register, Vol. 39, No. 219, November 12, 1974.
3Draft Method Revised 28 July 1978.
-1-
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CRUSHER-GRIZZLEY EXHAUST DUCT
Test Participate Concentration
Number Date Grains/DSCF
0.008
0.010
0.013
1 9-27-79
2 9-27-79
3 9-27-79
Series Average
Test
Number
Date
1 9-27-79
2 9-27-79
3 9-27-79
Series Average
Particulate Emission Rate
Pounds/Hour
0.169
0.229
0.298
0.232
CRUSHER SCRUBBER OUTLET DUCT
Particulate Concentration
Grains/DSCF
0.002
0.005
Q.QQk
FINE ORE BINS SCRUBBER OUTLET DUCT
Particulate Emission Rate
Pounds/Hour
0.146
0.314
0.223
0.228
Test
Number
Date
1 9-28-79
2 9-28-79
3 9-28-79
Series Average
Test
Number
Date
1 9-28-79
2 9-28-79
3 9-28-79
Series Average
Test
Number
Date
1 9-28-79
2 9-28-79
3 9-28-79
Series Average
Particulate Concentration
Grains/DSCF
0.003
0.002
0.002
FINE ORE BINS SCRUBBER INLET DUCT
Particulate Emission Rate
Pounds/Hour
0.042
0.041
0.039
0.041
Particulate Concentration
Grains/DSCF
0.006
0.003
0.004
Particulate Emission Rate
Pounds/Hour
0.089
0.057
0.065
0.070
FINE ORE BINS HOPPER EXHAUST DUCT
Particulate Concentration
Grains/DSCF
0.003
0.003
0.003
Particulate Emission Rate
Pounds/Hour
0.010
0.008
0.008
0.009
-2-
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Test
Number Date
1 10-1-79
2 10-1-79
3 10-1-79
Series Average
DRYER SCRUBBER INLET DUCT
Participate Concentration
Grains/DSCF
2.527
3.335
0.900
Test
Number
Date
Participate Emission Rate
Pounds/Hour
12.53
15.75
4.35
10.88
DRYER SCRUBBER OUTLET DUCT
1 10-1-79
2 10-1-79
3 10-1-79
Series Average
Participate Concentration
Grains/DSCF
0.125
0.051
0.027
PACKAGING AREA EXHAUST DUCT
Particulate Emission
Pounds/Hour
Rate
2.81
1.02
0.61
1.48
Test Particulate Concentration
Number Date Grains/DSCF
0.007
0.003
0.003
. 1 10-1-79
2 10^1-79
3 10-1-79
Series Average
Particulate Emission Rate
Pounds/Hour
0..050
0.025
0.023
0.033
The measured particulate removal efficiency of the Crusher Area Scrubber
was 53.0%, that of the Fine Ore Bins Scrubber was M).3% the Dryer
Scrubber was .85.7%.
-3-
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INTRODUCTION
The Emission Measurement Branch of the I). S. Environmental Protection
Agency contracted Roy F. Weston, Inc. to conduct a source testing and
analysis program at the Exxon Minerals Company, U.S.A.'s Converse County,
Wyoming Uranium Processing Facility. The objective of the testing pro-
gram was to measure various emission parameters relating to milling,
drying and packaging operations at the plant.
/
The locations tested, plus the number and types of tests performed at
each site are listed below:
1. Crusher Transfer Point Exhaust Duct
a. Three particulate tests by EPA Method 5.
b. Three particle size distribution tests by cascade
ImpactI on (Anderson ).
2. Crusher Scrubber Inlet Duct
a. Three particulate tests by EPA Method 5.
b. Three particle size distribution tests by cascade
impaction (Anderson^). •
3. Crusher-Grizzley Exhaust Duct
a. Three particulate tests by EPA Method 5.
b. Three particle size distribution tests by cascade
impaction (Anderson^).
A. Crusher Scrubber Outlet Duct
a. Three particulate tests by EPA Method 5.
b. One particle size distribution test by cascade
impaction (Anderson^).
c. One opacity test by EPA Method 9 simultaneous with
Run One particulate test.
5. Crusher-Grizzley Hood Area
a. Three opacity tests by EPA Method 9 and three
fugitive tests by Method 22. Visual determination
of plume opacity and frequency performed concurrently
with particulate tests.
-5-
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6. Conveyor Transfer Point Area
a. Three opacity tests by EPA Method 9 and three
fugitive tests by Method 22 performed in con-
junction with particulate tests.
7. Crusher Transfer Point Area
a. Three EPA Method 9 and Method 22 tests performed
in conjunction with the particulate tests.
8. Fine Ore Bins Scrubber Outlet Duct
a. Three particulate tests by EPA Method 5.
b. One particle size distribution test by cascade
impaction (Anderson^).
c. One opacity test by EPA Method 9 simultaneous with
Run One particulate test.
9. Fine Ore Bins Scrubber Inlet Duct
a. Three particulate tests by EPA Method 5.
b. Three particle size distribution tests by cascade
impaction (Anderson^).
10. Fine Ore Bins Hopper Exhaust Duct
a. Three particulate tests by EPA Method 5.
b. Three particle size distribution tests by cascade
impaction (Anderson^).
11. Fine Ore Storage Bins Entrance Area
a. Three EPA Method 9 and Method 22 tests performed
in conjunction with particulate tests.
12. Fine Ore Bins Hopper Area
a. Three EPA Method 9 and Method 22 tests performed
in conjunction with particulate tests.
13. Dryer Scrubber Inlet Duct
a. Three particulate tests by EPA Method 5.
b. Three particle size distribution tests by cascade
impaction (Anderson")'.
-6-
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1A. Dryer Scrubber Outlet Duct
a. Three particulate tests by EPA Method 5.
b. One particle size distribution test by cascade
impact ion (Anderson^).
c. Three opacity tests by EPA Method 9 simultaneous
with each particulate test.
15. Packaging Area Exhaust Duct
a. Three particulate tests by EPA Method 5.
b. Three particle size distribution tests by cascade
impaction (Anderson^).
16. Barreling Enclosure Area
a. Three EPA Method 9 and Method 22 tests performed
simultaneously with particulate tests at the
packaging area.
All tests were conducted during the period from September 27 through
October 1, 1979 by Weston personnel and were observed by Mr. Dennis P.
Hplzschuh, EPA Technical Manager.
Test data and test result summaries are presented in Tables 1 through
20 of this report. Particle size distribution results are shown In
Tables 21 through Mt. Also included is a description of the facility
processes, test locations, test equipment, test procedures, sample
recovery, analytical methods used during the test program and trace
elements analysis results. Raw test data, laboratory reports,
sample calculations, equipment calibration data, and a list of project
participants are provided in Appendices A through E, respectively.
-7-
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DESCRIPTION OF TEST LOCATIONS
Crusher Transfer Point Exhaust Duct
Two 4" I.D. test ports, 90° apart, were installed on a straight section
of the 32" I.D. metal stack at a location greater than 8 diameters (501)
downstream and greater than 2 diameters (20') upstream from the nearest
flow disturbances. EPA Method 1 criteria for this test location re-
quired a minimum of 8 traverse points. See Figure 2 for port and sam-
pling point locations.
Crusher Scrubber Inlet Duct
Two 4" I.D. test ports at 100° were placed on the 28" I.D. metal stack
1.3 diameters downstream and 1.1 diameters upstream from the nearest
flow disturbances. Obstructions near the duct necessitated installing
the ports > 90° apart. Forty-eight sampling points (2k per axis) were
required for testing. See Figure 3 for port and sampling point locations.
Crusher-Grizzley Exhaust Duct
Two 4" I.D. test ports were placed at right angles on a straight section
of the 16" I.D. ductwork leading to the inlet of the scrubber at a
location of 12'-' (. 75.diameter) downstream, and 36" (2.3 diameters) upstream
from the nearest gas stream flow disturbances. The stack geometry re-
quired the use of the maximum number of traverse points specified by EPA
Method 1 (48, 2k points per axis). Figure k illustrates port and
sampling point locations.
Crusher Scrubber Outlet Duct
Two V I.D. test ports, 90° apart, were installed in a straight section
of the 41" I.D. metal duct at a location which was < 1 duct diameters
downstream and <1 diameter upstream from flow disturbances. A total of
48 points were selected for this test location (24 per axis). Figure 5
illustrates port and traverse point locations.
Fine Ore Bins Hopper Exhaust Duct
Two 4" I.D. test ports, 90° apart, were installed on a straight section
of the 6" I.D. metal duct at a location greater than 8 stack diameters
downstream and greater than 2 stack diameters upstream from the nearest
flow disturbances. Due to the smaller duct diameter (6") a one point
traverse was used during the sampling program. See Figure 6 for port
and sampling point locations.
-15-
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Fine Ore Bins Scrubber Inlet Duct
Two V I.D. test ports, 90° apart, were installed on a straight section
of the 10" I.D. metal duct leading to the inlet of the scrubber. The
test ports were located 1 diameter downstream and 2 diameters upstream
from the nearest gas stream flow disturbances. A total of 20 traverse
points (10 per axis) were sampled for 3 minutes per point resulting in a
total test time of 60 minutes. See Figure 7 for port and sampling point
locations.
Fine Ore Bins Scrubber Outlet Duct
Two V I.D. test ports, 90° apart, were located on a straight section of
the 12" I.D. metal stack at a location —-3 stack diameters downstream
and less than 1 diameter upstream from the nearest flow disturbance. A
total of 32 traverse points (16 per axis) were sampled for 2 minutes per
point for a total test time of 64 minutes. See Figure 8 for port and
sampling point locations.
Packaging Area Exhaust Duct^
Two 4" I.D. test ports, 90° apart, were placed on the 7" I.D. duct lead-
ing from the packaging area. The ports were located greater than 8 stack
diameters downstream and greater than 2 stack diameters upstream from the
nearest flow disturbances. The smaller duct diameter resulted in util-
izing a one-point traverse during the sampling. Figure 9 shows the port
and sampling point location.
Dryer Scrubber Outlet Duct
/
Two V I.D. test ports, 90° apart, were located on the 13-3A" I.D. duct.
The ports were installed on a straight section of the metal duct 5 di-
ameters downstream and 2 diameters upstream from the nearest gas stream
flow disturbances. Sixteen sampling points C8 per axis) were selected
for testing. See Figure 10for port and sampling point locations.
Dryer Scrubber Inlet Duct
Two V I.D. sampling ports were installed on a straight section of the
13~3/4" I.D. duct. The ports were positioned 3 duct diameters downstream
and 5 duct diameters upstream from the nearest gas stream flow disturb-
ances. Sixteen traverse points across the X axis were traversed during
sampling. Port Y diameter could not be traversed because the port was
** 2' above, and in line with, the platform which precluded the insertion
of the sampling probe. Figure 11 illustrates the port and sampling point
locations.
-16-
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WALL
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
FIGURE 2
CRUSHER TRANSFER POINT EXHAUST DUCT
PORT AND SAMPLING POINT LOCATIONS
r^ «-"
c
)
GAS FLOW
r
)
— -rn :>u 9\
y
4
X
^
k ^
V2" I.D
r )
U '""• ^
Y
—1-2" I. Dv
PORT X
TRAVERSE
POINT
NUMBER
1
2
3
DISTANCE FROM
INSIDE NEAR
WALL, inches
3A
3
9
1H
-17-
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EXXON .MINERALS COMPANY, U.S.A.
Converse County, Wyoming
FIGURE 3
CRUSHER SCRUBBER INLET DUCT
PORT AND SAMPLING POINT LOCATIONS
H-36'"
32'
FLOW
O
ID
PAN
PORT X
PORT Y
100 SEPARATION DUE TO
GRATING OBSTRUCTIONS
TRAVERSE
POINT
NUMBER
1
2
3
4
5
6
7
8
DISTANCE FROM
INSIDE NEAR
WALL, inches
' • 4
7/8
1*
24
2 7/8
3 5/8
4*
5 3/8
9 6
10
11
12
13
14
15
16
17
18
19
20
21
22
7 5/8
3
11 1/8
16 3/4
18 7/8
204
21*
22
23 3/8
244
25
25 5/8
26 3/8
23 ' 27
24 27 5/8
FLOOR
-18-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
FIGURE k
CRUSHER-GRIZZLEY EXHAUST DUCT
PORT AND SAMPLING POINT LOCATIONS
FROM
GRIZZLEY
\r
t
TO
SCRUBBER
Ote^
P
Y
i 11 i 1 1 |
1 ' 1 J ' ^
k
16" 1 .
f
"16
16
PORT Y
TRAVERSE
POINT
NUMBER
• 1
1
2
3
4
S
6
7
8
9
10
11
12
13
14
15
16
DISTANCE FROM
INSIDE NEAR
WALL, inches
4
3A
1 3/8
2
2 3A
3i
H
6
10
11i
12*
134
14
14 5/8
154
15 3/4
PORT X
-16" ID"
-19-
-------
EXXON MINERALS COMPANY*.U.S.A.
Converse County, Wyoming
FIGURE 5
CRUSHER SCRUBBER OUTLET DUCT
PORT AND SAMPLING POINT LOCATIONS
O
X
PORT Y
PORT X
TRAVERSE
POINT
NUMBER
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
DISTANCE FROM
INSIDE NEAR
WALL, inches
i
1*
24
34
H
5 3/8
6 5/8
8
9i
11 1/8
134
16 3/8
24 3/4
27 3/4
29 7/8
3H
33 1/8
34 3/8
35i
36 3/4
37
38
39
40i
-20-
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EXXON MINERALS COMPANY,'.U.S.A.
Converse County, Wyoming
FIGURE 6
FINE ORE BINS HOPPER EXHAUST DUCT
PORT AND SAMPLING POINT LOCATIONS
RAILINGS
GRATING LEVEL
O
PORT Y
T
50'
TRAVERSE
POINT
NUMBER
CENTER
POINT
DISTANCE FROM
INSIDE NEAR
WALL, inches
PORT X
RAILING
TOP VIEW
-21-
-------
EXXON MINERALS COMPANY,. U.S.A.
Converse County, Wyoming
FIGURE 7
FINE ORE BINS SCRUBBER INLET DUCT
PORT AND SAMPLING POINT LOCATIONS
FAN
EXIT
o
Y
TRAVERSE
POINT
NUMBER
1
2
<2
5
6
7
/
8
9
10
DISTANCE FROM
INSIDE NEAR
WALL, inches
2+
7/8
U
3 3/8
6
7 3A
8i
9 1/8
9 3A
PORT Y
PORT X
-22-
-------
EXXON MINERALS. COMPANY, U.S.A.
Converse County, Wyoming
FIGURE 8
FINE ORES BIN SCRUBBER OUTLET DUCT
PORT AND SAMPLING POINT LOCATIONS
O
RAILING
RAILING
12" I.D.
PORT Y
TRAVERSE
POINT
NUMBER
1
2
3
k
5
6
7
8
9
10
11
12
13
15
16
DISTANCE FROM
INSIDE NEAR
WALL, inches
4
5/8
1
1 i
24
2 5/8
3 3/8
*»i
7i
8 5/8
9 3/8
10
10*
11
11*
11 3 A
-23-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
FIGURE 9
PACKAGING AREA EXHAUST DUCT
PORT AND SAMPLING POINT LOCATIONS
5'
IfO1
QX ^ Y
FLOOR LEVEL
4
7"
^-~
kD- EH
PORT Y
TRAVERSE .DISTANCE FROM
POINT INSIDE NEAR
NUMBER
CENTER
POINT
WALL, inches
PORT X
-24-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
FIGURE 10
DRYER SCRUBBER OUTLET DUCT
PORT AND SAMPLING POINT LOCATIONS
7'
FAN
13 3/V1 l.D.
1r
PORT Y
TRAVERSE
POINT
NUMBER
1
2
3
J»
5
6
7
8
DISTANCE FROM
INSIDE NEAR
WALL, inches
i
1 3/8
2 5/8
•4 3/8
94
10 7/8
12
13
PORT X
-25-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
FIGURE 11
DRYER SCRUBBER INLET DUCT
PORT AND SAMPLING POINT LOCATIONS
PLATFORM
' 13 3 A" .1.0.
T jjf-
^^ — ~~~~ f6^~~^-^
^^ ' ~^-^
/ ' x
/ *
/ ' \
/ , \
/ - \
/ • \
/ '
\16 1 /
\ ' /
\ § /
\ ' /
TRAVERSE
POINT
NUMBER
j
i
1
2
3
5
6
7
8
9
— , 10
1 OrtOT* V 11
PORT A 1 1
— ' 12
13
15
16
DISTANCE FROM
INSIDE NEAR
WALL, inches
4
5/8
1 1/8
1 3 //t
2 3/8
3
3 7/8
54
8 5/8
9 7/8
10 ""Jk
\ \J j/ *t
Hi
12
12 5/8
13
1 3i
Port Y
NOTE: Port Y not traversed due to port
access blockage by platform.
-26-
-------
DESCRIPTION OF SAMPLING TRAINS
_P_art.i culate Sampling Trains
The test train utilized for participate sampling at all test locations
was the standard EPA Method 5 train (see Figure 12).
A stainless steel nozzle was attached to a heated (—250°F) borosilicate
glass probe which was connected directly to a borosilicate filter holder
containing a 9~cm Reeve Angel 900 AF glass fiber filter. The filter
holder was maintained at approximately 250°F in a heated chamber, and
was connected by Tygon^ vacuum tubing to the first of four Greenburg-
Smith impingers which were included in the train to condense the moisture
in the gas stream. Each of the first two impingers contained 100 ml
of distilled water, the third was dry and the final impinger contained
200 grams of dry per-weighted silica gel. The first, third, and fourth
impingers were modified Greenburg-Smith type; the second was a standard
Greenburg-Smith impinger. All impingers were maintained in a crushed
ice bath. A RAC control console with vacuum pump, dry gas meter, a
calibrated orifice, and inclined manometers completed the sampling train.
Flue gas temperature was measured by means of a Type K thermocouple
which was connected to a direct readout pyrometer. The thermocouple
sensor was positioned adjacent to the sampling nozzle.
Gas velocity was measured using a calibrated "S" type pi tot tube pro-
vided with extensions and fastened alongside the sampling probe. Gas
stream composition (carbon dioxide, oxygen, and carbon monoxide content)
was determined utilizing Orsat apparatus to analyze stack gas samples.
Gas stream composition proved to be ambient air with the exception of
the dryer inlet and outlet test sites which contained products of
combustion.
Figure 13 shows the EPA Method 5 train utilized at the Fine Ore Bins
Hopper Duct and the Packaging Area Duct. The test train shown is
identical to the one described above, except a rigid glass connection
is used between the back half of the filter holder and the first im-
pinger, rather than the flexible vacuum tubing.
Particle Size Distribution Sampling Apparatus
A stainless steel nozzle was connected directly to an 8-stage Anderson^
cascade impaction device which separated the particles according to
their effective aerodynamic particle diameters. A glass fiber filter
was used to capture any particles that passed through the impactor sub-
strates to permit the measurement of total particulate. The filter
holder was maintained at stack temperature and was connected by Tygon^
-27-
-------
0.75 TO I in.
I ItMl
J Jf
TEMPERATURE SENSOR
PROBE
TEMPERATURE CONTROLLED
HEATED AREA
> 0.75 in.
THERMOMETER
TEMPERATURE SENSOR
PITOT MANOMETER
ORIFACE
REVERSE-TYPE
PITOT TUBE
THERMOMETERS
\
DRt GAS METER
AIR TIGHT PUMP
CHECK VALVE
VACUUM
LINE
FIGURE 12 PARTICULATE SAMPLING TRAIN
EPA METHOD 5
-------
I
10
yTEMPERATURE
SENSOR
THERMOMETER
CHECK VALVE
THERMOMETERS
VACUUM LINE
ACUUM GUAGE
HEATED AREA
FILTER HOLDER
REVERSETYPE
PITOT TUBE
PITOT MANOMETER
ICE BATH
DISTILLED WATER
ORIFICE
AND
MANOMETER
FIGURE 13 PARTICULATE SAMPLING TRAIN-EPA METHOD 5
-------
vacuum tubing to the first of four Greenburg-Smith impingers which were
included in the train to condense the moisture in the gas stream. All
impingers were maintained in a crushed ice bath. A RAC control console
with vacuum pump, dry gas meter, a calibrated orifice, and inclined
manometers completed the sampling train (see Figures 1^ and 15).
-30-
-------
Thermometer
Nozzle
Vacuum
Tubing
Reverse-Type
Pilot Tube
oaaai
' rr^—v^—r^—r^—i
~\ /—\ — ,—\ i—
Pilot Manometer/Tnermometers Bypass Valve Impingers
Orifice
Vacuum Gauge
Air Tight Pump
Check Valve
Vacuum
Line
FIGURE 14 PARTICLE SIZE DISTRIBUTION SAMPLING
APPARATUS - ANDERSEN 2000, INC.
-------
CROSSHAIR GASKET
PLATE '0'
INCONEL SPACER
CROSSHAIR GASKET
CONFIGURATION '2'
PLATE 'I1
INCONEL SPACER
CROSSHAIR GASKET
CONFIGURATION '!'
PLATE '2'
INCONEL SPACER
CROSSHAIR GASKET
CONFIGURATION '2'
PLATE '3'
INCONEL SPACER
CROSSHAIR GASKET
CONFIGURATION 'I1
PLATE '4'
INCONEL SPACER
CROSSHAIR GASKET
CONFIGURATION '2'
PLATE '5'
INCONEL SPACER
CROSSHAIR GASKET
CONFIGURATION '!'
PLATE Y6Y
INCONEL SPACER
CROSSHAIR GASKET
CONFIGURATION '2'
PLATE '7'
INCONEL SPACER
CROSSHAIR GASKET
CONFIGURATION '!'
PLATE '8'
INCONEL SPACER
CROSSHAIR GASKET
BACKUP FILTER
PLATE 'F'
INCONEL SPACER
SUBSTRATE
SUBSTRATE
SUBSTRATE
SUBSTRATE
SUBSTRATE
SUBSTRATE
SUBSTRATE
SUBSTRATE
PLATE HOLDER
FIGURE 15
ANDERSEN SAMPLER HEAD
PLATE ASSEMBLY
-32-
-------
TEST PROCEDURES
Preliminary Tests
Preliminary test data was obtained at each sampling location. Stack
geometry measurements were recorded and sampling point distances calcu-
lated. A preliminary velocity traverse was performed at each test
location utilizing a calibrated "S"-type pi tot tube and a Dwyer inclined
manometer to determine velocity profiles. A check for the presence or
absence of cyclonic flow was conducted at each test location prior to
formal testing. Stack gas temperatures were observed with a direct read-
out pyrometer equipped with a chromel-alumel thermocouple.
Preliminary test data was used for nozzle sizing and nomagraph set-up
for isokinetic sampling procedures.
Calibration of the probe nozzles, pitot tubes, metering systems, probe
heaters, temperature gauges and barometer were performed as specified
in Section 5 of EPA Method 5 test procedures (see Appendix D for cali-
bration data).
Crusher Transfer Point Exhaust Duct
A series of three tests were conducted at the Crusher Transfer Point Ex-
haust Stack to measure the concentration and mass rate of particulate
matter emissions. Eight traverse points (Vper port axis) were sampled
for 12 minutes each, resulting in a total test time of 96 minutes.
During particulate sampling, gas stream velocities were measured by in-
serting a calibrated "S"-type pitot tube into the stream adjacent to the-
sampling nozzle. The velocity pressure differential was observed immedi-
ately after positioning the nozzle at each point, and sampling rates were
adjusted to maintain isokinetic sampling. Stack gas temperatures were
also monitored at each point with the pyrometer and thermocouple. Addi-
tional temperature measurements were made at the final impinger and at
the inlet and outlet of the dry gas meter.
Test data were recorded at each traverse point during all test periods.
Leak checks were performed according to EPA Method 5 instructions prior
to and after each run and/or component change. Table 1 presents a
summary of test data for each of the three runs. Test result summari-
zation appears on Table 11.
One sampling point located at a site of average velocity was selected
from particulate traverse data for particle size distribution testing.
The gas stream was sampled isokinetically at that point for 75 minutes,
which permitted collection of sufficient samples for analysis without
overloading the filter substrates. Sample volume, temperature, and
pressure data were recorded every 5 minutes during sampling. See Tables
21 through 23 for distribution plots.
-33-
-------
Crusher Scrubber Inlet Duct
Three 96-minute Method 5 test runs were performed at the scrubber inlet.
A total of 48 points were sampled for 2 minutes each per test.
Procedures for isokinetic sampling were identical to those described in
Crusher Transfer Point Exhaust Duct section.
See Tables 2 and 12 for test data and test result summaries, respectively.
Three particle size distribution tests were conducted at a point of
average velocity. Each particle size distribution test was one hour in
length. Sample volume, temperature, and pressure data were recorded
every 5 minutes. See Tables 2k through 26 for distribution plots.
Crusher-Grizzley Exhaust Duct
Three Method 5 tests were performed at the Crusher-Grizzley Exhaust Duct.
32 points were traversed (16 per axis) for 3 minutes each, yielding a
test period of 36 minutes.
Isokinetic sampling procedures were identical to those previously des-
cribed. Table 3 shows test data summarization and Table 13 presents
test results.
Three particle size distribution tests were conducted at an average
point of velocity. Each sample set was 75 minutes in length. Readings
were recorded every 5 minutes during each test. See Tables 28 through
30 for distribution plots.
Crusher Scrubber Outlet Duct
Three Method 5 test runs were conducted on the Crusher Scrubber Outlet
Duct. Forty-eight sampling points (2k per axis) were sampled for two
minutes each, resulting in a total test time of 96 minutes.
Sampling procedures were identical to those previously described. See
Tables k and 1A for test data and test result summaries, respectively.
One particle size distribution test was completed at an average point of
velocity. Total test time was 160 minutes, with readings taken every 5
minutes. See Table 27 for particle distribution plot.
Fine Ore Bins Scrubber Outlet Duct
Three Method 5 tests were performed at the scrubber outlet site. Thirty-
two traverse points (16 per axis) were sampled for 2 minutes at each
point, yielding a 64-minute test period.
-------
Sampling procedures were identical to those previously described.
Table 5 shows test data summarization and Table 15 presents test results,
One particle size distribution sample was collected isokinetical ly at
a point of average velocity over a 90-minute period. Sample volume,
temperature, and pressure data were recorded every 5 minutes during
sampling. See Table 31 for distribution results.
Visual determinations of plume opacity were performed by a certified
observer according to Method 9 procedures during test Run One. A
summary of results is presented in Table 50.
Fine Ore Bins Scrubber Inlet Duct
Three test runs were conducted by EPA Method 5 procedures at the inlet
to the Fine Ore Bins Scrubber. A total of twenty traverse points (10
per axis) were sampled for 3 minutes each, resulting in a total test
time of 60 minutes. Tables 6 and 16 show test data and test results,
respectively.
Three particle size distribution tests were performed at a point of
average velocity over a 90-minute period. Readings were taken every 5
minutes during sampling. Tables 32 through 3** show the particle size
distribution.
Fine Ore Bins Hopper Exhaust Duct
Three 6^-minute Method 5 test runs were performed at the Hopper Exhaust.
A one point traverse was sampled for 6A minutes per test.
Procedures for isokinetic sampling were identical to those described
for the other locations. Table 7 shows test data summarization and
Table 17 presents test results.
Three particle size distribution tests were conducted at a point of
average velocity over an 85-minute period. Tables 35 through 37 show
the particle size distribution.
Dryer Scrubber Inlet Duct
Three Method 5 tests were performed at the inlet simultaneous with par-
ticulate tests at the outlet. Sixteen points were traversed for 4
minutes each, yeilding a test period of 6k minutes.
Isokinetic sampling procedures were identical to those previously des-
cribed except that test data were recorded every A minutes. Table 8
shows test data summarization and Table 18 presents test results.
-35-
-------
Three particle size distribution samples were collected isokinetically
at a point of average velocity over a 2 minute period. Sample volume,
temperature, and pressure data was recorded before and after the test.
See Tables 39 through 41 for distribution results.
Dryer Scrubber Outlet Duct
Three EPA Method 5 tests were performed at the outlet simultaneous with
particulate test runs at the inlet. Sixteen points were traversed (8
per port axis) for 4 minutes each, yeilding a test period 64 minutes in
length.
Procedures for isokinetic sampling were identical to those described
for the first location, except that test data were recorded every 4
minutes. Test data and test result summaries are provided in Tables 9
and 19, respectively.
One sampling point located at a site of average velocity was selected
from particulate traverse data for particle size distribution testing.
The gas stream was sampled isokinetically at that point for 4 minutes
which permitted collection of sufficient samples for analysis without
overloading the filter substrates. Sample volume, temperature, and
pressure data were recorded before and after the test. See Table 38
for a distribution plot.
Visual determinations of plume opacity were performed by a certified
observer according to Method 9 procedures. A summary of results is
presented in Table 51.
Packaging Area Exhaust Duct
A one point traverse in the center of the small diameter duct was sampled
for 64 minutes during each of the three EPA Method 5 tests. Readings
were taken every 4 minutes during the test period.
Isokinetic sampling procedures were identical to those previously des-
cribed except that all test data were taken at a single point. Table
10 shows test data summarization and Table 20 presents test results.
Three particle size distribution samples were taken at midpoint in the
duct. Total sample time for each run was 55 minutes. Tables 42 through
44 present particle distribution plots.
-36-
-------
ANALYTICAL PROCEDURES
Particulate Sample Recovery
At the conclusion of each test, the sampling trains were dismantled,
openings sealed, and the components transported to the field laboratory.
Sample integrity was assured by maintaining chain-of-custody records,
which will be supplied upon request.
A consistent procedure was employed for sample recovery.
The glass fiber filter(s) was removed from its holder with
tweezers and placed in its original container (petri dish),
along with any loose particulate and filter fragments (Sample 1).
The probe (EPA 5) and nozzle were separated, and the internal
particulate rinsed with acetone into a borosilicate container
while brushing a minimum of three times until no visible
particles remained. Particulate adhering to the brush was
rinsed with acetone into the same container. The front half
of the ,fi1ter hoider was rinsed wi th acetone while brushing
a minimum of three times. The rinses were combined (Sample
2) and the container sealed with a Teflon-lined closure.
The total liquid in impingers one, two and three was measured,
the value recorded, and the liquid discarded.
The silica gel was removed from the last impinger and immed-
i ately weighted.
An acetone sample was retained for blank analysis.
Particulate Analyses
The filters (Sample 1) and any loose fragments were desiccated for 2k
hours and weighed to the nearest 0.1 milligram to a constant weight.
The acetone wash samples (Sample 2) were evaporated at ambient temper-
ature and pressure in tared beakers, and desiccated to constant weight.
All sample residue weights were adjusted by the acetone blank value.
The weight of the material collected on the glass fiber filter(s) plus
the weight of the residue of the acetone nozzle/probe/front-half filter
holder washes represents the "total" EPA Method 5 catch. Complete
laboratory results are presented in Appendix B of this report.
-37-
-------
Particle Size Sample Recovery and Analyses
The cascade impactor substrates and any loose fragments were carefully
removed from their support plates with tweezers and placed in individual
containers (petri dishes) for shipment toWeston's laboratory.
Each cascade impactor filter was fired at 525°C and pre-weighed to the
nearest 0.1 milligram to constant weight at Weston's laboratory prior
to on-site application. Subsequent to emissions exposure, the cascade
impactor substrates, back-up filters and any loose fragments (Sample k)
were desiccated for 2k hours in the laboratory, and weighed to the
nearest 0.1 milligram to constant weight.
-38-
-------
York Ssn/tcss Corporation
• Energy and Environmental Systems Engineering
• Atmospheric Sciences Services
• Emission Measurement Services
December 9, 1980
One Research Drive
Stamford. Connecticut 06906
Telephone: 1203) 325-1371
TWX: 710-474-3947
Mr. David Ralston
Roy F. Weston, Inc.
Weston Way
West Chester, PA 19380
Reference: TRACE ELEMENT ANALYSIS OF PARTICIPATE SAMPLES
Dear Mr. Ralston:
The results of the trace element analyses of your particulate
samples are enclosed. The samples are identified with the numbers
listed below and correspond to your sample descriptions as follows:
#37700 - Exxon - Dryer Scrubber, Run 3, 10/1/79 WESTON #25455
Please contact Mr. Robert Bradley, if you have any questions
Sincerely,
Maria Denaro
Project Scientist
MD/mdf
cc: Dennis Holzschuh
Roger Kniskern
Robert Bradley
A Subsidiary of York Research Corporation
-------
CASLE ADDRESS "LEDOUX TSANECK"
TELEX 134340
Q .;X 359 Alfred Avenue, Teaneck, Ne\v Jersey 07666 • Telephones:
***** .
I INDEPENDENT CONTROL. AND RESEARCH CHEMISTRY. INSTRUMENTAL AND CHEMICAL ANALYSIS • SAMPllttG.
I WEIGHING. SHIPPERS' REPRESENTATION. SENEFICIAriON. AND STORAGE OF ORES AND METALS
REPORT OF ANALYSIS
October
Our analysis of the sample of DUST SAMPLES
From York Research Corporation
Marked: Samples as below P.O. #3-5830
: - . :: '- - '.. ,••-••• . ••-.- PARTS PER MILLION
" -'-:.-•' -URANIUM --—---—--- v :
THORIUM •
:..- .' " BISMUTH"—' ----
. LEAD • —
; '^.'.-'-~- THALLIUM —
' v': " MERCURY -——-—-——— " •
GOLD — >'
PLATINUM
IRIDIUM
OSMIUM
RHENIUM :
TUNGSTEN
TANTALUM
HAFNIUM
LUTETIUM
YTTERBIUM
THULIUT^
ERBIUT^
HOLMIUM
DYSPROSIUM
TERBIUM
GADOLINIUM
EUROPIUM :
SAMARIUM '•
NEODYMIUM
PRASEODYMIUM
# » *
and submitted to us, shows:
. 37700
M
10.
<2.
<1.
<2.
<0.2
<1.
<0.2
-------
CA£L£ A jDRESS "LEDOUX TEANcCK"
TELEX 134340
BS
* ^9 ^ '/''^ A venue> Ttaneck. New Jersey 0 7666 . Telephones:
I INDEPENDENT CONTROL. AND RESEARCH CHEMISTRY, INSTRUMENTAL AND CHEMICAL ANALYSIS • SAMPLING.
I WEIGHING. SHIPPERS' REPRESENTATION. SENEFICIATION. AND STORAGE OF ORES AND METALS
REPORT OF ANALYSIS
October 31. 1980
Our analysis of the sample of DUST SAMPLES
i
7rom York Research Corporation
*
-Marked: Samples as below P.O. #3-5830
and submitted to us, shows:
. •:•-•' PARTS PER MILLION .
37700
CERIUM -: . '5."
LANTHANUM 10 ...
BARIUM • ' 10. .
CESIUM — — <1. ' . .
_ IODINE' XI. /
TELLURIUM • :- •
-------
BS
CABLE A33HCS3 "LECOUX TcANECK"
TELEX 134140
201 837 7160
\~>£j .••."•** 359 Alfred Avenue, Teancck. New Jersey 07666 • Telephones: ,., (
' l'**^-
I INDEPENDENT CONTROL. AND RESEARCH CHEMISTRY. INSTRUMENTAL AND CHEMICAL ANALYSIS • SAMPLING.
1 WEIGHING. SHIPPERS' REPRESENTATION.. BENEFICIATION. AMD STORAGE Of ORES AhO METALS
REPORT OF ANALYSIS
October 31, 1980
Our analysis of the sample of DUST SAMPLES
i ' .
From . York Research Corporation
Marked: Samples as below P.O. #3-5830
"PARTS • PER "MILLION
and. submitted to
COPPER' --
NICKEL •
. COBALT .._--————
IRON, ——-—-—-—,
•MANGANESE ---—
CHROMIUM——
VANADIUM —
TITANIUM
SCANDIUM
CALCIUM
POTASSIUM -
CHLORINE —
SULFUR
PHOSPHORUS
SILICON
ALUMINUM ^
MAGNESIUM
SODIUM
FLUORINE
CARBON
BORON
BERYLLIUM
LITHIUM
» * #
377QP.
10:
20.
' .5;'
- M.'
100.
10.
200
100.
5.
1000.
M .
50.
200.
20.
M
M
A
M
1
20.
A
2.
us, shows:
A. Matrix Interference
M. Signifie's Major Constituent of Sample
To
York Research Corporation
. PAGE 12 of 12 PAGES
LEDOUX &. COMPANY
NO WARRANTY IS EXTENDED IN RESPECT TO SERVICES PROVIDED BY LEDOUX & COMPANY
rar CTC cctr
-------
DISCUSSION OF TEST RESULTS
Participate test data and test result summaries are presented in Tables
1 through 20 of this report. Tables 21 through kk list the particle
size distribution of the particulate matter for all locations.
No unusual sampling difficulties or process operating problems were en-
countered during any of the test periods.
The amount of particulate matter discharged to the atmosphere from the
Crusher Scrubber and the Fine Ore Bins Scrubber was low (^0.005 grains/
dscf and ^ 0.31 pounds/hour). The certified observer verified the par-
ticulate test findings at the Crusher and Fine Ore Bins Scrubbers, since
no visible emissions were recorded emanating from either stack during
the simultaneous observation periods.
The particulate matter discharged from the Dryer Scrubber for the three
test runs averaged 0.068 grains/dscf and 1.5 pounds/hour. Opacity read-
ings observed during the first test run on the Dryer Scrubber Exhaust
were ^ 5 percent. Readings of 15 percent or less were recorded during
run two. A few 5 percent readings were observed during test three; the
balance of the readings were zero's.
Uranium was the major solid constituent entering the yellowcake scrubber
(-65 percent by weight). The uranium content of the yellowcake scrubber
discharge was~31 percent by weight. See Appendix B, Laboratory Reports,
page B-50 for the results of a detailed radionuclide analysis performed
on Run 1 yellowcake scrubber inlet and outlet test filters by Eberline-
Albuquerque Laboratory.
The particulate removal efficiency of the Dryer Scrubber averaged 85.7
percent for the three test sets; efficiency of the Fine Ore Bins Scrubber
averaged 40.3 percent; efficiency of the Crusher Scrubber averaged 53
percent.
During the preliminary velocity traverse at the Crusher Scrubber Outlet
and the Fine Ore Bin Scrubber Outlet, it was determined that a high
cyclonic flow condition existed. The yaw rotation angle at the null
point ranged from 48° to 68°. Alternative methodology, as approved by
the Administrator, was used at the outlet site to perform accurate sample
and velocity traverses. The probe/nozzle/pi tot tube assembly was rotated
during sampling so that the planes of the openings of the nozzle and
pitot tube were perpendicular to the oncoming gas stream at each traverse
point based on information obtained during the preliminary traverse.
-------
Due to high cyclonic flows, data obtained at the Crusher Scrubber Outlet
and the Fine Ore Bin Scrubber Outlet was recalculated based on their
respective inlet flows.
Fugitive emission tests were performed at the following locations, where
the illumination was-<10 foot candles (the level which is considered
necessary for proper application of the method):
1. Fine Ore Bins Transfer Point (3 f.c.).
2. Barreling Enclosure Area (9 f.c.)-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
TABLE 1
Crusher Transfer Point Exhaust Duct
SUMMARY OF TEST DATA
Test Data
Test Run Number
Test Date
Test Period
Sampling Data
Sampling Duration, minutes
Nozzle Diameter, Inches
Barometric Pressure, inches mercury
Average Orifice Pressure Differential, inches water
Average Dry Gas Temperature at Meter, °F
Total Water Collected by Train, ml
standard Volume of Water Vapor Collected, cubic feet
Dry Gas Meter Calibration Factor, dimensionless
Sample Volume at Meter Conditions, cubic feet
Sample Volume at Standard Conditions, cubic feet'
Gas Stream Composition
C02. percent by volume
02, percent by volume
CO, percent by volume
N2> percent by volume
Moisture in Gas Stream, percent by volume
Mole Fraction of Dry Gas
Molecular Weight of Dry Gas
Molecular Weight of Wet Gas
Gas Stream Velocity and Volumetric Flow
Static Pressure, inches water
Absolute Pressure, inches mercury
Average Temperature, °F
Pitot Tube Calibration Coefficient, dimensionless
Total Number of Traverse Points
Velocity at Actual Conditions, feet/second
Stack/duct Cross-Sectional Area, square feet
Volumetric Flow at Actual Conditions, cubic feet/minute
Volumetric Flow at Standard Conditions, cubic feet/minute
Percent Isokinetic
9-27-79
1735-1940
9-27-79
2058-2245
9-27-79
2355-0138
96.0
0.242
24.77
0.77
95.
9.5
0.45
0.995
52.20
41.02
96.0
0.21)2
24.77
0.72
88.
10.0
0.47
0.995
50.65
40.27
96.0
0.242
24.77
0.71
81.
14.7
0.69
0.995
47.42
38.22
0.0
20.9
0.0
79.1
1.1
0.989
28.97
28.85
0.0
20.9
0.0
79-1
1.2
0.988
28.97
28.84 .
0.0
20.9
0.0
79.1
1.8
0.982
28.97 '
28.77
-0.13
24.76
76.0
0.855
8.0
27.6
0.79
1300.
1050.
-0.05
24.77
71.
0.855
8.0
26.4
0.79
1240.
1010.
-0.05
24.77
67-
0.855
8.0
25.4
0.79
1200.
970.
99.9
102.1
100.4
Unit/Process Operations Data
MONITORED BY GCA CORPORATION PERSONNEL
'standard Conditions = 68°F (20°C) and 29-92 inches (760 mm) mercury, dry basis.
Ibid.
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
TABLE 2
Crusher Scrubber Inlet Duct
SUMMARY OF TEST DATA
Test Data
Test Run Number
Test Date
Test Period
SampI ing Data
Sampling Duration, minutes
Nozzle Diameter, inches
Barometric Pressure, inches mercury
Average Orifice Pressure Differential, inches water
Average Dry Gas Temperature at Meter, °F
Total Water Collected by Train, ml
standard Volume of Water Vapor Collected, cubic feet
Dry Gas Meter Calibration Factor, dimension less
Sample Volume at Meter Conditions, cubic feet
Sample Volume at Standard Conditions, cubic feet'
Gas Stream Composition
C02> percent by volume
02, percent by volume
CO, percent by volume
N2, percent by volume
Moisture In Gas Stream, percent by volume
Mole Fraction of Dry Gas
Molecular Weight'of Dry Gas
Molecular Weight of Wet Gas
Gas Stream Velocity and Volumetric Flow
Static Pressure, inches water
Absolute Pressure, inches mercury
Average Temperature, °F
Pilot Tube Calibration Coefficient, dimensionless
Total Number of Traverse Points
Velocity at Actual Conditions, feet/second
Stack/duct Cross-Sectional Area, square feet
Volumetric Flow at Actual Conditions, cubic feet/minute
Volumetric Flow at Standard Conditions, cubic feet/minute
Percent Isokinetic
Unit/Process Operations Data
9-27-79
1750-1917
96.0
0.250
21*. 77
1.37
110.
14.It
0.68
0.995
65.06
49.80
0.0
20.9
0.0 •
79.1
1.3
0.987
28.97
28.82
'1.9
24.63
77.
0.853
48.0
34.7
4.28
8890.
7100.
2
9-27-79
2120-2308
96.0
0.250
24.77
1.52
100.
19.0
0.90
0.995
71.03
55-39
0.0
20:9
o.o
79.1
1.6
0.984
28.97
28.80
-1.8
24.64
71.
0.853
48.0
36.3
4.28
9320.
7510.
9-27-79
2400-0149
96.0
0.250
24.77
1.30
99.
9.0
0.42
0.995
62.19
48.54
0.0
20.9
0.0
79.1
0.9
0.991
28.97
28.88
-1.7
24.65
71.
0.853
48.0
33-0
4.28
8470.
6870.
91.6 96.3 92.3
MONITORED BY GCA CORPORATION PERSONNEL
'standard Conditions = 68°F (20°C) and 29.92 inches (760 mm) mercury, dry basis.
2.
Ibid.
-46-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
TABLE 3
Crusher - Grizzley Exhaust Duct
SUMMARY OF TEST DATA
Test Data
86.0
0.241
2*1.77
1.21
110.
11.6
0.55
0.994
59.97
145.86
96.0
0.241
24.77
1.1(2
122.
8. it
O.ltO
0.994
70.89
53.17
96.0
0.241
24.77
1.41
116.
8.7
0.41
0.994
70.18
53.13
Test Run Number 1 2 3
Test Date 9-27-79 9-27-79 9-27-79
Test Period 1751-1945 2112-2258 0001-0139
SampI Ing Data
Sampling Duration, minutes
Nozzle Diameter, Inches
Barometric Pressure, inches mercury
Average Orifice Pressure Differential, inches water
Average Dry Gas Temperature at Meter, °F
Total Water Collected by Train, ml
standard Volume of Water Vapor Collected, cubic feet
Dry Gas Meter Calibration Factor, dimensionless
Sample Volume at Meter Conditions, cubic feet
Sample Volume at Standard Conditions, cubic feet'
Gas Stream Composition
C02. percent by volume
02, percent by volume
CO, percent by volume
N2, percent by volume
Moisture In Gas Stream, percent by volume
Mole Fraction of Dry Gas
Molecular Weight of Dry Gas
Molecular Weight of Wet Gas
Gas Stream Velocity and Volumetric Flow
Static Pressure, inches water -1.1 -1.1 -1.1
ASsolute Pressure, inches mercury 24.69 24.69 24.69
Average Temperature, °F 78. 75. 72.
Pitot Tube Calibration Coefficient, dimensionless 0.856 0.856 0.856
Total Number of Traverse Points 32.0 32.0 32.0
Velocity at Actual Conditions, feet/second 35.4 38.2 38.0
Stack/duct Cross-Sectional Area, square feet 1.40 1.40 1.40
Volumetric Flow at Actual Conditions, cubic feet/minute . 2960. 3200. 3180.
Volumetric Flow at Standard Conditions, cubic feet/minute 2370. 2580. 2590.
Percent Isokinetic
99.2 9(1.5 91,. 3
0.0
20.9
0.0
79-1
1.2
0.988
28.97
28.84
o.n
20.9
0.0
79-1
0.7
0.992
28.97
28.89
0.0
20.9
0.0
79-1
0.8
0.992
28.97
28.89'
Unit/Process Operations Data
MONITORED BY GCA CORPORATION PERSONNEL
Standard Conditions
2lbid.
68°F (20°C) and 29.92 inches (760 mm) mercury, dry basis.
-1*7-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
TABLE 4
Crusher Scrubber Outlet Duct
SUMMARY OF TEST DATA
Test Data
Test Run Number J 2 3
Test Date 9-27-79 9-27-79 9-27-79
Test Period 1800-1940 2119-2259 0005-0145
Sampling Data
Sampling Duration, minutes 96-0 96.0 96.0
Nozzle Diameter, inches 0.250 0.250 0.250
Barometric Pressure, inches mercury 21).Ik 24.74 24.74
Average Orifice Pressure Differential, inches water '-08 1.04 1.01
Average Dry Gas Temperature at Meter, °F 101. 102. 98.
Total Water Collected by Train, ml 15.0 14.0 10.5
standard Volume of Water Vapor Collected, cubic feet 0-71 0.66 0.50
Dry Gas Meter Calibration Factor, dimensionless 0.986 0.986 0.986
Sample Volume at Meter Conditions, cubic feet 61.08 61.09 60.18
Sample Volume at Standard Conditions, cubic feet' 47.02 46.92 46.57
Gas Stream Composition
C02. percent by volume 0.0 0.0 0.0
02, percent by volume 20.9 20.9 20.9
CO, percent by volume 0.0 0.0 0.0
N2, percent by volume 79.1 79.1 79.1
Moisture in Gas Stream, percent by volume '.5 1.4 1.1
Mole Fraction of Dry Gas 0.985 0.986 0.989
Molecular Weight of Dry Gas . 28.97 28.97 28.97
Molecular Weight of Wet Gas . 28.81 28.82 ' . 28.85
Gas Stream Velocity and Volumetric Flow
Static Pressure, inches water 0.19 0.19 0.19
Absolute Pressure, inches mercury . 24.75 24.75 24.75
Average Temperature, °F 74. 72. 71.
Pitot Tube Calibration Coefficient, dimensionless 0.855 0.855 0.855
Total Number of Traverse Points 48.0 48.0 48.0
Velocity at Actual Conditions, feet/second 31.9 31.4 30.8
Stack/duct Cross-Sectional Area, square feet 9.17 9.17 9.17
Volumetric Flow at Actual Conditions, cubic feet/minute - 17,500. 17,300. 16,900.
Volumetric Flow at Standard Conditions, cubic feet/minute 14,100. 14,000. 13,800.
Percent Isokinetic
93.2 94.0 94.8
Unit/Process Operations Data MONITORED BY GCA CORPORATION PERSONNEL
'standard Conditions = 68°F (20°C) and 29-92 inches (760 mm) mercury, dry basis.
Ibid. -48-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
TABLE 5
Fine Ore Bins Scrubber Outlet Duct
SUMMARY OF TEST DATA
Test Data
Test Run Number
Test Date
Test Period
Sampling Data
Sampling Duration, minutes
Nozzle Diameter, inches
Barometric Pressure, inches mercury
Average Orifice Pressure Differential, inches water
Average Dry Gas Temperature at Meter, °F
Total Water Collected by Train, ml
-tandard Volume of Water Vapor Collected, cubic feet
Dry Gas Meter Calibration Factor, dimensionless
Sample Volume at Meter Conditions, cubic feet
Sample Volume at Standard Conditions, cubic feet'
Gas Stream Composition
C02, percent by volume
02, percent by volume
CO, percent by volume
NZ, percent by volume
Moisture in Gas Stream, percent by volume
Mole Fraction of Dry Gas
Molecular Weight of Dry Gas
Molecular Weight of Wet Gas
Gas Stream Velocity and Volumetric Flow
Static Pressure, inches water
Absolute Pressure, inches mercury
Average Temperature, °F
Pitot Tube Calibration Coefficient, dimensionless
Total Number of Traverse Points
Velocity at Actual Conditions, feet/second
Stack/duct Cross-Sectional Area, square feet
Volumetric Flow at Actual Conditions, cubic feet/minute
Volumetric Flow at Standard Conditions, cubic feet/minute
Percent Isoklnetic
9-28-79
1855-2005
64.0
0.183
24.77
1.53
79.
ll.l
0.52
0.995
1(8.07
38.98
0.0
20.9
0.0
79.1
1.3
0.987
28.97
28.82
1.1
24.85
69.
0.850
32.0
63-5
0.79
2990.
2450.
107.0
9-28-79
2122-2236
64.0
0.183
24.77
1.61
72.
10.0
0.47
0.995
47.54
39.07
0.0
20.9
0.0
79.1
1.2
0.988
28.97
28.85
1.1
24.85
64.
0.850
32.0
65.0
0.79
3060.
2530.
103-6
3
9-28-79
2331-0040
64.0
0.183
24.77
1-39
70.
8.6
0.41
0.995
44.23
36.47
0.0
20.9
O.o
79.1
1.1
0.989
28.97
28.85
1.1
24.85
63.
0.850
32.0
58.9
0.79
2770.
2300.
106.4
Unit/Process Operations Data
MONITORED BY GCA CORPORATION PERSONNEL
Standard Conditions
2lbid.
68°F (20°C) and 29-92 inches (760 mm) mercury, dry basis.
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
TABLE 6
Fine Ore Bins Scrubber Inlet Duct
SUMMARY OF TEST DATA
Test Data
Test Run Number
Test Date
Test Period
SamplIng Data
Sampling Duration, minutes
Nozzle Diameter, inches
Barometric Pressure, inches mercury
Average Orifice Pressure Differential, inches water
Average Dry Gas Temperature at Meter, °F
Total Water Collected by Train, ml
standard Volume of Water Vapor Collected, cubic feet
Dry Gas Meter Calibration Factor, dimensionless
Sample Volume at Meter Conditions, cubic feet
Sample Volume at Standard Conditions, cubic feet'
Gas Stream Composition
C02. percent by volume
02, percent by volume
CO, percent by volume
N2, percent by volume
Moisture in Gas Stream, percent by volume
Mole Fraction of Dry Gas
Molecular Weight of Dry Gas
Molecular Weight of Wet Gas .
Gas Stream Velocity and Volumetric Flow
Static Pressure, inches water
Absolute Pressure, inches mercury
Average Temperature, °F
Pilot Tube Calibration Coefficient, dimensionless
Total Number of Traverse Points
Velocity at Actual Conditions, feet/second
Stack/duct Cross-Sectional Area, square feet
Volumetric Flow at Actual Conditions, cubic feet/minute 2
Volumetric Flow at Standard Conditions, cubic feet/minute
Percent Isokinetic
9-28-79
1848»2002
60.0
0.188
2lt. 77
1.82
89.
8.0
0.38
0.998
48.38
38.69
0.0
20,9
0.0
79.1
1.0
0.990
28.97
28.86
-7,2
24.24
72.
0.81(9
20.0
71.0
0.55
2320.
1850.
98.6
9-28-79
2125-2238
60.0
0.188
24.77
1.93
84.
8.0
0.38
0.998
49.43
39.88
0.0
20.9
0.0
79.1
0.9
0.991
28.97
28.87
-7.5
24.22
64.
0.849
20.0
72.1
0.55
2360.
1910.
98.6
3
9-28-79
2328-0038
60.0
0.188
24.77
1.86
83.
8.0
0.38
0.998
48.17
38.89
0.0
20.9
0.0
79-1
1.0
0.990
28.97
28.86
-7.1
24.25
61.
0.849
20.0
70.8
0.55
2320.
1880,
97.3
Unit/Process Operations Data
MONITORED BY GCA CORPORATION PERSONNEL
'standard Conditions = 68°F (20°C) and 29-92 inches (760 mm) mercury, dry basis.
•Ibid.
-50-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
TABLE 7
Fine Ore Bins Hopper Exhaust Duct
SUMMARY OF TEST DATA
Test Data
Test Run Number
Test Date
Test Period
SampI ing Data
Sampling Duration, minutes
Nozzle Diameter, inches
Barometric Pressure, inches mercury
Average Orifice Pressure Differential, inches water
Average Dry Gas Temperature at Meter, °F
Total Water Collected by Train, ml
.tandard Volume of Water Vapor Collected, cubic feet
Dry Gas Meter Calibration Factor, dimensionless
Sample Volume at Meter Conditions, cubic feet
Sample Volume at Standard Conditions, cubic feet'
Gas Stream Composition
C02i percent by volume
02, percent by volume
CO, percent by volume
N2, percent by volume
Moisture in Gas Stream, percent by volume
Mole Fraction of Dry Gas
Molecular Weight of Dry Gas
Molecular Weight of Wet Gas
Gas Stream Velocity and Volumetric Flow
Static Pressure, inches water
Absolute Pressure, inches mercury
Average Temperature, °F
Pitot Tube Calibration Coefficient, dimensionless
Total Number of Traverse Points
Velocity at Actual Conditions, feet/second
Stack/duct Cross-Sectional Area, square feet
Volumetric Flow at Actual Conditions, cubfc feet/minute 2
Volumetric Flow at Standard Conditions, cubic feet/minute
Percent Isokinetic
Unit/Process Operations Data
9-28-79
181(5-2000
64.0
0.250
24.76
1.53
101.
13.5
0.61.
0.986
148.07
37.11
0.0
20.9
0.0
79.1
1.7
0.983
28.97
28.79
-4.7
24.1)1
70.
0.855
16.0
37.2
0.20
44o.
350.
9-28-79
2120-2222
64.0
0.250
24.77
1.55
90.
8.3
0.39
0.986
45.09
35-47
0.0
20.9
0.0
79.1
1.1
0.989
28.97
28.85
-4.2
24.46
66.
0.855
16.0
36.9
0.20
430.
350.
9-28-79
2325-0031
64.0
0.250
24.77
1.33
85.
7.4
0.35
0.986
46.37
36.84
0.0
20.9
0.0
79.1
0.9
0.991
28.97
.28.87
-5.4
24.37
64.
0.855
16.0
34.3
0.20
400.
330.
95.4 99-0 100.9
MONITORED BY GCA CORPORATION PERSONNEL
Standard Conditions
2lbid.
68°F (20°C) and 29-92 inches (760 mm) mercury, dry basis.
-51-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
TABLE 8
Dryer Scrubber Inlet Duct
SUMMARY OF TEST DATA
Test Data
Test Run Number
Test Date
Test Period
SamplIng Data
Sampling Duration, minutes
Nozzle Diameter, inches
Barometric Pressure, inches mercury
Average Orifice Pressure Differential, inches water
Average Dry Gas Temperature at Meter, °F
Total Water Collected by Train, ml
standard Volume of Water Vapor Collected, cubic feet
Dry Gas Meter Calibration Factor, dimensionless
Sample Volume at Meter Conditions, cubic feet
Sample Volume at Standard Conditions, cubic feet'
Gas Stream Composition
C02, percent by volume
02, percent by volume
CO, percent by volume
N2, percent by volume
Moisture in Gas Stream, percent by volume
. Mole Fraction of Dry Gas
Molecular Weight of Dry Gas
Molecular Weight of Wet-Gas
Gas Stream Velocity and Volumetric Flow
Static Pressure, inches water
Absolute Pressure, inches mercury
Average Temperature, °F
Pilot Tube Calibration Coefficient, dimensionless
Total Number of Traverse Points
Velocity at Actual Conditions, feet/second
Stack/duct Cross-Sectional Area, square feet
Volumetric Flow at Actual Conditions, cubic feet/minute
Volumetric Flow at Standard Conditions, cubic feet/minute
Percent Isokinetic
Unit/Process Operations Data
10-1-79
0935-1045
64.0
0.1492
23-98
3-30
132.
327.0
15.39
0.998
67-13
48.33
1.7
4.6
0.0
81.8
24.2
0.758
29.19
26.1(9
-0.36
23-95
595.
0.81(9
16.0
30.A
1.03
1880.
570.
10-1-79
1230-1325
64.0
0.356
23.98
0.82
136.
262.0
12.33
0.998
35.87
25.46
1.7
4.5
0.0
81.9
32.6
0.674
29-19
25.54
-0.34
23.96
595.
0.840
16.0
33.0
1.03
2040
550.
3
10-1-79
1430-1545
64.0
0.356
23.98
O.S9
139.
109.0
5.13
0.998
31-58
22.28
1.7
4.6
0.0
81.9
18.7
0.813
29.18
27.09
-0.46
23.95
595.
0.849
16.0
28.0
1.03
1730.
560.
103.1 107.7 92.1
MONITORED BY GCA CORPORATION PERSONNEL
'standard Conditions = 68°F (20°C) and 29.92 inches (760 mm) mercury, dry basis.
Ibid.
-52-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
TABLE 9
Dryer Scrubber Outlet Duct
SUMMARY OF TEST DATA
Test Data
Test Run Number
Test Date
Test Period
SamplIng Data
Sampling Duration, minutes
Nozzle Diameter, inches
Barometric Pressure, inches mercury
Average Orifice Pressure Differential, inches water
Average Dry Gas Temperature at Meter, °F
Total Water Collected by Train, ml
standard Volume of Water Vapor Collected, cubic feet
Dry Gas Meter Calibration Factor, dimensionless
Sample Volume at Meter Conditions, cubic feet
Sample Volume at Standard Conditions, cubic feet'
Gas Stream Composition •
C02. percent by volume
02, percent by volume
CO, percent by volume
N2, percent by volume
Moisture in Gas Stream, percent by volume
Mole Fraction of Dry Gas
Molecular Weight of Dry Gas
Molecular Weight of Wet Gas
Gas Stream Velocity and Volumetric Flow
Static Pressure, inches water
Absolute Pressure, inches mercury
Average Temperature, °F
Pitot Tube Calibration Coefficient, dimensionless
Total Number of Traverse Points
Velocity at Actual Conditions, feet/second
Stack/duct Cross-Sectional Area, square feet
Volumetric Flow at Actual Conditions, cubic feet/minute .
Volumetric Flow at Standard Conditions, cubic feet/minute
Percent Isokinetic
Unit/Process Operations Data
10-1-79
0939-1052
64.0
0.235
23.98
2.85
107.
144.5
6.80
0.998
65.58
49.38
0.7
5.7
0.0
80.5
12.1
0.879
28.97
27.64
0.9
24.05
131.
0.855
16.0
69.5
0.99
4140.
2620.
2
10-1-79
1226-1339
64.0
0.235
23.98
2.50
119.
170.5
8.03
0.998
62.70
46.05
0.7
5.7
0.0
80.5
14.8
0.852
28.99
27-36
1.03
24.06
137.
0.855
16.0
64.9
0.99
3870.
2340.
3
10-1-79
1439-1550
64.0
0.235
23.98
2.81
119.
118.5
5-58
0.998
66.38
48.79
0.7
5.7
0.0
80.5
10.3
0.897
28.98
27.85 •
1.00
24.05
125.
0.855
16.0
68.0
0.99
4060.
2640.
97.3 101.3 95.3
MONITORED BY GCA CORPORATION PERSONNEL
^Standard Conditions = 68°F (20 C) and 29-92 inches (760 mm) mercury, dry basis.
7
lbid.
-53-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
TABLE 10
Packaging Area Exhaust Duct
SUMMARY OF TEST DATA
Test Data
Test Run Number 323
Test Date 10-1-79 10-1-79 10-1-79
Test Period 0915-1045 1430-1540 1435-1545
SamplIng Data
Sampling Duration, minutes " 64.0 64.0 64.0
Nozzle Diameter, Inches 0.183 0.183 0.183
Barometric Pressure, inches mercury 23.98 23.98 23.98
Average Orifice Pressure Differential, inches water 2.70 2.38 2.49
Average Dry Gas Temperature at Meter, °F 106. 115. 120.
Total Water Collected by Train, ml 17-0 20.2 15-4
standard Volume of Water Vapor Collected, cubic feet 0.80 0.95 0.73
Dry Gas Meter Calibration Factor, dtmenslonless 1.006 1.006 1.006
Sample Volume at Meter Conditions, cubic feet 63.86 61.15 63.01
Sample Volume at Standard Conditions, cubic feet' 48.44 45.64 46.60
Gas Stream Composition
C02. percent by volume 0.0 0.0 0.0
02, percent by volume 20.9 20.9 20.9
CO, percent by volume 0.0 0.0 0.0
N2, percent by volume 79.1 79.1 79.1
Moisture in Gas Stream, percent by volume 1.6 2.0 1.5
Mole Fraction of Dry Gas . 0.984 0.979 0:985
Molecular Weight of Dry Gas . 28.97. 28.97 28.97 .
Molecular Weight of Wet Gas 28.79 28.75 28.80
Gas Stream Velocity and Volumetric Flow
Static Pressure, inches water 2.4 2.5 2.3
Absolute Pressure, inches mercury 24.16 24.16 24.15
Average Temperature, °F 98. 105. 120..
Pltot Tube Calibration Coefficient, dimenslonless 0.855 0.855 0.855
Total Number of Traverse Points 16.0 16.0. 16.0
Velocity at Actual Conditions, feet/second 92.6 88.0 91.1
Stack/duct Cross-Sectional Area, square feet 0.21 0.21 0.21
Volumetric Flow at Actual Conditions, cubtc feet/minute 1180. 1120. 1160.
Volumetric Flow at Standard Conditions, cubic feet/minute 890. 830. 860.
Percent Isokinetic
99.3 100.1 99.2
Unit/Process Operations Data
MONITORED BY GCA CORPORATION PERSONNEL
'standard Conditions • 68°F (20°C) and 29-92 Inches (760 mm) mercury, dry basis.
Ibid.
-54-
-------
Test Data
EXXON MINERALS COMPANY, U..S.A.
Converse County, Wyoming
Table 11
Crusher Transfer Point Exhaust Duct
Summary of Test Results
Test Number
Test Date
Test Time
Gas Flow
Standard Cubic Feet/minute, dry
Acutal Cubic Feet/minute, wet
Particulates
Nozzle and Front Half Filter Holder
Catch Fraction, g
Filter Catch Fraction, g
Total Particulates, g
Particulate Emissions
2
Grains/dry standard cubic foot
Pounds/hour
1
9/27/79
1735-1940
2
9/27/79
2058-2245
3
9/27/79
2355-0138
1,050.
1,300.
0.0044
0.002
0.021
1,010.
1,240.
0.0060
0.003
0.029
970.
1,200.
0.0306
0.0019
0.0063
0.0026
0.0086
0.0010
0.0316
0.013
0.107
Visible Emissions
3
5 percent opacity, minutes observed 0
0 percent opacity, minutes observed 118
Unobserved readings, minutes observed 0
0
102
0
0
98
0
1
Based on Total Particulates captured by train.
Standard Conditions = 68°F and 29-92 inches mercury.
Opacity results listed are in minutes of the observed reading during the test period.
-55-
-------
EXXON-MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 12
Crusher Scrubber Inlet Duct
Summary of Test Results
Test Data
Test Number 1 2 3
Test Date 9/27/79 9/27/79 9/27/79
Test Time 1750-1917 2120-2308 2l»00-OHt9
Gas Flow
Standard Cubic Feet/minute, dry 7,100. 7,510. 6,870.
Actual Cubic Feet/minute, wet 8,890. 9,320. 8,^70.
Particulates
Nozzle and Front Half Filter Holder
Catch Fraction, g 0.0256 0.0157 0.0111
Filter Catch Fraction, g 0.0137 0.0156 0.0071
Total Particulates, g 0,0393 0.0313 0.0182
Particulate Emissions . .
2
Grains/dry standard cubic foot 0.012 0.009 0.006
Pounds/hour 0.7^2 0.562 0.3^1
Based on Total Particulates captured by train.
Standard Conditions = 68°F and 29.92 inches mercury.
-56-
-------
Test Data
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 13
Crusher-Grizzley Exhaust Duct
Summary of Test Results
Test Number
Test Date
Test Time
Gas Flow
Standard Cubic Feet/minute, dry
Actual Cubic Feet/minute, wet
Particulates
Nozzle and Front Half Filter Holder
Catch Fraction, g
Filter Catch Fraction, g
Total Particulates, g
Particulate Emissions
2
Grains/dry standard cubic foot
Pounds/hour
1
9/27/79
1751-19*5
2,370.
2,960.
0.008
0.168
2
9/27/79
2112-2258
2,580.
3,200.
3
9/27/79
0001-0139
2,590.
3,180.
0.01^
0.0102
0.02A6
0.0265
0.0091
0.0356
0'.OA03
0.0059
O.OA62
0.010
0.229
0.013
0.298
Visible Emissions3
5 percent opacity, minutes observed 0
0 percent opacity, minutes observed 76
Unobserved readings, minutes observed 0
0
102
0
0
96
0
1
Based on Total Particulates captured by train.
Standard Conditions = 68 F and 29-92 inches mercury.
3
Opacity results listed are in minutes of the observed reading during the test period.
-57-
-------
EXXON MINERALS COMPANY,.U.S.A.
Converse County, Wyoming
Table 14
Crusher Scrubber Outlet Duct
Summary of Test Results
Test Data
Test Number 1 2 3
Test Date 9/27/79 9/27/79 9/27/79
Test Time 1800-1940 2119-2259 0005-0145
Gas Flow
Standard Cubic Feet/minute, dry 14,100. 14,000. 13,800.
Actual Cubic Feet/minute, wet 17,500. 17,300. 16,900.
Particulates
Nozzle and Front Half Filter Holder
Catch Fraction, g 0.0060 0.0138 0.0101
Filter Catch Fraction, g 0.0013 0.0010 0.0013
Total Particulages, g 0.0073 0.0148 0.0114
Particulate Emissions
2
Grains/dry standard cubic foot 0.002 0.005 0.004
Pounds/hour^ 0.146 0.314 0.223
Scrubber Particulate Removal
Efficiency, percent 80.3 44.1 34-.6
Visible Emissions
5 percent opacity, minutes observed 0
0 percent opacity, minutes observed 69
Unobserved readings, minutes observed 0 ---
Based on Total Particulates captured by train.
fy
Standard Conditions = 68°F and 29-92 inches mercury.
Due to high cyclonic flows at the outlet, emissions were
calculated using inlet flows.
^
Opacity results listed are in minutes of the observed reading
during the test period.
-58-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 15
Fine Ore Bins Scrubber Outlet Duct
Summary of Test Results
Test Data
Test Number 12 3
Test Date 9/28/79 9/28/79 9/28/79
Test Time 1855-2005 2122-2236 2331-00^0
Gas Flow
Standard Cubic Feet/minute, dry 2,^50. 2,530. 2,300.
Actual Cubic Feet/minute, wet 2,990. 3,060. 2,770.
Particulates
Nozzle and Front Half Filter Holder
Catch Fraction, g 0.0056 0.00^9 0.0042
Filter Catch Fraction, g 0.0011 0.0014 0.0015
Total Particulates, g 0.0067 0.0063 0.0057
Particulate Emissions . . .
2
Grains/dry standard cubic foot 0.003 0.002 0.002
Pounds/hour3 0.0*f2 O.OM 0.039
Scrubber Particulate Removal
Efficiency, percent 52.8 28.1 kO.O
Visible Emissions^"
5 percent opacity, minutes observed 0 ---
0 percent opacity, minutes observed 60 ---
Unobserved readings, minutes observed 0 —-
Based on Total Particulates captured by train.
Standard Conditions = 68°F and 29.92 inches mercury.
Due to high cyclonic flows at the outlet, emissions were
calculated using inlet flows.
Opacity results listed are in minutes of the observed reading
during the test period.
-59-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 16
Fine Ore Bins Scrubber Inlet Duct
Summary of Test Results
Test Data
Test Number 12 3
Test Date 9/28/79 9/28/79 9/28/79
Test Time 1848-2002 2125-2238 2328-0038
Gas Flow
Standard Cubic Feet/minute, dry 1,850. 1,910. 1,880.
Actual Cubic Feet/minute, wet 2,320. 2,360. 2,320.
Particulates
Nozzle and Front Half Filter Holder
Catch Fraction, g 0.0103 0.0067 0.0086
Filter Catch Fraction, g 0.0039 0.0023 1 0.0016
Total Particulates, g 0.0142 0.0090 0.0102
Particulate Emissions
2
Grains/dry standard cubic foot 0.006 0.003 0.004
Pounds/hour _ 0.089 0.057 0.065
Visible Emissions
5 percent opacity, minutes observed 000
0 percent opacity, minutes observed 75 75 67
Unobserved readings, minutes observed 0 0 0
Based on Total Particulates captured by train.
f\
Standard Conditions = 68 F and 29.92 inches mercury.
Opacity results listed are in minutes of the observed reading during the test period.
-60-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 17
Fine Ore Bins Hopper Exhaust Duct
Summary of Test Results
Test Data
Test Number 1 2 3
Test Date 9/28/79 9/28/79 9/28/79
Test Time 18A5-2000 2120-2222 2325-0031
Gas Flow
Standard Cubic Feet/minute, dry 350. 350. 330.
Actual Cubic Feet/minute, wet MO. ^30. AOO.
Particulates
Nozzle and Front Half Filter Holder
Catch Fraction, g 0.0065 0.0052 0.0057
Filter Catch Fraction, g 0.0012 0.0009 O.OOTt
Total PartTculates, g 0.0077 0.0061 0.0071
Particulate Emissions
Grains/dry standard cubic foot2 0.003 0.003 0.003
Pounds/hour 0.010 0.008 0.008
Visible Emissions
5 percent opacity, minutes observed 000
0 percent opacity, minutes observed 82 AO 65
Unobserved readings, minutes observed 000
Based on Total Particulates captured by train.
A
Standard Conditions = 68°F and 29.92 inches mercury.
Opacity results listed are in minutes of the observed reading during the test period.
-61-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 18
Dryer Scrubber Inlet Duct
Summary of Test Results
Test Data
Test Number 1 2 3
Test Date 10/1/79 10/1/79 10/1/79
Test TTme 0935-1045 1230-1325 1430-15^5
Gas Flow
Standard Cubic Feet/minute, dry 570. 550, 560.
Actual Cubic Feet/mtnute, wet 188°- 2,040. 1,730.
Particulates
Nozzle and Front Half Filter Holder
Catch Fraction, g 1.2^38 0.7097 0.1*629
Filter Catch Fraction, g 6.6719 4.7913 0.8368
Total Particulates, g 7-9157 5-5010 1-2997
Particulate Emissions
Grains/dry standard cubic foot2 2.527 3-335 0-900
Pounds/hour 12.W \5-lS A.35
Based on Total Particulates captured by train.
f*
Standard Conditions = 68°F and 29.92 inches mercury.
-62-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 19
Dryer Scrubber Outlet Duct
Summary of Test Results
Test Data
Test Number
Test Date
Test Time
Gas Flow
Standard Cubic Feet/minute, dry
Actual Cubic Feet/minute, wet
Particulates
Nozzle and Front Half Filter Holder
Catch Fraction, g
Filter Catch Fraction, g
Total Particulates, g
Particulate Emissions
2
Grains/dry standard cubic foot
Pounds/hour
Scrubber Particulate Removal
Efficiency, percent
Visible Emissions
15 percent opacity, minutes observed
10 percent opacity, minutes observed
5 percent opacity, minutes observed
0 percent opacity, minutes observed
Unobserved readings, minutes observed
1
10/1/79
0939-1052
2,620.
if, 140.
0.2875
0.1135
0.4010
0.125
2.81
77.6
0
0
8-1/2
55-1/2
0
2
10/1/79
1226-1339
2,340.
3,870,
0.0952
0.0563
0.1515
0.051
1.02
93-5
3/4
7-3/4
36-3/4
25-1/2
0
3
10/1/79
1439-1550
2,640.
4,060.
0.0219
0.0628
0.0847
0.027
0.61
86.0
0
0
3/4
64-1/4
0
1
Based on Total Particulates captured by train.
Standard Conditions = 68°F and 29.92 inches mercury.
Opacity results listed are in minutes of the observed reading during the test period.
-63-
-------
EXXON. MINERALS C.OMPANY , U.S.A.
Converse County, Wyoming
Table 20
Packaging Area Exhaust Duct
Summary of Test Results
Test Data
Test Number 1 2 3
Test Date 10/1/79 10/1/79 10/1/79
Test Time 0915-1045 1430-1540 1435-1545
Gas Flow
Standard Cubic Feet/minute, dry 890. 830. 860.
Actual Cubic Feet/minute, wet 1,180. 1,120. 1,160.
Particulates
Nozzle and Front Half Filter Holder
Catch Fraction, g 0.0113 0.0071 0.0087
Filter Catch Fraction, g 0.0093 0.0031 0.0010
Total Particulates, g 0.0206 0.0102 0.0097
Particulate Emissions
2
Grains/dry standard cubTc foot 0.007 0.003 0.003
Pounds/hour 0.050 0.025 0.023
Visible Emissions
5 percent opacity, minutes observed 000
0 percent opacity, minutes observed 64 63 70
Unobserved readings, minutes observed 000
Based on Total Particulates captured by train.
^
Standard Conditions = 68°F and 29.92 inches mercury.
Opacity results listed are in minutes of the observed reading during the test period.
-6k-
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
TABLE 21
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: September 28, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Crusher Transfer Point
Exhaust Duct
Traverse Point No. Sampled: X-3
Pbar (in- Hg.) 24.77
Stack Temp (°F) 72.
Sample Time (min) 75.
Sample Volume (cf) 43.65
Moisture (% H20) 1.1
Meter TemO (°F) 83.
Flow Setting, &H 0.97
(in. H20)
Nozzle Diameter (in.) 0.242
Sample
Plate
No.
1
2
3
4
5
6
7
8
Flow Rate (at
Net Wt.
(mg)
0.5 .
0.4
0.5
0.4
0.3
0.6
0.5
0.4
stack condi tions) :
%
11.9
9-5
11.9
9-5
7.1
14.3
11.9
9-5
0.62 cfm
Cumulative
100.0
88.1
78.6
66.7
57.2
50.1
35.8
23.9
EAD
(Microns)
13.5
8.55
5.65
4.0
2.5
1.3
0.80
0.54
Backup
Filter 0.6
14.3
14.3
TOTAL
4.2-
-65-
-------
Crusher Transfer Point Exhaust Duct
Run 1
cr>
ON
I
crons
MIC PARTICLE DIAMETER
EFFECTIVE AERODY
10.0
9.0
8.0
7.0
6.0
5.0
4.0
3.0
2.0
OOOOOOO—
VjJ .p- VI <7\ -~J OOVJO O
O
N5
0.1
0.01 "0.05 0. I 0.2 0.5 1
10 20 30 40 50 60 70 BO
CUMULATIVE PERCENTAGE
90
95
98 99
99.1 99.9
99.99
by weight^- diameter)
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
TABLE 22
PARTICLE SIZE DISTRIBUTION
Run: 2
Date: September 28, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Crusher Transfer Point
Exhaust Duct
Traverse Point No. Sampled: X-4
bar " -
Stack Temp (°F)
Sample Time (min)
Sample Volume (cf)
Moisture (% H20)
Meter TemO (°F)
24.76
72.
90.
57-87
1.2
91.
1.05
Flow Setting,AH
(in. H20)
Nozzle Diameter (in.) 0.242
Sample Flow Rate (at stack-conditions): 0.63 cfm
Cumulative
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
0.6
0.8
0.5
0.3
1.2
1.0
0.5
0.6
10.3
13.8
8.6
5.2
20.7
17.2
8.6
10.3
1 00 .^0
89.7
75-9
67-3
62.1
41.4
24.2
15.6
EAD
(Microns)
13.2
8.4
5.5
3-8
2.5
1.25
0.78
0.52
Backup
Filter 0.3
5-2
5.2
TOTAL
5.8
-67-
-------
Crusher Transfer Point Exhaust Duct
Run 2
I
cr>
co
i
EFFECTIVE AERODYNAMIC PARTICLE DIAMETER, microns
O O OOOOOOO— NS VjJ .p- VI ON ^J OOVO C
— NJ V*> .p- \J1 ON ^J OOVD O O O OOOOOOC
/
•/
/
/
f
f
/
/
»
/
I
•
/
/
»
•
/
/
I
4
/
/
y
0.01 0.05 0. I 0.2 0.5 I
10 20 30 40 50 80 70 BO
CUMULATIVE PERCENTAGE
90
95
96 99
99.1 99.9
99.99
(% by weight < diameter)
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
. TABLE 23
PARTICLE SIZE DISTRIBUTION
Run: 3
Date: September 28, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Crusher Transfer Point
Exhaust Duct
Traverse Point No. Sampled: X-A
Pbar (in. Hg.) 2A.76
Stack Temp (°F) 72.
Sample Time (min) 90.
Sample Volume (cf) 56.83
Moisture (% H20) 1.8
Meter TemO (°F) 88.
Flow Setting,4H
(in. H20) 1-05
Nozzle Diameter (in.) 0.2^2
Sample Flow Rate (at stack conditions).: 0.63 cfm
Plate
No.
1
2
3
k
5
6
7
8
Net Wt.
(mg)
0.7
0.3
0.5
0.7
1.0
0.5
0.5
0.7
Backup
Filter
0.6
12.7
5.5
9.1
12.7
18.2
9-1
9.1
12.7
10.9
Cumulative
%
100.0
87.3
81.8
72.7
60.0
1*1.8
32.7
23.6
10.9
EAD
(Microns)
13.2
8.1*
5.5
3.8
2.5
1.25
0.78
0,52
TOTAL
5.5
-69-
-------
Crusher Transfer Point Exhaust Duct
Run 3
-oz-
EFFECTIVE AERODYNAMIC PARTICLE DIAMETER, microns
o o ooooooo— to VAj.p-vnaN^j co^oo
—t ro \jo .£- \ji cr> ^j OO^D o o o ooooooo
/
4
/
/
*
»
•
/
/
1
1 /
V
A
*
0.01 0.05 0. I 0.2 0.5 I
10 20 30 40 50 60 70 BO 90
CUMULATIVE PERCENTAGE
95
96 99
99.1 99.9
99.99
by weight < diameter)
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 2k
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: September 27, 1979
Location: Exxon Mineral Company
Sampling Location: Crusher Scrubber Inlet Duct
Traverse Point No. Sampled: X~16
Pbar (in. Hg.) 24.75
Stack Temp (°F) 73-
Sample Time (min) 60.
Sample Volume (cf) .^9.17
Moisture (% H20) 1.3
Meter Temp (°F) 9A.
Flow Setting, J± H 1.8
(in. H20)
Nozzle Diameter (in.) 0.250
Sample Flow Rate (at stack conditions);- -0.81 cfm
Plate
No.
1
2
3
k
5
6
7
8
Net Wt.
(mg)
1.0
0.8
0.6
0.5
0.8
1.0
1.0
1-3
%
12.0
9-6
7-2
6.0
9.6
12.1
12.1
15.7
Cumulative
100.0
88.0
78.3
71.1
65.1
55.5
31.3
EAD
(Microns)
11.7
7-5
5.0
3.5
2.2
1.1
0.67
0.45
Backup
Filter
1.3
15-7
15.7
TOTAL
8.3
-71-
-------
CRUSHER SCRUBBER INLET DUCT
Run 1
EFFECTIVE AERODYNAMIC PARTICLE DIAMETER, microns
O O OOOOOOO— NJ V*> -C~ VJ1 C^ ^J OOVO C
— . M \jj jr- vn cr> ~-J oovo o o o ooooooc
'
/
/
f
J
/
I
1
%
1.
-------
EXXON MINERALS COMPANY, .U.S.A.
Converse County, Wyoming
Table 25
PARTICLE SIZE DISTRIBUTION
Run: 2
Date: September 28, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Crusher Scrubber Inlet Duct
Traverse Point No. Sampled: X-16
('"• H9-) 2k.75
Stack Temp (°F) 73.
Sample Time (min) 70.
Sample Volume (cf) kJ.Qk
Moisture (% HzO) 1.6
Meter Temp (°F) 80.
Flow Setting, AH 1.8
(in. H20)
Nozzle Diameter .(in.-) 0.250
Sample Flow Rate (at stack conditions): 0.69 cfm
Plate
No.
1
2
3
1*
5
6
7
8
Net Wt.
(mg)
0.9
0.3
0.6
0.8
1.1
1.2
1.2
0.8
%
10.9
3-6
7.2
9.6
13.3
14.5
14.5
9-6
Cumulative
%
100.0
89-2
85.6
78. i»
68.8
55.5
41.0
26.5
EAD
(Microns)
12.7
8.05
5.3
3.75
2.35
1.2
0.74
0.50
Backup
Filter
TOTAL
8.3
16.9
16.9
-73-
-------
CRUSHER SCRUBBER INLET DUCT
Run 2
1 U * V
O Q
8 0
7 0
S c; 0
1_
u
•— Li n
£ H.U
P^. in
uj .5 .u
UJ
z:
!^T on
0 ^ ,U
Ul
1 0
no
^ 08
^ n 7
>- u . /
o 06
o o.b
iii
n L
--* U .H
1-
UJ (->7
U. V . 3
LL.
UJ
00
. f.
0.1
•_
.
/
/
I
/.
/
1
t
'
•
/
/•
/
-
0.01 0.05 0. I 0.2 0.5 I 2
10 20 30 40 50 60 70 BO
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 26
PARTICLE SIZE DISTRIBUTION
Run: 3
Date: September 28, 1979
Location: Exxon Minerals Company,. U.S.A.
Sampling Location: Crusher Scrubber Inlet Duct
Traverse Point No. Sampled: X-16
Pbar (in. Hg.) 2^.78
Stack Temp (°F) 73-
Sample Time (min) 70.
Sample Volume (cf) A6.A9
Moisture (% H20) 0.9
Meter Temp (°F) 83.
Flow Setting, AH 1.8
(in. H20)
Nozzle Diameter (in.) ,. 0.250
Sample Flow Rate (at stack conditions)
0.67 cfm
Plate
No.
1
2
3
k
5
6
7
8
Net Wt.
(nig)
0.9
0.5
1.0
0.7
1.6
0.9
1.0
0.6
%
11.it
6.3
12.7
8.9
20.3
11. it
12.7
7.6
Cumulative
%
100.0
88.6 -
82.3
69-7
60.8
itO.6
29.2
16.5
EAD
(Microns)
12.6
8. ^
5. it5
3.75
2. it
1.2
0.76
0.52
Backup
Filter
0.7
8.9
8.9
TOTAL
7-9
-75-
-------
o
u
LU
t-
LU
CJ
O
LU
o
CRUSHER SCRUBBER INLET DUCT
Run 3
2*u
8 n
7 n
A n
c n
L. n
H.U
3n
.U
2n
i n
OQ
• 3
0 8
n 7
n A
Or
O
01,
.H
0-1
. .3
00
0.1
^y
^
/
/
/
/
f
i
r
/
/
;
>y
/
/
/
•
/
/
/
O.Dl 0.05 O.I 0.2 0.5 I 2
10 20 30 40 50 60 70 80
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 27
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: September 27, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Crusher Scrubber Outlet Duct
Traverse Point No. Sampled: X-11
Pbar (in. Hg.) 24.74
Stack Temp (°F) 65.
Sample Time (min) 160.
Sample Volume (cf) 110.48
Moisture (% HzO) 1.4
Meter Temp (°F) 82.
Flow Setting, AH 1.1
(in. H20)
Nozzle Diameter (in.) 0.250
Sample Flow Rate (at stack conditions): 0.68 cfm
Plate
No.-
1
2
3
4
5
6
7
8
Net Wt.
(mg)
0.2
0.2
0.3
0.4
0.7
0.6
0.7
1.0
%
4.2
4.2
6.25
8-3
14.6
12.5
14.6
20.8
Cumulative
%
100.0
95.8
91.6
85-4
77.1
62.5
50.0
35.4
EAD
(Microns)
12.4
8.0
5.35
3.7
2.4
1.2
0.73
0.50
Backup
Filter
TOTAL
0.7
4.8
14.6
14.6
-77-
-------
00
CRUSHER SCRUBBER OUTLET DUCT
Run 1
EFFECTIVE AERODYNAMIC PARTICLE DIAMETER, microns
O O OOOOOOO— N> VjO .p- VJ1 O~* ^»J OOVD C
— • NJ v>J .£- VM O> ^J OOVO O O O OOOOOOC
J
w
/
/
/
/
r
I
/
1
t
I I
L
A
/
y
/
/
/
f
-
-
O.Ol 0.05 0. I 0.2 0.5 I
10 20 3D 40 50 . 60 70 80
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 28
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: September 28, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: _C_rusher-Grizzley
Exhaust Duct
Traverse Point No. Sampled: X-10
Pbar (in. Hg.) 2A.79
Stack Temp (°F) 75.
Sample Time (min) 75.
Sample Volume (cf) 62.22
Moisture (% H20) 1.2
Meter Temp (°F) 117.
Flow Setting, AH 1.7
(in. H20)
Nozzle Diameter (in.) 0.2^1
Sample Flow Rate (at stack conditions): 0.77 cfm
Plate
No. =
1
2
3
k
5
6
7
8
Net Wt.
(mg)
1.1
0.6
0.9
0.5
1.3
1.0
0.9
0.7
%
13-8
7-5
11.3
6.3
16.3
12.5-
11.3
8.8
Cumulative
%
100.0
86.3
78.8
67.5
61.2
^5.0
32.5
21.3
EAD
(Microns)
12.2
7.7
5.3
3.7
2.3
1 .2
0.72
O.i»7
Backup
Filter
1.0
12.5
12.5
TOTAL
8.0
-79-
-------
c
o
o
LU
K
LU
X
O
LU
O
I
oo
o
o
o
(£
o
UJ
LU
10.0
9.0
8.0
7.0
6.0
2.0
1.0
°-2
0.8
0.7
0.6
0.4
0.3
0.2
0.1
CRUSHER-GRIZZLEY. EXHAUST DUCT
Run 1
T
T
0.0! 0.05 0. I 0.2 0.5 I
10 20 3D 40 50 60 70 BO 90
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 29
PARTICLE SIZE DISTRIBUTION
Run: 2
Date: September 28, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Crusher-Grizzley
Exhaust Duct
Traverse Point No. Sampled: X-10
Pbar (in. Hg.) 24.76
Stack Temp (°F) 75.
Sample Time (min) 75.
Sample Volume (cf) 58.14
Moisture (% H20) 0.7
Meter Temp (°F) 87.
Flow Setting, AH 1.7
(in. H20)
Nozzle Diameter (in.) 0.241
Sample Flow Rate (at stack conditions): 0.77 cfm
Plate
No. ...
1
2
3
4
5
6
7
8
Net Wt.
(mg)
1.7
1.2
0.8
0.4
0.7
0.8
0.8
0.6
%
22.1
15.6
10.4
5.2
9.1
10.4
10.4
7.8
Cumulative
*
100.0
77-9
62.3
51.9
46.7
37.6
27.2
16.8
EAD
(Microns)
12.2
7.7
5.3
3.7
2.3
1.2
0.72
0.47
Backup
Filter
0.7
9.1
9-1
TOTAL
7.7
-81-
-------
c
o
u
u
C£
LU
K-
LU
z:
O
<
>-
o
LU
10.0
9.0
8.0
7.0
5.0
1.0
0.9
0.8
0.7
0.6
0.5
0.3
0.2
0.1
CRUSHER-GRIZZLEY EXHAUST DUCT
Run 2
0.01 0.05 0. I 0.2 0.5 1 2
10 20 30 40 SO 60 70 BO
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 30
PARTICLE SIZE DISTRIBUTION
Run: 3
Date: September 28, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Crusher-Grizzley
Exhaust Duct
Traverse Point No. Sampled: X-10
Pbar (in. Hg.) 24.76
Stack Temp (°F) 75.
Sample Time (min) 75.
Sample Volume (cf) 57.41
Moisture (% H20) 0.8
Meter Temp (°F) 88.
Flow Setting, &H 1.7
(in. H20)
Nozzle Diameter (in.) 0.241
Sample-Flow Rate (at stack conditions): 0.76 cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
1.0
0.5
0.4
0.5
1 .2
1.3
0.9
0.8
%
13-2
6.6
5.3
6.6
15.8
17-1
11.8
10.5
Cumulative
%
100.0
86.9
80.3
75.0
68.it
52.6
35.5
23-7
EAD
(Microns)
12.it
7.. 9
5.3
3-7
2.4
1.2
0.73
0.48
Backup
Filter
TOTAL
1.0
7.6
13-2
13.2
-83-
-------
i
oo
CRUSHER-GRIZZLEY EXHAUST DUCT
Run 3
9n
.u
a 0
7 n
/ «u
A n
U) °'U
n R 0
U
— L n
g H.U
•*
P-. 7 n
Ul J .U
UJ
<
~ on
O ^ . U
UJ
_i
u
DC:
2
1 0
LJ *
n Q
— u .3
Z no
? 07
> U . /
o n fi
o o.b
^ AC
< U o
UJ
•~» n L.
-" U .H
O
ui n 7
u. u o
u.
UJ
09
.£
0.1
H'
/
/
4
r
/
•!
,
/
/
/
/•
t
1
/L
&
O.Q! 0.05 0. L 0.2 0.5 1 2
10 20 30 40 50 BO 70 BO 90
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 31
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: September 28, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Fine Ore Bins Scrubber
Outlet Duct
Traverse Point No. Sampled: Y-5
Pbar ('"• H9-) 23.98
Stack Temp (°F) 65.
Sample Time (min) 90.
Sample Volume (cf) 79.80
Moisture (% H20) 1.2
Meter Temp (°F) 85.
Flow Setting, A H 2.2
(in. H20)
Nozzle Diameter (in.) 0.185
Sample Flow Rate (at stack conditions): 0.83 cfm
Plate
No.
1
2
3
k
5
6
7
8
Net Wt;
(mg)
0.1
0.1
0.2
0.3
0.4
0.7
0.8
0.5
%
2.9
2.9
5-9
8.8
11.8
20.6
23-5
14.7
Cumulative
%
100.0
97.1
94.1
88.2
79.4
67.6
47.1
23-5
EAD
(Microns)
11.4
7-1
4.8
3.4
2.1
1.1
0.65
0.45
Backup
Filter
TOTAL
0.3
3-4
8.8
8.8
-85-
-------
FINE ORE BINS SCRUBBER OUTLET DUCT
Run 1
-98-
EFFECTIVE AERODYNAMIC PARTICLE DIAMETER, microns
o o ooooooo— ro vjojrvjioN^j oou> c
_ to »jj Jr- vn C^ ~~1 OOU> O O O OOOOOOC
i
•/
/
/
/
/
•
/
f
/
9
jt
/
f
/
/
/*
/
•
/
/
O.OI 0.05 0. I 0.2 0.5 I 2
ID 20 30 40 50 60 70 80
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 32
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: September 28, 1979
Location: Exxon Mineral's Company, U.S.A.
Sampling Location: Fine Ore Bins Scrubber
Inlet Duct
Traverse Point No. Sampled: X-7
Pbar ('"• H9«) 24.76
Stack Temp (°F) 66.
Sample Time (min) 90.
Sample Volume (cf) 71.78
Moisture (% H20) 1.0
Meter Temp (°F) 83.
Flow Setting, & H 1.85
(in. H20)
Nozzle Diameter (in.) 0.18*
Sample Flow Rate (at stack conditions):- 0-.80 cfm
Plate
No.
1
2
3
k
5
6
7
8
Net Wt.
(mg)
0.6
2.0
3-5
1.1
1.7
2.0
1.1
0.9
%
A. 4
14.7
25-7
8.1
12.5
14.7
8.1
6.6
Cumulative
% ^
100.0
95.6
80.9
55.1
47.1
34.6
19.9
11.8
EAD
(Microns)
11.8
7.4
4.9
3-5
2.2
1.1
0.67
0.^6
Backup
Filter
0.7
5.1
5.1
TOTAL
13-6
-87-
-------
oo
00
FINE ORE BINS SCRUBBER INLET DUCT
Run 1
i • u./
S 06
O U . D
°Z
LU o c
< U">
^ n L
> U . H
LU n 3
tz U<:J
LU
LU
09
. «.
0.1 I
r
rp
rp
M
M
h
n
r j
1
rp
rp
P
P
p
U
M
n
M
M
h
n
D
P
M
t
M
M
H
n
n
n
h
h
n
n
p
p
u
p
p
p
p
n
H
tp
p
p
n
U
h
D
H
M
rp
M
H
n
D
-3
L3
P
n
n
n
n
n
p]
p
p
n
n
n
H
n
pi
rj
p
n
p
H
n
h
M
M
M
M
M
U
n
n
r
tZJ
rp
rp
H
n
h
h
h
PP
tui
tq
rp
M
M
P
P
h
pn
r
rp
rj
P
P
M
H
n
pd
rzj
rp
rj
M
n
n
D
D
i — 1
rp
rj
M
M
h
n
r 3
run
rp
[ZJ
rz
ra
P
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: — i
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rj
n
n
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rd
[7\
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n
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U
m
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p
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n
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a
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0
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n
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rq
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u
H
P
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n
pi
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M
M
M
M
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2_J
P
M
n
H
n
r 3
tzzj
rp
rp
M
M
h
n
c
— n
ZZ:
pi
pj
pi
n
n
P
n
pj
tzd
M
r:
LZ
r
r
L
• — i
rzJ
1
rzJ
rj
P
H
n
i
tii
M
M
P
r
L
zq
rj
M
n
n
n
n
0
M
M
P
P
n
r
r
L
: — i
: 3
—4
nd
3
M
n
H
r_ J
tznj
tP
UP
H
H
P
n
zj
q
n
j
1
1
n
P
n
n
n
n
n
r
L
L -1
: ]
zip
^p
nn
^
i
— i
n
turd
t— 1
tP
PP
M
H
n
0.01 0.05 0. I 0.2 0.5 i 2
10 20 30 40 50 60 70 80
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 33
PARTICLE SIZE DISTRIBUTION
Run: 2
Date: September 30, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Fine Ore Bins Scrubber
Inlet Duct
Traverse Point No. Sampled: x~7
Pbar (in. Hg.)
Stack Temp (°F)
Sample Time (min)
Sample Volume (cf)
Moisture (% H20)
Meter Temp (°F)
Flow Setting, AH
(in. H20)
Nozzle-Diameter (in.)
2*1.76
66.
90.
72.82
0.9
92.
1.85
0.188
Sample Flow Rate (at stack conditions): 0.80 cfm
Plate .
No.
1
2
3
k
5
6
7
8
Net Wt.
(mg)
0.4
0.2
0.5
0.7
0.8
0.5
0.5
0.4
%
9.5
4.8
11.9
16.7
19.0
11.9
11.9
9.5
Cumulative
%
100.0
90.5
85.7
73.8
57.1
38.1
26'. 2
14.3
EAD
(Microns)
11.8
7.4
4.9
3.5
2.2
1.1
0.67
0.46
Backup
Filter
0.2
4.8
4.8
TOTAL
4.2
-89-
-------
I
VD
O
I
FINE ORE BINS SCRUBBER INLET DUCT
Run 2
EFFECTIVE AERODYNAMIC PARTICLE DIAMETER, microns
O O OOOOOOO— NJ \jO .£- \J1 ^J OOVD O
— ro oj .p- \j-i cr> --J OOVD o o o ooooooo
/
^
/
/
/•
/
/
/
x
/
/
/*
ft
0.0! 0.05 0. I 0.2 0.5 I
10 20 30 40 50 60 70 80
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 34
PARTICLE SIZE DISTRIBUTION
Run: 3
Date: September 30, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Fine Ore Bins Scrubber
Inlet Duct
Traverse Point No. Sampled X-7
Pbar ('"• H9«)
Stack Temp (°F)
Sample Time (min)
Sample Volume (cf)
Moisture (% H20)
Meter Temp (°F)
Flow Setting, AH
(in. H20)
Nozzle Diameter (in.)
24.76
g£.
35.
68.54
1.0
81 .
1 .85
0.1 8£
Sample Flow Rate (at stack conditions): 0.81 cfm
Plate
No.
1
2
3
k
5
6
7
8
Net Wt.
(mg)
0.9
0.6
1.0
0.3
1.5
0.7
0.7
0.6
%
13-2
8.8
14.7
4.4
22.1
10.3
10.3
8.8
Cumulative
%
100.0
86.8
77-9
63.2
58.8
36.8
26.5
16.2
EAD~
(Microns)
11.8
7. A
A. 9
3-5
2.2
1.1
0.67
0.1*6
Backup
Filter
0.5
TOTAL
6.8
-91-
-------
FINE ORE BINS SCRUBBER INLET DUCT
Run 3
-26-
EFFECTIVE AERODYNAMIC PARTICLE DIAMETER, microns
O O. O OOOOOO— Ni VjO .p- \J1 O1^ ^J COU> C
— • M \jo .p- \jn o^ --J OO^O O O O OOOOOOC
/
/
/
/
/
•
/
•
/
•
/
/
/
/
/
/
/
/
/
9
•
1
^
_.
0.01 0.05 0. I 0.2 0.5 1 2
10 20 30 40 SO 80 70 BO
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U..S.A.
Converse County, Wyoming
Table 35
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: September 29, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Fine Ore Bins Hopper
Exhaust Duct
Traverse Point No. Sample'd Center Point
Pbar (in. Hg,) 2k.j6
Stack Temp (°F) 66.
Sample Time (min) 75.
Sample Volume (cf) 59.88
Moisture (% HzO) 1.7
Meter Temp (°F) 8^.
Flow Setting, £ H 1.7
(in. H20)
Nozzle Diameter—(in.) 0.250
Sample Flow Rate (at stack conditions):. 0.77 cfm
Plate
No.
1
2
3
1»
5
6
7
8
Net Wt.
(nig)
0.2
0.3
O.A
0.7
1.0
0.8
0.7
0.5
%
3-9
5.9
7.8
13-7
19.6
15-7
13-7
9-8
Cumulative
%
100.0
96.1
90.2
82.it
68.6
49.0
33-3
19-6
EAD
(Microns)
12.0 and larger
7.5
5.0
3.6
2.2
1.1
0.7
Backup
Filter
0.5
9-8
9.8
TOTAL
5.1
-93-
-------
FINE ORE BINS HOPPER EXHAUST DUCT
Run 1
EFFECTIVE AERODYNAMIC PARTICLE DIAMETER, microns
w jr en o> -J OOU> o
o o o pp poo- £ . bob bob
° k^_ C, > " o^ o°^o ° ° •
, '
I p
rp
M
M
M
n
n
n
3
r 1
1
rp
M
M
U
p
ll
n
r
n
n
n
p
p
p
p
p
n
H
D
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M
n
h
M
p
n
n
P
P
P
P
n
h
H
p
^q
zd
P
n
n
U
h
D
rj
rz
M
M
n
n
p
]
rn
rj
M
r
h
M
h
h
M
rz
r
M
M
M
H
h
i
rj
p
n
M
h
h
h
UP
M
M
P
n
P
p
i
rp
rl
M
M
n
h
U
h
rr
rz
rp
P
P
h
G
D
r
r
rp
M
P
P
M
n
n
r
tzJ
rp
M
M
M
n
h
D
i — i
tn:
rp
rn
H
P
pi
U
n
n
tin
rp
M
rp
n
n
M
~n
zj
nj
ll
n
n
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D
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M
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N
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h
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rz
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h
M
h
h
D
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IJ
ll
n
n
n
G
p
h
M
M
G
rn
M
n
n
M
h
h
U
H
M
n
h
M
n
M
D
— i
rj
p
n
n
M
h
H
1
M
M
M
n
n
H
D
ZZ1
ZIJ
HI
ZJ
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n
n
^
U
rn
M
M
rj
n
n
n
H
D
: — i
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nl
^q
rq
d
/
n
n
r d
\~\
rn
M
H
n
U
c
:
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u2
3
n
n
M
r~J,
i
pi
t-
rz
r
L
i
[HJ
aJ
rn
M
n
n
n
—
[
rz:
M
t
t
r
L
zn
rj
M
n
n
n
M
U
0
M
M
M
n
h
L
i
L
- n
pp
dJ
tzq
M
n
H
n
j
r 3
pp
pp
rn
M
p
r
Z]
IJ
n
n
n
1
1
n
P
n
r
h
r
L
L
I
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1
:
up
pp
n
n
n
h ]
LZZZJ
rnzj
fZZJ
t^
n
n
0.01 0.05 0. I 0.2 0.5 I 2
10 20 30 40 50 60 70 80
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 36
PARTICLE SIZE DISTRIBUTION
Run: 2
Date: October 1, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Fine Ore Bins Hopper
Exhaust Duct
Traverse Point No. Sampled: Center Point
Pbar (in. Hg.) 2lt.76
Stack Temp (°F) 55
Sample Time (min) 75f
Sample Volume (cf) 59.78
Moisture (% HzO) 1.1
Meter Temp ( F) gfc.
Flow Setting, AH 1.7
(in. H20)
Nozzle Diameter (in.) 0.250
Sample Flow Rate (at stack conditions): 0.75 cfm
Plate -
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
0.2
0.1
0.3
0.4
0.4
0.7
0.6
0.5
%
5-7
2.9
8.6
11.4
11.4
20.0
17-1
14.3
Cumulative
%
100.0
94.3
91.A
82.8
71.4
60.0
40.0
22.9
EAD
(Microns)
12.1 and larger
7.6
5.1
3.6
2.3
1.2
0.7
0.45
Backup
Filter
0.3
8.6
8.6
TOTAL
3-5
-95-
-------
0
0£
LU
I-
LU
Q
1-
O
LU
10.0
9.0
8.0
7.0
;.o
kO
°'§
0.8
0.7
0.6
OJ
0.2
0.1
FINE ORE BINS HOPPER EXHAUST DUCT
Run 2
T
0.01 0.05 0. I 0.2 0.5 I 2
10 20 30 40 50 80 70 80
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 37
PARTICLE SIZE DISTRIBUTION
Run: 3
Date: October 1, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Fine Ore Bins Hopper
Exhaust Duct
Traverse Point No. Sampled: Center Point
Pbar (in. Hg.) 24.76
Stack Temp (°F) 66.
Sample Time (min) 85.
Sample Volume (cf) . 66.55
Moisture (fc HzO) 0.9
Meter Temp (°F) 81.
Flow Setting, AH 1.7
(in. H20)
Nozzle Diameter-(in.)— 0.250
Sample Flow Rate (at stack conditions): Q.76 cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
0.2
0.1
0.4
0.7
0.9
1.1
0.7
0.5
%
4.2
2.8
8.3
14.6
18.8
22.9
14.6
10.4
Cumulative
% -
100.0
95.8
93.8
85.4
70.8
52.1
29.2
14.6
EAD
(Microns)
12,0
7-5
5.0
3.6
2,2
1.1
0,7
0.45
Backup
Filter
TOTAL
0.2
4.8
4.2
4.2
-97-
-------
in
c
o
u
u
C£
UJ
H
LU
U
{£.
O
Q
O
oc
1-
o
10.0
9.0
8.0
7.0
6.0
5.0
4.0
3.0
2.0
1.0
0.9
0.8
0.6
OJ
1.3
0.2
0.1
FINE ORE BINS HOPPER EXHAUST DUCT
Run 3
T
T
_L
0.0! 0.05 0. I 0.2 0.5 I
10 20 30 40 50 60 70 60 90
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 38
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: October 1, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Dryer Scrubber Outlet
Duct
Traverse Point No. Sampled: X-3
Pbar (in. Hg.)
Stack Temp ( F)
Sample Time (min)
23.98
Sample Flow Rate (at stack conditions): 0.81 cfm
1
2
3
5
6
7
8
Net Wt.
(mg)
1.1
0.7
0.3
0.2
0.4
0.8
0.5
0.3
21.6
13-7
5-9
3.9
7-8
15.7
9.8
5.9
.81 cfm
Sample Volume (wscf)
Moisture (% H20)
Meter Temp (°F)
Flow Setting, & H
(in. H£0)
Nozzle Diameter (in.).
2.42
12.1
108.
1.2
0.188
Cumulative EAD
% (Microns)
100.0
78.4
64.7
58.8
54.9
47-1
31.4
21.6
12.8
8.2
5.4
3.9
2.3
1.2
0.74
0.50
Backup
Filter
0.8
15.7
15.7
TOTAL
5.1
-99-
-------
DRYER SCRUBBER OUTLET DUCT
Run 1
-ooi-
EFFECTIVE AERODYNAMIC PARTICLE DIAMETER, microns
O O OOOOOOO— ts> V*> .p- \J1 ON ^J OOVO C
• • . «»..«•• • » • »•»»»•
— • Is} VjJ .p- \J1 O> ^J OOVO O O O OOOOOOC
)
J
9'
1
/
/
fc
\
•
•
/
•
/
/
•
T
/
0.01 0.05 0. I 0.2 0.5 I
10 20 30 40 50 60 70 80
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 39
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: October 1, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Dryer Scrubber Inlet Duct
Traverse Point No. Sampled: x~10
Pbar (in. Hg.) 23.98
Stack Temp (°F) 587.
Sample Time (min) 2.
Sample Volume(wscf) 1.90
Moisture (% H20) 25.0
Meter Temp (°F) 98.
Flow Setting, A H 2.8
(in. H20)
Nozzle Diameter (in.) 0.^92
Sample Flow Rate . (at stack conditions): 2,35 cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
30.6
22.1
14.1
12.6
3.1*
2.3
3-5
2.6
%
30.5
22.1
H.I
12.6
9.4
2.3
3.5
2.6
Cumulative
%
100.0
69.5
47.4
33-3
20.8
11.4
9.1
5.6
EAD
(Microns)
12.6
8.1
5.5
3.7
2.4
1.2
0.72
0.49
Backup
Filter
3-0
3.0
3.0
TOTAL
100.2
-101-
-------
o
N)
I
DRYER SCRUBBER INLET DUCT
Run 1
1 U . n L
••* U . H
1-
o
LU n -1
U. °O
U.
LU
OO
0.1
•
y
f
/"
/
1
.
/
...
y
/
•/
^
/
^
/
/
«
0.0! 0.05 O.I 0.2 0.5 I 2
10 20 30 40 50 60 70 BO
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 40
PARTICLE SIZE DISTRIBUTION
Run: 2
Date: October 1, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Dryer Scrubber Inlet Duct
Traverse Point No. Sampled: X-10
Pbar (in. Hg.)
Stack Temp (°F)
Sample Time (min)
Sample Volume (wscf)
Moisture (% H20)
Meter Temp (°F)
Flow Setting, A H
(in. H20)
Nozzle Diameter, (in.)
Sample Flow Rate (at stack conditions) ;=2.44 cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt..
(mg)
24.8
26.3
13.0
12.9
7-9
3.4
2.3
2.0
%
25. 9
27.5
13.6
13.5
8.3
3.7
2.4
2.1
Cumulative
%
100.0
74.0
46.5
32.9
19.4
11.1
7.5
5.1
EAD
(Microns)
12.4
8.0
5.4
3-6
2.3
1.2
0.71
0.48
23.98
587.
2.
1.97
25.0
97.
2.8
Backup
Filter
2.9
3.0
3.0
TOTAL
95-5
-103-
-------
DRYER SCRUBBER INLET DUCT
Run 2
o
-C-
1 V/ • \J
9n
«*
8 n
7 n
/ •"
A n
(/> b-u
n ^ 0
U
— L n
E 4.0
Pi 7 n
UJ } .U
LU
<
~r 9 n
O t . U
UJ
_i
u
a:
g
i n
u ' - u. /
o n A
o O.b
^ n q
< u • y
^ n L
^ u .*+
l-
u
uj o -i
u. u • J
u.
LU
09
. /:
0.1
D.
01. O.C
5 0
1 0
.2 0
5
2 £
/
„/
7
/
i
i
'
./
/
0 2
/
/
0 31
/
/
) 41
/
/
/
) 50
/
6
D 7
•„.
D 80
9
D 9
5 91
I 9
e 99.
1 9!
.9 99.
CUMULATIVE PERCENTAGE
[% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse'County, Wyoming
Table 41
PARTICLE SIZE DISTRIBUTION
Run: 3
Date: October 1, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Dryer Scrubber Inlet Duct
Traverse Point No. Sampled: X-10
Pbar (in. Hg.) 23-98
Stack Temp (°F) 587.
Sample Time (min) 1.5
Sample Volume(wscf) 1.24
Moisture (% HzO) 25.0
Meter Temp (°F) 100.
Flow Setting, &H 2.8
(in. H20)
Nozzle Diameter (in.) 0.^92
Sample Flow Rate (at stack conditions): 2.04 cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
29-3
24.7
13.2
9.2
5.9
2.3
1.7
1.2
%
32.7
27.6
U.7
10.3
6.6
2.6
1.9
1.3
Cumulative
%
100.0
67.3
39.7
24.9
14.6
8.0
5-5
3-6
EAD
(Microns)
13-9
8.5
5.7
3.9
2.5
1.3
0.77
0.52
Backup
Filter
TOTAL
2.0
89.5
2.2
2.2
-105-
-------
DRYER SCRUBBER INLET DUCT
Run 3
-901-
EFFECTIVE AERODYNAMIC PARTICLE DIAMETER, microns
O O O OOOOOO— . N* VjO .p- V/l O ~vl OOVO C
— M OJ Jr- vn CJN -^J OO^O O O O OOOOOOC
/
/
;
/
/
9
•I
/
*/
7
/
i
/
/
A
\
/
•
•
i
0.01 0.05 0.I 0.2 0.5 I 2
10 20 30 40. 50 BO 70 80
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 42
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: October 1, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Packaging Area Exhaust
Duct
Traverse Point No. Sampled: Center Point
Pbar (in. Hg.) 23.98
Stack Temp ( F) 104.
Sample Time (min) 55.
Sample Volume (cf) 54.88
Moisture (% H20) 1.6
Meter Temp (°F) 96.
Flow Setting, A H 2.7
(in. H20)
Nozzle-Diameter (in.) - . 0.183
Sample. Flow Rate (at stack conditions): 1.01 cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
1-3
1.6
1.0
1.0
1.9
2.1
1.0
°:9
%
11.7
14.4
9.0
9.0
17.1
18.9
9-0
8.1
Cumulative
%
100.0
88.3
73-9
64.9
55.9
38,7
19.8
10.8
EAD
(Microns)
7.0
4.7
3-3
2.0
0.99
0.65
0.44
Backup
Filter
0.3
2.7
2.7
TOTAL
11.1
-107-
-------
o
oo
i
PACKAGING AREA EXHAUST DUCT
Run 1
EFFECTIVE AERODYNAMIC PARTICLE DIAMETER, microns
o o ooooooo— • 10 v»» .p- vn ON xj covoo
— ro v*> -t- vn ON >j oovo o o o ooooooo
<
J
/
J
/
/
/
I
/
*
1
/
/
t
/
*
f *
0.01 0.05 0.1 0.2 0.5 1
10 20 30 40 50 60 70 80
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 43
PARTICLE SIZE DISTRIBUTION
Run: 2
Date: October
1, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Packaging Area Exhaust
Duct
Traverse Point No. Sampled: Center Point
Sample Flow Rate (at stack
Plate
No.
1
2
3
4
5
6
7
8
Backup
Filter
Net Wt.
(mg) -
1.6 1
1.6 1
0.8
1.0
2.0 1
1.4 1
1.4 1
0.8
1.5 1
conditions) : . 0
.96 cfm
Pbar (in. Hg.)
Stack Temp (°F)
Sample Time (min)
Sample Volume (cf)
Moisture (% H20)
Meter Temp (°F)
Flow Setting, & H
(in. H20)
Nozzle-Diameter (in.)
23.98
104.
55.
50.77
2.0
91.
2.7
0.183
Cumulative EAD
% % (Microns)
3.2
3.2
6.6
8.3
6.5
1.6
1.6
6.6
2.4
100.0
86.8
73.6
66.9
58.7
42.2
30.6
19-0
12.4
11.5
7.2
4.8
3-4
2.2
1.1
0.67
0.45
TOTAL
12.1
-109-
-------
O
I
PACKAGING AREA EXHAUST DUCT
Run 2
9n
• U
8 0
7 0
/ «u
A n
b-u
n ^ 0
u
0
— L n
^ H.U
P-. 7 n
LU j .U
LU
<
~ on
O e. ,\J
LU
_l
O
01
£
i n
C_3 ' *U
n Q
31 08
z 0 -j
>- u. /
o 06
o o.b
w n r
< u . p
^ n L.
•^ U .H
O
LU n 1
U. U • J
U.
LU
09
.£
0.1
1
.
i
/
/
:
/
/
/
r
, ,
/
»
f
/
•,
/
V
/
•
/
/
0.01 0.05 0. I 0.2 0.5 1 2
10 20 30 40 50 60 70 80 90
CUMULATIVE PERCENTAGE
(% by weight
-------
EXXON MINERALS COMPANY, U.S.A.
Converse County, Wyoming
Table 44
PARTICLE SIZE DISTRIBUTION
Run: 3
Date: October 1, 1979
Location: Exxon Minerals Company, U.S.A.
Sampling Location: Packaging Area Exhaust
Duct
Traverse Point No. Sampled: Center Point
Pbar (in. Hg.)
Stack Temp ( F)
Sample Time (min)
Sample Volume (cf)
Moisture (% HzO)
Meter Temp (°F)
Flow Setting, A. H
(in. H20)
Nozzle Diameter (in.)
55.
51.89
1.5
103.
2.7
0.183
Sample Flow Rate (at stack conditions): 0.96 cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
1.0
0.8
1.0
1.3
1.6
1.3
1.2
1.0
%
9.7
7.8
9.7
12.6
15.5
12.6
11.7
9.7
Cumulative
100.0
90.3
82.5
72.8
60.2
44.7
32.0
20.4
HAD
(Microns)
11.5
7-2
4.8
2.2
1.1
0.67
0.45
Backup
Filter
1.1
10.7
10.7
TOTAL
10.3
-111-
-------
c
o
l_
u
o
UJ
N)
i
>-
o
o
cc.
10.0
9.0
8.0
7.0
5.0
l\ .0
1.0
:.o
i.o
0.9
0.8
0.7
0.6
OJ
1.3
o.;
0.1
PACKAGING AREA EXHAUST DUCT
Run 3
r-
T
T
O.QI 0.05 O.I 0.2 0.5 I
10 20 30 40 50 60 70 80 90
CUMULATIVE PERCENTAGE
(% by weight
-------
TABLE 45
SUMMARY OF VISIBLE EMISSIONS
Page 1 of 2
September 27. 1979
Date: ^ _ _
-Type of Discharge: Process Hoods
Height of Point of Discharge: Approx. 12 ft
Wind Direction:
JColor of Plume:
3bserver No. :
Distance from Observer to Discharge Point:
Direction of Observer from Discharge Point: North
Height of Observation Point: Ground Level
Type of Plant: Uranium Mine
Location of Discharge: Grizzley Hood S- Crusher Ent
Description of Sky: Area (TP9 and TP10)
Wind Velocity:
Detached Plume:
Duration of Observation: Approx. 5-3/4 hours
Approx. 25 ft
Jescription of Background: Inside Crusher Building on Ground Level
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
SUMMARY OF AVERAGE OPACITY
Tl
Start
1745
1751
1757
1803
1809
1815
1821
1827
1833
1839
1845
1851
1857
1903
1909
1915
1921
1927
1933
1939
ne
End
1751
1757
1803
1809
1815
1821
1827
1833
1839
1845
1851
1857
1903
1909
1915
1921
1927
1933
1939
1945
Opacity
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Set
Number
21
22
23
2k
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
T
Start
1945
1951
2115
2121
2127
2133
2139
2145
2151
2157
2203
2209
2215
2221
2227
2233
2239
2245
2251
2257
me
End
1951
1953
2121
2127
2133
2139
2145
2151
2157
2203
2209
2215
2221
2227
2233
2239
2245
2251
2257
2303
Opac
Sum
0
0
0
0
0
0
0
0
. 0
0
0
0
0
0
0
0
0
0
0
0
;i ty
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Sketch Showing How Opacity Varied with Time:
Opaci ty
1 hr
2 hr
3 hr
hr
5 hr
6 hr
Time, Hours
-113-
-------
Date: September 27. 1979
TABLE 45
SUMMARY OF VISIBLE EMISSIONS
(continued)
Type of Plant: Uranium Mine
Page 2 of 2
Type of Discharge: Process Hoods
Height of Point of Discharge: Approx. 12 ft
Wind Direction:
Color of Plume:
Observer No. :
Distance from Observer to Discharge Point: Approx. 25 ft
Location of Di scharge:Gr i zzley Hood & Crusher
Description of Sky: Area (TP9 and TP10)
Wind Velocity: _ •_
Detached Plume:
Duration of Observation: Approx. 5 "3/4 hours
Direction of Observer from Discharge Point: North
Height of Observation Point: Ground Level
Description of Background: Inside Crusher Building on Ground Level
Set-
Number
41
42
43
4*»
45
46
47
48
49
50
51
52.
53
5A
55
56
57
58
59
SUMMARY OF AVERAGE OPACITY
Time
Start
2303
0005
0011
0017
0023
0029
0035
0041
0047
0053
0059
0105 .
0111
0117
0123
0129
0135
0141
0147
End
2305
0011
0017
0023
0029
0035
0041
0047
0053
0059
0105
0111
0117
0123
0129
0135
0141
0147
0149
Opacity
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Set
Number
T
Start
me
End
Opacity ^
Sum
Average
'
Sketch Showing How Opacity Varied with Time:
Opaci ty
(*)
Time, Hours
-114-
-------
September 27,
rue": "Process" Hoods
1979
Date:
ype oT"
(eight of Point of Discharge: Approx. 50 ft
Wind Direction:
•*.olor of Plume:
ibserver No.
Type of Plant: Uranium Mine
Page 1 of Z
Location of Discharge; Crusher Transfer Point
Description of Sky:
Wind Velocity: _
Detached Plume:
Distance from Observer to Discharge Point:
Direction of Observer from Discharge Point: __^
'eight of Observation Point: 5 ft Above on Walkway
Jescription of Background: Near crusher transfer point
Duration of Observation: Approx. 5-1A hours
Approx. 50 ft .
Set
Number
1
2
3
k
5
6
7
"8
9
10
11
12
13
U
15
16
17
18
19
20
SUMMARY OF AVERAGE OPACITY
Time
Start
1740
1746
1752
1758
1804
1810
1816
1822
1828
1834
-1840
1846
1852
1858
1:904
1910
1916
1922
1928
1934
End
1746
1752
1758
1804
1810
1816
1822
1828
1834
1840
1846
1852
1858
1904
1910
1916
1922
1928
1934
1938
Opaci ty
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Average
0
0
0
0
0
0
0
0
0
0
0
0.
0
0
0
0
0
0
0
0
Set
Number
21
22
23
2k
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
AO
T
Start
2100
2106
2112
2118
2124
2130
2136
2142
2148
2154
2200
2206
2212
2218
2224
2230
2236
0000
0006
0012
me
End
2106
2112
2118
2124
2130
2136
2142
2148
2154
2200
2206
2212
2218
2224
2230
2236
2242
0006
0012
0018
Opaj
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
pity
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Sketch Showing How Opacity Varied with
Opaci ty
1 hr
2 hr
3 hr
4 hr
5 hr
Time, Hours
-115-
-------
Date: September 2?, 1_979_
Type of Discharge: Process Hoods
TABLE 46
SUKI'.ARY OF VISIBLE EMISSIONS
(continued)
Type of Plant:
Page 2 of 2
Uranium Mine
Height of Point of Discharge: Approx. 50 ft
Wind Direction:
Color of Plume:
Observer No.:
Location of Pischarge;Crusher Transfer Point
Description of Sky:
Wind Velocity:
Detached Plume:
Distance from Observer to Discharge Point:
Direction of Observer from Discharge Point:
Height of Observation Point: 5 ft Above on Walkway
Description of Background:
Duration of Observation: Approx. 5-1A hours
Approx. 50 ft •
Near crusher transfer point
Set
Number
41
42
43
44
45
46
47
48
49
50
51
52
53
5**
SUMMARY OF AVERAGE OPACITY
Time .
Start
0018
0024
0030
0036
0042
0048
0054
0100
0106
0112
0118
0124
0130
0136
End
0024
0030
0036
0042
0048
0054
0100
0106
0112
0118
0124
0130 .
0136
0138
Opacity
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Set
Number
T
Start
me
End
Opa
Sum
pity
Average;
Sketch Showing How Opacity Varied
Opacity
Time, Hours
-116-
-------
TABLE 47
SUMMARY OF VISIBLE EMISSIONS
Date: September 27, 1979
Type of Discharge; Process Hoods
Height of Point of Discharge:
Wind Direction:
Color of Plume:
Observer No. : ^ __
Distance from Observer to Discharge Point:
Direction of Observer from Discharge Point:
Height of Observation PoTnt:
Type of Plant:Uranlum Mine
Page 1 of 2
Location of Discharge: Crusher Grlzzley
Description of Sky:
Wind Velocity:
Detached Plume:
Duration of Observation: Approx. 4-1/2 hours
Approx. 20 ft
Description of'Background: Inside crusher building, 20 ft from hood
Set
Number
1
2
'3
k
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
SUMMARY OF AVERAGE OPACITY
T!
Start
1751
1757
1803
1809
1815
1821
1827
1833
1839
1845
1851
1857
1903
2116
2122
2128
213^
2140
2146
2152
ne
End
1757
1803
1809
1815
1821
1827
1833
1839
1845
1851
1857
1903
1907
2122
2128
2134
2140
2146
2152
2158
Opacity
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0"
0
0
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Set
Number
21
22
23
2k
25
26
27
28
29
30
31
32
33
34 .
35
36
37
38
39
ko
T
Start
2158
2204
2210
2216
2222
2228
2234
2240
2246
2252
0002
0008
0014
0020
0026
0032
0038
0044
0050
0056
me
End
2204
2210
2216
2222
2228
2234
2240
2246
2252
2258
0008
0014
0020
0026
0032
0038
0044
0050
0056
0102
Opa<
Sum
0
0
0
0
0
0
0
0
0
0
0
0
- o
0
0
0
0
0
0
0
;ity
Average
0
0
0
0
0
0
0 .
0
0
0
0
0
0
0
0
0
0
0
0
0
Sketch Showing How Opacity Varied with Time:
Opacity
1 hr
2 hr
3 hr
4 hr
Time, Hours
-117-
-------
September 27. 1979
Date:
Type of Discharge; Process Hoods
TABLE 47
SUMMARY OF VISIBLE EMISSIONS
(continued)
Type of Plant: Uranium Mine
Page 2 of 2
Height of Point of Discharge:
Wind Direction:
Color of Plume:
Observer No.:
Location of Discharge: Crusher Grizzley
Description of Sky:
Wind Velocity:
Detached Plume:
Distance from Observer to Discharge Point; Approx. 20 ft
Direction of Observer from Discharge Point:
Height of Observation Point:
Duration of Observation: Approx. 4-1/2 hours
Description of Background: Inside crusher but!ding, 20 ft from hood
Set
Number
41
42
4'3
4*»
45
46
SUMMARY OF AVERAGE OPACITY
Tl
Start
0102
0108
0114
0120
0126
0132
tie
End
0108
0114
0120
0126
0132
0138
Opacity
Sum
0
0
0
0
0
0
Average
0
0
0
0
0
0
Set
Number
T
Start
me
End
Opa
Sum
pity
Average
Sketch Showing How Opacity Varied with Time:
Opacity
(*)
Time, Hours
-118-
-------
TABLE 48
SUMMARY OF VISIBLE EMISSIONS
Date: September 27, 1979
Type of Discharge: Stack
Height of Point of Discharge: Approx. 120 ft
Wind Direction: JW
Color of Plume: •
Observer No.:
Type of Plant: Uranium Mine
Location of Discharge: Crusher Scrubber Outlet
Description of Sky; Partly Cloudy
Wind Velocity: 5 to 15 mph
Detached Plume:
Duration of Observation: 69 minutes
Distance from Observer to Discharge Point; Approx. 7 ft
Direction of Observer from Discharge Point:
NW
Height of Observation Pofnt: Approx. 5 ft below Up
Description of Background:
Scattered
Set
Number
1
2
'3
k
5
6
7
8
9
10
11
12
SUMMARY OF AVERAGE OPACITY
T!
Start
1804
1810
1816
1822
1828
1834
1840
1846
1852
1858
1904
1910
me
End
1810
1816
1822
1828
1834
1840
1846
1852
1858
1904
1910
1913
Opacity
Sum
0
0
0
0
0
0
0
0
0
0
0
0
Average
0
0
0
0
0
0
0
0
0
0
0
0
Set
Number
T
Start
me
End
Opa<
Sum
;ity
Average
Sketch Showing How Opacity Varied with Time:
Opaci ty
15 mlns. 30 mins. 45 mtns. 60 mlns. 75 mlns.
Time, Minutes
-119-
-------
TABLE 49
SUMMARY OF VISIBLE EMISSIONS
September 28, 1979
Discharge: Transfer Point
Approx. 8 ft
Date:
Type oT
Height of Point of Discharge:
Wind Direction:
Color of Plume:
Observer No.:
Distance from Observer to Discharge Point:
Direction, of Observer from Discharge Point:
Height of Observation Point: '
Description of'Background:
Type of Plant: Uranium Mine
_
Location of Discharge fine Ore Bins Scrubber
Description of Sky: _
Wind Velocity: _
Detached Plume:
Inle!
Duration of Observation:
Approx. 25 ft
Approx. 3-1/2 hours
East
Set
Number
1
2
'3
k
5
6
7
8
9
10
11
12
13
U»
15
16
17
18
19
20
SUMMARY OF AVERAGE OPACITY
Time
Start
1850
1856
1902
1908
1914
1920
1926
1932
1938
1944
1950
1956
2002
2125
2131
2137
2143
2149
2155
2201
End
1856
1902
1908
191^
1920 .
1926
1932
1938
1944
1950
t.956
2002
2005
2131
2137
2143
2149
2155
2201
2207
Opacity
Sum
0
0
.0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Set
Number
21
22
23
2k
25
26
27
28
29
30
31
32
33
34
35
36
37
38
T
Start
2207
2213
2219
2225
2231
2237
2330
2336
2342
2348
2354
2400
0006
0012
0018
0024
0030
0036
me
End
2213
2219
2225
2231
2237
2240
2336
2342
2348
2354
2400
0006
0012
0018
0024
0030
0036
0037
Opa<
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
?ity !
Average ^
i
0 1
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Sketch Showing How Opacity Varied with Time:
Opacity
(*)
1 hr
2 hr
3 hr
4 hr
Time, Hours
-120-
-------
TABLE 50
SUMMARY OF VISIBLE EMISSIONS
Date: September 28, 1979
Type of Plant: Uranium Mine
Type of Discharge; Process Area
Height of Point of Discharge:
Wind Direction:
Color of Plume:
Observer No.:
Location of D?scharge:FIne Ore Bins Hopper Exhaust
Description of Sky: Duct
Wind Velocity:
Detached Plume:
Duration of Observation: Apprpx. 3 hours
Distance from Observer to Discharge Point; Approx. 50 ft
Direction of Observer from Discharge Point:
Height of Observation Point: Eye Level to Source
Description of Background:
Set
Number
1
2
"3
k
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
SUMMARY OF AVERAGE OPACITY
Tt
Start
181*8
1854
1900
1906
1912
1918
1924
1930
1936
1942
1948
1954
2000
2006
2120
2126
2132
2138
2144
2150
me
End
1854
1900
1906
1912
1918
1924
1930
1936
1942
1948
1954
2000
2006
2010
2126
2132
2138
2144
2150
2156
Opacity
Sum
Average
Set
Number
21
22
23
24
25
26
27
28
29
30
31
32
T
Start
2156
2325
2331
2337
2343
2349
2355
0001
0007
0013
0019
0025
me
End
2200
2331
2337
2343
2349
2355
0001
0007
0013
0019
0025
0030
Opa<
Sum
pity
Average
•
• •
i
Sketch Showing How Opacity Varied with Time:
Opacity
(«
1 hr
2 hr
3 hr
Time, Hours
-121-
-------
TABLE 51
SUMMARY OF VISIBLE EMISSIONS
Date: September 28, 1979
Type of Discharge: Stack
Height of Point of Discharge: Approx. 170 ft
Wind Direction: NW
Color of Plume:
Observer No.:
Type of Plant: Uranium Mine
Location of Discharge;Fine Ore Bins Scrubber Out*"
Description of Sky: Clear let Due
Wind Velocity: '5 to 15 mph ;
Detached Plume: (
Duration of Observation: 1 hour
Distance from Observer to Discharge Point: Approx. 35 ft
Direction of Observer from Discharge Point: West
Height of Observation Potnt: Approx. 150 ft
Description of'Background:
Set
Number
1
2
'3
*»
5
6
7
8
9
10
SUMMARY OF AVERAGE OPACITY
Tt
Start
18^5
1851
1857
1903
1909
1915
192T
1927
1933
1939
TIC
End
1851
1857
1903
1909
1915
1921
1927
1933
1939
19^5
Opacity
Sum
0
0
0
0
0
0
0
0
0
0
Average
0
0
0
0
0
0
0
0
0
0
Set
Number
T
Start
me
End
Opa<
Sum
pity
Average
Sketch Showing How Opacity Varied with Time:
Opacity
(*)
20 mins.
kO mins.
60 mins.
Time, Minutes
-122-
-------
TABLE 52
SUMMARY OF VISIBLE EMISSIONS
Date: October 1, 1979
Type of Discharge; Stack
Type of Plant: Uranium Mine
Height of Point of Discharge: Approx. 80 ft
Wind Direction: _SW
Color of Plume:
Observer No. :
Location of Discharge:Dryer Scrubber Outlet Duct
Description of Sky: Clear
Wind Velocity: 10 to 15 mph
Detached Plume:
Distance from Observer to Discharge Point:
Direction of Observer from Discharge Point: South
Height of Observation Point: Approx. 65 ft
Description of Background:
Duration of Observation: Approx. 3-1/4 hours
Approx. 150 ft
Set
Number
1
2
'3
k
5
6
7
8
9
10
11
12
13
U
15
16
17
18
19
20
SUMMARY OF AVERAGE OPACITY
Tl
Start
0930
0936
0942
0948
0954
1000
1006
1012
1018
1024
1030
1230
1236
1242
1248
1254
1300
1306
1312
1318
me
End
0936
0942
0948
0954
1000
1006
1012
1018
1024
1030
1033
1236
1242
1248
1254
1300
1306
1312
1318
1324
Opacity
Sum
70
50
5
0
5
0
0
0
0
0
0
130
85
115
105
105
125
70
70
100
Average
2.9
2.1
0.2
0.0
0.2
0
0
0
0
0
0
5.4
3.5
4.8
4.4
4.4
5.2
2.9
2.9
4.2
Set
Number
21
22
23
2k
25
26
27
28
29
30
31
32
33
3V
T
Start
1324
1330
1336
1430
1436
1442
1448
1454
1500
1506
1512
1518
1524
1530
me
End
1330
1336
1340
1436
1442
1448
1454
1500
1506
1512
1518
1524
1530
1534
Opa<
Sum
95
65
30
5
0
0
0
0
0
0
5
10
0
0
pity
Average
4.0
2.7
1.5
0.2
0 .
0
0
0
0
0
0.2
0.4
0
0
Sketch Showing How Opacity Varied with Time:
Opacity
(*)
30 mfns.
1 hr
30 mlns.
2 hr
30 mins.
3 hr
Time, Hours
-123-
-------
TABLE 53
SUMMARY OF VISIBLE EMISSIONS
Date: October 1, 1979
Type of Plant: Uranium Mine
Type of Discharge; Process Area
Height of Point of Discharge:
Wind Direction:
Color of Plume:
Observer No.:
Location of Discharge: Barreling Enclosure Area
Description of Sky:
Wind Velocity:
Detached Plume:
Duration of Observation: Approx. 3-1/4 hours
SW
Distance from Observer to Discharge Point; Approx. 15 ft at Eye Level
Direction of Observer from Discharge Point:
Height of Observation Point: '
Description of Background:
Indoors
Set
Number
1
2
'3
/»
5
6
7
8
9
10
11
12
13
U
15
16
17
18
19
20
SUMMARY OF AVERAGE OPACITY
Tl
Start
0930
0936
0942
09^*8
0954
1000
1006
1012
1018
1024
1030
1230
1236
1242
1248
1254
1300
1306
1312
1318
me
End
0936
0942
0948
0954
1000
1006
1012
1018
1024
1030
1034
1236
1242
1248
1254
1300
1306
1312
1318
1324
Opacity
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Average
0
0
0
0
0
0
0
0
0
0
0
. 0
0
0
0
0
0
0
0
0
Set
Number
21
22
23
2k
25
26
27
28
29
30
31
32
33
34
T
Start
1324
1330
1435
1441
1447
1453
1459
1505
1511
1517
1523
1529
1535
1541
me
End
1330
1333
1441
1447
1453
1459
1505
1511
1517
1523
1529
1535
1541
1545
i
Opa
Sum
0
0
0
0
0
0
0
0
0
o-
0
0
0
0
pity
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Sketch Showing How Opacity Varied with Time:
Opaci ty
1 hr
2 hr
Time, Hours
3 hr
-124-
-------
TABLE
Mean fugitive emission values (% frequency emission)
for three tests at each location are presented. Values
are given for each oberserver.
Fine Ore Bins - Scrubber Inlet Duct Area TP-19
Observer 1 Test Mean
Test 1 0.0 0.0
Test 2 0.0 0.0
Test 3 0.0 0.0
Site Mean 0.0 0.0
Fine Ore Bins - Hopper Exhaust Duct Area TP-18
Test 1 0.0 0.0
Test 2 0.0 0.0
Test 3 0.0 0.0
Site Mean . 0.0 • . 0.0
Dryer Scrubber Inlet Area TP-2A
Test 1 0.0 0.0
Test 2 0.0 0.0
Test 3 0.0 0.0
Site Mean 0.0 0.0
-125-
-------
TABLE 55
Mean fugitive emission values (% frequency emission)
for three tests at each location are presented. Values
are given for each observer.
Grizzley Hood & Crusher Entrance Area TP-9 and 10.
Observer 1 Test Mean
Test 1 0.0 0.0
Test 2 0.0 0.0
Test 3 0.0 0.0
Site Mean 0.0 0.0
Crusher Transfer Point Area TP-13
Test 1 0.0 • 0.0
Test 2 0.0 0.0
Test 3 0.0 0.0
Site Mean 0.0 0.0
Crusher-Grizzley Area. TP-12 .
Test 1 0.0 0.0
Test 2 0.0 0.0
Test 3 0.0 0.0
Site Mean 0.0 0.0
-126-
-------
Appendix A
Raw Test Data
-------
TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
PLANT
DATE
SAMPLING
INSIDE OF FAR WALL TO
OUTSIDE OF PORT. (DISTANCE A) _
INSIDE OF NEAR WALL TO
OUTSIDE OF PORT. (DISTANCE B) _
STACK I.O.. (DISTANCE A - DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE.
CALCULATOR.
4
SCHEMATIC OF SAMPLING LOCATION
\
TRAVERSE
| POINT
NUMBER
s
j
I
1 J?
4
I
FRACTION
OF STACK 1.0.
-0^-?
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, ^-5
.
-------
PRELIMINARY VELOCITY TRAVERSE
PLANT &*X09* xW»»«^t/
DATE , in.H20
' ^^CP*^
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TEMPERATURE
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SCHEMATIC OF TRAVERSE POINT LAYOUT
TRAVERSE
POINT
NUMBER
~"~- -.
AVERAGE
VELOCITY
HEAD
iApsi. in.H20
STACK .
TEMPERATURE
(Ts<. "F
A-2
-------
NOMOGRAPH DATA
PLANT
DATE
9-
SAMPLING LOCATION
CONTROL BOX MO. _
/
7X
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
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A-3
-------
FIELD DATA
PLANT
DATE
PROBE LENGTH AND TYPE_c51
NOZZLE 1.0..
Fsr
SAMPLING LOCATION.X.V*,^
SAMPLE TYPE A^a^ey/
RUN NUMBER.
OPERATOR _
Ft f*T«
>ER n _ _
J_
ASSUMED MOISTURE.
SAMPLE BOX NUMBER
METER BOX NUMBER XcP<^<
METER AH,
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. y_
*=,-j~ -Tiv
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TRAVERSE
POINT
NUMBER
CLOCK TIME
4-0
34
GAS METER READING
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573.7
576.3
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ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H2Q)
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TEMPERATURE
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FIELD DATA
PLANT
DATE
-------
FIELD DATA
r
PROBE LENGTH AND TYPF 3 & QutO yLlCflTZ
NOZZLE ID ^y^
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER '3
OPERATOR Ba&
-------
i-UGI 1 iVt L,Vii>i>,u,\'
INSPECTION
:>mp;:ny
Location i
ompany Rep.i
. Inspector_
Affilitation.
Date'
;y Conditions
Precipitation
Wind Direction
Wind Speed;
Facility TypeL
Emission Source1.
Sketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points. ^^ _.^ ^ -._J lt/. __ ^—. ;—^.,-- g"M^6lOH $6(*fc&-
UBSERVATIONS
Time.
^egin.ObservationJ 5"',
AccOmuIated
Observation
Period
(Min: Sec)
5; os
AccOmuIated
Emission
Time-. .
(Min::Seo)
A..
(•, o "sc
S1'.
u <->
;oo
O'eC .
5'.oo
*' 0 O
End Observation
0 P/V\
5 r QQ
o;oO
O i O O
A-7
-------
I-UGI'I IVt t.Vibb.u.M
INSPECTION
Compcny
/
Location L
Company Rep.
Inspector,
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RECORD OF VISIBLE EMISSIONS
Company Name h / yfox-, U r-g ^ > U -x~ Date _
Plant Address D$vi .VL . W-. •r''v~.'.rv>-
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,
fi /0>7/ /v\
Weather Conditions
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Location
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TIME
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MIN
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01
02
03
04
05
06
07
08
09
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
SECONDS
00
0
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COMMENTS
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A-63
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TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
f l_HPI I - - -it—• nr - •- - -
DATE ...g^afe-7f
SAMPLING LOCATION
INSIDE OF FAR WALL TO
OUTSIDE OF PORT, (DISTANCE A) _
INSIDE OF NEAR WALL TO
OUTSIDE OF PORT, (DISTANCE B) _
STACK I.O.. (DISTANCE A - DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE.
CALCULATOR C) AJg / / /
"
&"
JjJyt).
2L
"s ' •
= .38:
-------
PRELIMINARY VELOCITY TRAVERSE
LOCATION
STACK I.D.
BAROMETRIC PRESSURE, in. Hg _
STACK GAUGE PRESSURE, in. H,0
OPERATORS
,::>
/*V
/ft <^
SCHEMATIC OF TRAVERSE POINT LAYOUT
TRAVERSE
POINT
NUMBER
X /
A
3
¥
5
<*
7
9
1
/o
ti
/^
/J
//
//
/t
/7
/
7
^
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//
/a
/3
/y
/$
/u
n
/>
n
3O
5/
^a
iiJ
3r
AVERAGE
VELOCITY
HEAD
Upjt. in.H20
.3H
,^o
i z^q
,10
iH4
• 5T
.b-r
STACK .
TEMPERATURE
(Ts«. °F
7o
70
7o
^
1*
10
lo
A-65
-------
NOMOGRAPH DATA
PLANT.
DATE
SAMPLING LOCATION
CONTROL BOX NO.
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE (AMBIENT + 20°R,°F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in Hg
STATIC PRESSURE IN STACK, in. Hg Z <^ -7 ^ . \ *)
(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
AHr?
Tmavg.
Bwo
' Pm
ps
P*Pm
savg.
A"avg.
•iPmax.
I.
o*:
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•
/.8V
£5*°
3%
2^.15
7.^.4*
AO
75
35
.rr
/
i5O
A50
^
A-66
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er *#*V •tf'V."'
\r * vv •» a > %
—T V^
'
FIELD DATA
SAMPLING LOCATJON C,.^
SAMPLE TYPE
RUN NUMBER.
OPERATOR _
PROBE LENGTH AND TYPE
NOZZLE I.D.JS
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P$).
FILTER NUMBER Is)
V- ;
ASSUMED MOISTURE,*
SAMPLE BOX NUMBER
METER BOX NUMBER
METER 'AHt L
C FACTOR ___i»-l
PITOT TUiE FACTOR V/T
REFERENCE Ap
NOTE
READ AND RECORD ALL DATA EVERY
2.O
MINUTES
TRAVERSE
POINT
NUMBER
X /
ft
/T
ao
a/
CLOCK TIME
U2_
1O
'11-
2,0
tO
GAS METER READING
. 0
0
. 7
VELOCITY
HEAD
(APS). in. H20
,-3
.V3)
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED (ACTUAL
,2
-3C-
4*
lo
_LJL
H
STACK
TEMPERATURE
(T$).°F
H
77
^
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74
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TEMPERATURE
INLET | OUTLET
/Q'^
HO
-U£
111
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loo
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100
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JA
PUMP
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in. H|
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ft
.1
i 10,, 48
65. H59
24, 77
0.
14, 4
28,. 97
4.27605
0. 25
0.9949
n 1-1 \- •-,
i. J. «~' • i. "i
14.4
49.79709131
0.67896
er
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28.82244109
24.63029412
34.65209677
8890= 445904
27.63966513
7104.143554
91.59114429
0.0393
0.
.0121789764
.7416077856
0.
0.
1 *••!'«
rll
,m
. '--= QC.J , T'fil
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r-RBfli^
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f:P'
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VSTD
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FHGR
FHLB
T GR'!
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TRAVERSE
POINT
NUMBER
CLOCK TIDE
GAS METER READING
(Vi. II3
VELOCITY
HEAD
lApsl. in HjO
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in H^Ol
DESIRED ACTUAL
STACK
TEMPERATURE
lTs»°F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in H|
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE
°F
0
/Ok
ion
fti. r
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•/O.
/on
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ITQ
UL
*
9JQ-Q
43-
J2.
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LH
2,-Z.o
J1Z
4
foo
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70
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in
,17
4^
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112.
i oo
t
2-2-5
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02.
l. 0
?<*
Il
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ife
.50
Ji
jza
\DT-
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>
ON
TRAVERSE
POINT
NUMBER
X- I
/„
-Z
10
II
/v
Hn
n
s2L
ao
33.
3o
CLOCK TIME
GAS METER READING
(Vmt. It3
FIELD DATA
- 79
DATE £r.
SAMPLING LOCATION.
SAMPLE TYPE <3Qr-f i'cuJO>e.-.
RUN NUMBER. "^
OPERATOR _
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE. (P)_J=L
FILTER NUMBER Is) _
|Q lg.tr
PROBE LENGTH AND TYPE.
NOZZLE 1.0
ASSUMED MOISTURE, %
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AH, /.£
C FACTOR __U_
PI TOT TUBE FACTOR
REFERENCE Ap
NOTE
READ AND RECORD ALL DATA EVERY.
MINUTES
£9.1
9<0 . 1
. 0
> 1
- />
VELOCITY
HEAD
(APst. in. H20
• 3o
,7 1
I
ORIFICE PRESSURE
DIFFERENTIAL
IAHI. in. H20)
DESIRED
-o
,92,
4-1
ACTUAL
STACK
TEMPERATURE
(TS).°F
"lo
13-
JZo.
10
70
70
^U.
DRY GAS METER
TEMPERATURE
INLET
#9
9JT
lol
HO
im.
OUTLET
£7
PUMP
VACUUM.
in. HI
^.
3
SAN
TEMF
0.57612
1.5204
.70.896
100.21
71. 028
24, 77
8.
28. 97
4.27605
96.
~ 1 ; H
0, 25
0B 9949
19."
55, HH^'-lh^o-
nn :-i9^-?i
1-590563211
j. 28«79551522
J 24._ 63764706
-! 9324=252175
29.2898bK6
-. 7514. 69604^
- 96.30759919
-! 0U0313
J " ' 0.
; -0087207897
I •.",5617188472
-------
TRAVERSE
pomi
NUMBER
CLOCK TIME
GAS METER READING
lVmi. It3
VELOCITY
HEAD
ORIFICE PRESSURE
DIFFERENTIAL
(AH), m H^Ol
DESIRED ACTUAL
STACK
TEMPERATURE
(T$I°F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in H|
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE
°F
-X^l
T^" T
j <;&. (j
.11
33.
.a.
7V
10
.HO
ja
^_
_^
^t
5T
^?3.5
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^
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I/**
l^L
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10
if
2£>
21
1-3
7/
1
n
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13
26
30
JL
Li
^
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lifL
LV*?
"71
.3-r
72
LJ_
M*.
,56
a
JO
7/
57
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JL-
73t-
SO
/w
3^
4//
/(010,
Ji.
Jtfk.
p^f
_AO_
o^-
Ai
l -
-^-
-------
TRAVERSE
POINT
NUMBER
r
L
10
II
13
.30
FIELD DATA
PLANT.
DATE_
-i-)-l""
PI TOT TUBE FACTOR
REFERENCE A p
NOTE
READ AND RECORD ALL DATA FVERY
MINUTES
CLOCK TIME
/O
11-
iff
lo
7.2-
X?
30
GAS METER READING
(Vl. It3
^13.0
VELOCITY
HEAD
(Aps), in. H20
,13
• IS
±
i M
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjOl
DESIRED
,57
v,o
Oo
Oo
40
ACTUAL
STACK
TEMPERATURE
(T$I,"F
"70
67
DRYGAS METER
TEMPERATURE
INLET
/07
1 10
(U
111
OUTLET
$7
PUMP
VACUUM,
in. HI
3
SAI
TEM1
L
I
'?
0. 52333
•1. 3U15
71.333
4. 276T5
-1.7
0. 25
0.9949
0. 853
9.
48.54474829
* a659190913
.9913408091
28.87500868,
24.64^
33.0075nn4i
S468,503327
26.7835747
6ci710 674275
92.30833679
/ 0.0132
• 0057856392
.3407733919
0.
0.
M
TH2I
1.1>
0.42403 - <'i>,g
>"l i ,-, .-. .-. , _ . • :''•'•' ••&
M]
MW<
p.;
VflCl
QflCfl
VSTIiI
QSTB1
' vif
FH(Ji
FHG
FHLB
T Gm
T Lg
JI£_
Ja.
13
^
J&.
J?37
120.
Ill
70
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-------
o?
P7S'
i
_22_
1002 .
73
1 0
it
I/
1Z
/%Q
73
/C
Zo
IP .O
-^^
ll. /
/ff
t/Z
MM
6 o
(A
170
rn
at
%
'M
L/fc
^L
<\^.
111
6- /
iEf
4
1
rr 3
-------
TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
PLANT c- XYOSJ ^l < rr*' •
DATE 9-26-77
SAN1PLINR 1 nrATION -TC^t/^fi?^ OaTltfT
INSIDE OF FAR
OUTSIDE 0
INSIDE OF NEAR
OUTSIDE 0
STACK I.O.. (CIS
NEAREST UPSTF
WALL TO
F PORT. (DISTANCE A)
WALL TO
F PORT. (DISTANCE B)
TANCE A • DISTANCE B
IEAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
r.Ai mi AT"R
^6-^
4x/t-
1 • -41"
«^l
CeJ&ilksyiA-
TRAVERSE
POINT
NUMBER
/
2-
t "^
-f-
£
fb
7
fr
FRACTION
OF STACK I.D.
.on
,032.
.0^
,079
,/of
752
./bl
1 ./
tf1/
/^
^??
J^f
.323
. 3fg
,60z
.677
,72?
,770
, 8"^6
x£3?
&t &
• o €^A
^^C
m
.HS
,9b%
.?,/?
STACK I.D.
4''
*
;
PRODUCT OF
COLUMNS 2 AND 3
(TO NEAREST 1. 8 INCH)
/%-
/ /^_
Z/^- ^*
3/4
4/2.
5"^
^> •%
%
J'fa.
//ft
/^^
/(^4^
«?4 ^>
«27-^
^ %
5/ /^-
^3/^
a^t 5A ;.
55/2^
^/ 3^f_
37^
?g> -5^i
, 3°l%
\ 4b'/z
SCHEMATIC OF SAMPLING LOCATION
DISTANCE B
4^2-
•
.--,
*
^ '
i - '
TRAVERSE POINT LOCATION
FROM OUTSIDE OF PORT
(SUM OF COLUMNS 4 & 5)
£
6
(c>JA
7^%
9\
9 ^j$
nn
I'z'fe.
/4
/5 ^fi(
/"? ~^/£i
2- &?/%
2VA-
•SILYz, ,-
5*1$$
<3G*%
3~)%%
^
-------
PRELIMINARY VELOCITY TRAVERSE
41
\%\
PLANT
DATE
LOCATION
STACK I.D.
BAROMETRIC PRESSURE, in. Hg.
STACK GAUG
OPERATORS.
M.frg- .\T-
STACK GAUGE PRESSURE, in. H.Q
/f efT ;=.
TRAVERSE
» POINT
NUMBER
VELOCITY
HEAD
Ups>, in.H2
y- /
5
n
/3
n
7*
AVERAGE
.2.70
,2,75
.-2^30
STACK
TEMPERATURE
(Ts>. "F
so
79
79
7%
n
7*
7?
77
77
77
77
77
60
57
SCHEMATIC OF TRAVERSE POINT LAYOUT
c
c
c
c
o
C
oc
cc
cC
cC
TRAVERSE
POINT
NUMBER
&1
r
/7
Z2-
AVERAGE
VELOCITY
HEAD
(Aps>. i
,100
,100
.110
.160
HO
Jbo
130
,476-
STACK .
TEMPERATURE
GO"
cc
cc
cc
cc.
cc
CC
AC?
Co
-------
NOMOGRAPH DATA
PLANT.
DATE._
SAMPLING LOCATION
CONTROL BOX NO. _
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
AHr?
Tmavg.
Bwo
pm
ps
P'Pm
savg.
APavg.
•^max.
/./
>3
,3
0,
-------
l\
FIELD DATA
PLANT.
DATE_
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
OPERATOR
PROBE LENGTH AND TYPE
NOZZLE 1.0
>E^
*£^~2 i
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE. (P,)_
FILTER NUMBER (s)
ASSUMED MOISTURE. %
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AH0
CFACTOR
PI TOT TUBE FACTOR
REFERENCE Ap
NOTE
READ AND RECORD ALL DATA EVERY
MINUTES
T./SO
.Zt
,110
/, or
,53
<*
~m~
'j
E
&•
o
/.OS
,53
77
76
7*
7%
to
H-
92,
/o?
2,5
J.o
5
0. 504OS'
,, C 1.0571
,.; :- 73.792
101,04
... • 61.077
• ' 24* 74
• - ' J
L_ B
• ' , 13. -
:.-. • 28,, 97
'. 9. 168432727--
. 96.''
>• 0..135--
•"•". • .' 0. 25
0.98615
.0. 855 •.
15. *
.47.02170312
•0. 70709
•1.481474711
.98518525?9
28.-807432??
•24. 75360294
31. 87639646-
17535= 39579
25.-69948186
14137.43824
.93.18396807
0.0073-
'0. ,
-•U023957738
... 290314817?
0. •
'0.
PBflR
,, as
.-. '.-'"Tf
: •' StflT:'
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L ••;•..' '•
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' ' • %$
FHWJ-
I Wt«"
FHGR;
FHLB>;
T (
T '.L&
t
t
-------
-------
>
->J
00
FIELD DATA
PLANT.
OATE_
SAMPLING LOCATION _
SAMPLE TYPE
RUN NUMBER ^ .
OPERATOR C&&&n0~
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE.
K
..
^V CLOCK TIME
sS?i"sN5Si
TIME, mm X^
r^f^—- —
GAS METER READING
32 ,S©0
3?,^o
?S,6tt>
3C,/*&
37,3Pe>
f?,$&&
9.t>£*
^/. z^o
^9?,6«*>
^5,Z^O
fa,9tr»
fl?<70T>
4£,/&*
Wtf&o
£J.1&0
£3,6&t>
£4,¥*z
f^uet)
5fcrSM>
VELOCITY
HEAD
(Aps). in. H20
.rtf
.l*£
,i¥f
itfO
j-70
.2^0
tzz§
<24Q
,1.^0
,3©d
2bQ
,f60
,ltt
,-*?o
,4&>
/4^°
ff l^d
,3^o
f5^o
r3do
4^O
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjO)
DESIRED
'72-
'77
!n
n*
.70
.fVf
M
m
!,-*>
(,7$
A/«>
,7?
,**>
l<6o
itft>
17*
(,
V,3^
^'/f
:2L
*• — HIMIIT
STACK
TEMPERATURE
(TS).°F
67
feg'
6-7
&>%
frv
67
/*%
fo
70
71
71
j?*-
72-
7Z
7V
7^>
1$L
7^
73
1^>
M
L-C^
ES ^.-Cp
DRY GAS METER
TEMPERATURE
INLET
(Tm ln».°F
5?4
c^^p
C^'7
O /
&"«'
d^
CL
?°
rl
V^r
f&
I
7
/ov
IO&
IWL
J04
(&\
/&*
/04
OUTLET
•T.^T
PUMP
VACUUM.
in. HI
/^
/,5^
I**
1,*
l,£
l,5~
3-.0
3.o
J.S
3,5
5rO
A5T
z.o
-------
, .
//??/
-------
FIELD DATA
''1- '
00
o
PLANT
DATE
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER -S
OPERATOR
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE.
C. FACTOR " /. /
PI TOT TUBE FACTOR £ft
BEFFBEMCEAp ,<3
NOTE
" : 0. 488
'*.! ' 1.0071
: ' 71.31 2"
;;. • • • 98. 104
N-..-- bU. 134-
: '.•"". 24.- 74
.0.
. 10,5
READ AND RECORD ALL DATA EVERY MINUTES ./.»
to®. 1.00
/oA soo
/02. l»&t>
/03. 9^0
/OS .OOO
foC».4do
/OK. «X90
/04. **o
ri/0.i&o>
/If. Ct»©O
iiz.y&o
114. 0o&
(/T. 150
lfo.3t>T>
VELOCITY
HEAD
(APS). in. H20
./ro
,/6O
./5"0
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TRAVERSE
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NUMBER
CLOCK TIME
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TIME
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PUMP
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in H|
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TEMPERATURE
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SUMMARY
RECORD OF VISIBLE EMISSIONS
Type of Plant
Company Name
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Discharge Location
OTHER
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Hours of Observation \ * o "V
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Plume Disporsion Behavior: Looping Coning
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Fanning
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Company Name
Plant Address
RECORD OF VISIBLE EMISSIONS
Date
Caspar
Stack Location
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fr.L.
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Company flame
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bserver's
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30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
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o
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0
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O
O
O
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RECORD OF VISIBLE EMISSIONS
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Observer
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ft
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TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
PLANT
DATE
SAMPLING LOCATION
gflUgc*f -fr-w
INSIDE OF FAR WALL TO
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STACK I.O.. (DISTANCE A - DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE.
CALCULATOR
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SCHEMATIC OF SAMPLING LOCATION
TRAVERSE
POINT
NUMBER
1
!
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OF STACK 1.0.
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£%.
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TRAVERSE POINT LOCATION
FROM OUTSIDE OF PORT
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fh
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PRELIMINARY VELOCITY TRAVERSE
PLANT TJityQC' U4 rC**TM
DATE 0&Y" Cjk&t 3£+li'$£r
STACK I.D. & ' '
BAROMETRIC PRESSURE in HB
STACK GAUGE PRESSURE, in. H,0
OPERATORS
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POINT
NUMBER
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STACK
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49
-49
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00
TRAVERSE
POINT
NUMBER
X-J
4
ft
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PLANT.
DATE_
6//fl4A/r
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SAMPLE TYPE
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Dusrn 5-Aj/«T
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BAROMETRIC PRESSURE _
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FILTER NUMBER Is) _
READ AND RECORD ALL DATA EVERY
4
ASSUMED MOISTURE. %
SAMPLE BOX NUMBER.
METER BOX NUMBER.
METER AH0 i
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PI TOT TUBE FACTOR
REFERENCE Ap
NOTE
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SR
MINUTES
CLOCK TIME
12
1C.
to
a 6
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ivmi. n3
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9. i / ,
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HEAD
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DIFFERENTIAL
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DESIRED
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10
ACTUAL
7*6.
1.3
1*3
STACK
TEMPERATURE
(T$I."F
7/
70
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TEMPERATURE
INLET
lot
o
OUTLET
PUMP
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in. H|
TTs
3.0
3.0
3.0
3-0
3*0
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TE
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95.38980179
37. 1099411
0= 636365
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28.78505676
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437.7875929
29. 71986211,'
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00
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POINT
NUMBER
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HPERATURE 7O°F
PRESSURE 314 ,*n
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S O 3. V79/
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1 . 9890880553
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\ 29.96773.42
353. H489448
98. 98600;-:!"i9
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HEAD
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TEMPERATURE
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in. H|
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INSPECTION
Company.
: '
Lt .axion i_
Company Rep.
Inspcctpr
Affilitation.
Slf- Conditions
Pr'^ Jpitation
__ V\
Wind Direction
Wind Speed'
Facility TypeL
Emission
- H-Qppe
I" ketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points.
OBSERVATIONS
gin.pbservationj (^\50 PM
id Observation :
TOTALS:
Time:
130--n.'
A-91
Accumulated'
Observation
Period
(Min: Sec)
Accumulated
Emission
Time.. .
(Min::Sec)
. o: oa
o : o o
Q :
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Cnmnrnv £r^O\On T • llAt^rwf
i .
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Company Rpp ^° \l • ' ^^"in \1 *C .
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Prpripitatinnl 1^
Facility Typei ^ ^
lir-pnrtpr , <^XL3[T /\ • 73 TTtJ 1 1 € y
Affiliintinn ^f>\^CJ ^r^-i^^T
n?t«»' 1 1**$? 1 ii
Wind Direction 1 / A
WinHSpPPH1' l^n
Emission Source1 n^Pp^-r Do>6\t f- X'>(erf~
Sketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points.
.OBSERVATIONS'
BeglnlQbseryationj
Time.
Accumulated
Observation
Period
(M5n::Sec)
S'dO
AccCimutated
Emission
Time., .
(Min:::Seo)
5'oo
o - o p-
.o :o.o
0:00
; oo
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run
End Observation :
A-92
0 '.OO
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rr.rr.nam/ Rpn KOV F1 W^6Tft1rV ) -t V\C"
V
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/
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Wind Direction K\ i
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Fmi«inn SniirrP1 HopP^r bu5~Ver iTnie.l-
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and/or actual emission points.
1-20 FT* Accumulated
Observation
Period
(Min: Sec)
Accumulated
Emission
Time . .
{Min:!:Sec}
o:
-------
Company Name
Plant Address
Stack Location
RECORD OK VISIBLE EMISSIONS
a~f Date
- 7?
Observer
Weather Conditions
Observer's
Location
.3.
TIME
COMMENTS
HR
> ^£3
^^2
MItl
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
.53
59
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O
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0
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£2L
o
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Plant Address
RECORD OF VISIBLE EMISSIONS
a-f Date
Stack Location
Weather Conditions
Observer
Observer's
Location
TIME
HR
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MIN
00
01
02
03
04
05
06
07
08
09
10
11
12
13
14
15
16
17
18
19
20
21
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23
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27
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Company Name
Plant Address
Stack Location
Weather Conditions
RrCORO OK VISIBLE EMISSIONS
/
Date
Observer
Observer's
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TIME
COMMENTS
MR
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Company Name _
Plant Address
RECORD OF VISIBLE EMISSIONS
Date
Observer
Stack Location
Weather Conditions
Observer's
Location
TIME
HR
feO
0
MIN
00
01
02
03
04
05
06
07
08
09
10
11
12
13
14
15
16
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19
20
21
22
23
24
25
26
27
28
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SECONDS
00
O
o
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15
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0
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-------
Company Name _
Plant Address
Stack Location
RECORD OF VISIBLE EMISSIONS
Date
Observer
Weather Conditions
Observer's
Location
TIME
HR
/
MIN
00
01
02
03
04
05
06
07
08
09
10
11
12
13
14
15
16
17
18
19
20
21
22
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24
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26
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SECC.NDS
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-------
Company Name
Plant Address
Stack Location
RECORD OK VISIDLE EMISSIONS
Date
Observer
Weather Conditions
TIME
COMMENTS
MR
MIH
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
53
59
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RECORD OF VISIBLE EMISSIONS
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Observer C. .
Stack Location
Weather Conditions
Observer's
Location
TIME
HR
3
MIN
00
01
02
03
04
05
06
07
08
09
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
SECONDS
00
O
o
<£>
O
O
15
O
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O
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O
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COMMENTS
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A-100
-------
Company Name
Plant Address
RFCORD OK VISIBLE EMISSIONS
Date
o -
-
Observer
^"---^
t>
/
*•*. *"*~
Stack Location (^>,-tz
Weather Conditions
Observer's
Location
TIME
MR
^>3
MIN
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
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53
59
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15
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O
O
o
o
o
o
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Company Name _
Plant Address _
Stack Location
RECORD OF VISIBLE EMISSIONS
&-/ Date
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Observer
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Observer's
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TIME
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01
02
03
04
05
06
07
08
09
10
11
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13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
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A-102
-------
TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
PLANT £ffl -
DATE .....5
SAMPLING LOCATION
INSIDE OF FAR WALL TO
OUTSIDE OF PORT, (DISTANCE A) _
INSIDE OF NEAR WALL TO
OUTSIDE OF PORT. (DISTANCE B) _
STACK I.D.. (DISTANCE A - DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM,DISTURBANCE.
CALCULATOR.
tt£ b»U ScRtift(jgp XiOl.gr
10"
&
->
\
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FRACTION
OF STACK I.D.
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.
STACK 1.0.
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,
i
PRODUCT OF
COLUMNS 2 AND 3
(TO NEAREST 1. 8 INCH)
- &
r^
S"'4
93^
^
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I4"z
(SV8
L
-------
PRELIMINARY VELOCITY TRAVERSE
PLANT [cXK -*• 30 "
STACK GAUGE PRESSURE in H,0 fc "
OPERATORS 1
. i /, '
i
TRAVERSE
POINT
NUMBER
X - I
A
3
Y
5
6
9
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AVERAGE
VELOCITY
HEAD
Qps), in.H20
!
1,3
STACK
TEMPERATURE
(Tsl. "F
1Z
SCHEMATIC OF TRAVERSE POINT LAYOUT
TRAVERSE
POINT
NUMBER
y- i
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7
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. °F
-------
NOMOGRAPH DATA
PLANT r
DATE
W
SAMPLING LOCATION A&>
CONTROL BOX NO. NuJ/" >
•t> It,
-
*
,t> 11*
-J*~J
Z ? ! 5- '"/
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 $0 "
STATIC PRESSURE IN STACK, in. Hg 6 **" ' °7 ^
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE. °F
AVERAGE VELOCITY HEAD. in. H20
MAXIMUM VELOCITY HEAD. in. H20
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap. in. H20
•%„
Tmavg.
Bwo
s
pm .
PS
H
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avg.
\
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APmax..
t.os
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P
A-105
-------
FIELD DATA
-»*.
PLANT fc Vft - K f / t> IV U ftf rl , tUvU fW , +Jt*
•*
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>
1^
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TRAVERSE
POINT
NUMBER
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PROBE LENGTH AND TYPE >> Q* i
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ASSUMED Ml
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METER BOX
METER AH
C FACTOR.
PI TOT TU
HEFERENC
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NUMBER Mid* 1
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READ AND RECORD ALL DATA EVERY _*5 MINUTES
GAS METER READING
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6#s^yo
£?£. i
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I
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ACTUAL
v
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11
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71
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FIELD DATA
PLANT
OATE
on - f -f
SAMPL
SAMPLE TYPE
RUN NUMBER.
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, «%? are
/ft.
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PROBE LENGTH AND TYPE.
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AMBIENT TEMPERATURE .
BAROMETRIC PRESSURE .
STATIC PRESSURE. (Ps) .-, ?i,.,
FILTER NUMBER ($)
ASSUMED MOISTURE. *.
SAMPLE BOX NUMBER ~
METER BOX NUMBER.
METER AH~ L
CFACTOR
PI TOT TUIE FACTOR _*4
REFERENCE A p _____
NOTE *£-•£ ~ . f> I A.
READ AND RECORD ALL DATA EVERY.
MINUTES
,0/ (g) 7
TRAVERSE
POINT
NUMBER
GAS METER READING
IV.I.R1
t 126?
VELOCITY
HEAD
(Aps). in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjO)
DESIRED ACTUAL
STACK
TEMPERATURE
(T$).°F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in. HI
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
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FIELD DATA
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DATE ^ ~f?P "??
SAMPLING LOCATION-";..^ Or£--^C
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BAROMETRIC PRESSURE ^M .
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SAMPLE BOX NUMBER -~
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METER AH^ '
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REFERENCE Ap / ' 3
NOTE /£,^__* 1OI8"
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POINT
NUMBER
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READ AND RECORD ALL DATA EVERY
MINUTES
VELOCITY
HEAD
PjI. in. H20
-------
FUGITIVE EMISSION
INSPECTION
Location TP r/tJ?
Company Rep.
Inspector /-V/3
Affil Station
Date 7
Sky Conditions
Precipitation
Wind Direction A///-J-
Wind Speed
/I/'
Facility Type
Emission Source
Sketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points.
OBSERVATIONS
Time
Accumulated
Observation
"Period
(Min: Sec)
Begin Observation
Accumulated
Emission
Time
(Min: Sec)
o : c<
End Observation
A-109
-------
l-L'GI 1 !Vt t.Y-iijb.u.
INSPECTION
f>rr>p.->ny £? X ,
\ ofpiipn i _ ,, 1 ' 1" !/' f~ • *- -
Compnny Rpp- "f^^AA yARfo'/
-------
l-UGIl iVt L,ViSi>,ui\!
INSPECTION
00^ A/ /M ////=•/ 4/
•loraf.nn1 7" /* /^///^ ^/P^/?///
r\mp-T">y Rep- T^^ .-//4 A? X//^' <*^
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Prrripitation /1///V
' •*• * / ^ 40 f\ / ^ / / ' /L*^ /\ ^ / / /
P *»/**! 1 1\/ T^ V/rtPi ^ /v r • * ^ l ' t / ^- £-—
In.prrtpr ^ ^ C /^ A»/t A tfA
Affjlii.-iiinn fi&if F. \,4S & * r0W /A/C
Wind Direction' A/ /A
Emission Source ' ^ /^ >- {/*& C A- ,y/X/
Sketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points.
•AT.
OBSERVATIONS
ln Observation',
TFrne:
Accdmulatetl'
Observation
Period
(Mip: Sec)
Accumulated
Emission
Time. .
(Min::Sec)
a ;
End Observation :
A-111
-------
SUKMARY
RECORD OF VISIBLE EMISSIONS
Type of Plant
Company Name
Plant Address
fl i A
Date *7 -
v/OAt/'K
Hours of Observation
Observer
Type of Discharge STACK
Discharge Location
OTHER
OQV» iaj/i»a
Height of Point of Discharge
Observer's Location:
Distance to Discharge Point
Height of Observation Point
o
Direction from Discharge Point
Background Description
Weather: Clear
Overcast
Wind Direction
Plume Description:
Detached: Yes Ho
Color: Black V.'hite
Partly Cloudy Other
. Sky Color
Wind Velocity
mi/hr
Other
Plume Dispersion Behavior: Looping
Lofting
Estimated Distance Pluns Visible
Coning Fanning
Fumigating Othe/
i$ 56 -2005 '
- a 1 3$ -
A-112
-------
RFCORD OF VISIBLE EMISSIONS
Company Name yxT.v-1 P'l !/>£»%/ Date
Plant Address CflAfig r Uj v/ Q , Observer 3" D Q TLA0 ///
/
•~7'7
Stack Location I rixA/4<
~
Weather Conditions f*J/M.
Observer's
Location
rrt i
p
i\/>l£-
-
MR
/£fi
TIME
HIM
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
53
59
00
0
0
o
O
O
O
0
o
o
0
SECONDS
15
O
o
o
c
0
0
D
c
0
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30
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6
O
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COMMENTS
r / i, i f— • - / ••
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.
i
A-113
-------
Company Name
Plant Address f /^ C
A
LVr
Stack Location
Weather Conditions r-
RECORD OF VISIBLE EMISSIONS
n;..^ffc.f Date ^-ago^
<^ kv'v/n.- Observer T\ . D ^ O
/ >
< J •
Dg> i,-rt
f,. Observer's
Location
(0
TIME
HR
--vp»
g€
MIN
00
01
02
03
04
05
06
07
08
09
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
SECONDS
00
D
0
0
0
0
o
o
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0
0
o
0
o
o
o
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COMMENTS
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RFCORD OK VISIBLE EMISSIONS
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A< i * ;
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9-
Plant Address < ,f\ ,N.
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Weather Conditions
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34
35
36
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38
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42
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A-115
-------
Company Name _
Plant Address C^LC*?.
Weather Conditions
Observer's
Location
v/
p
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TIME
HR
31 r
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MIN
00
01
02
03
04
05
06
07
08
09
10
11
12
13
14
15
16
17
18
19
20
21
22
23
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25
26
27
28
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SECONDS
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COMMENTS
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A-116
-------
Company Name _
Plant Address
RECORD OF VISIBLE EMISSIONS
I Date ^-
Stack Location
Weather Conditions
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Observer's ,
Location ./A x nt UJC*.
TIME
HR
5-
MIN
0')
01
02
03
04
05
06
07
08
09
10
11
12
13
14
15
16
17
13
19
20
21
22
23
24
25
26
27
28
29
SECONDS
00
0
O
O
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15
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30
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COMMENTS
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A-117
-------
Company Name _
Plant Address
Stack Location
RECORD OK VISIBLE EMISSIONS
ri ; ^.P V^-i / Date
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A-118
-------
Company Name _
Plant Address
RECORD OF VISIBLE EMISSIONS
1 Date
"/ /
Stack Location
VA , Observer ^3" . D / 0 '/Qg i 11
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Weather Conditions
£»• 94. Observer's ,
Location /O
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PI TOT TU
REFERENC
NOTE
BE FACTOR
E AO '-
5*A
• V
U
RE AD AND RECORD ALL DATA EVERY / MINUTES
GAS METER READING
^y. y?^
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(AH), in. HjO)
DESIRED
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1
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SAMPLE TVP
RUN NUMBEF
OPERATOR .
AMBIENT TEI
BAROMETRIC
STATIC PRE!
FILTER HUM
NSV CLOCK TIME
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METER BOX
METER AH,
,.ii
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1KTIIBF t 3c7c,
( NUMBER /
NUMBER 1 13J£
/3£^
C FACTOR
PITOT TU
REFERENC
NOTE
BE FACTOR
F Ap i -
t
READ AND RECORD ALL DATA EVERY 't MINUTES
GAS METER READING
(Vj.lt3
OlV.tf/
0*1. V
c?*S.^
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DIFFERENTIAL
(AH), iii. H20)
DESIRED
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Z^s
2--S
£.s
3.S
3~r
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in. HI
2.6
2.0
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110. 638
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1164. 672859
66. 9930454
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0.
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l. 0235787 i' 18
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tut. TS =
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• '/. I/
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T Wt'
• FHGR/
FHLB
T GR
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, J
-------
FUGITIVE EMISSION
INSPECTION
Company
Location
F I LHV6-
Company Rep.
Inspector
6 C A ffi *# A
Affilitation
M/c
Date
///4
Facility Type
Emission Source
Sketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points.
AT
OBSERVATIONS
Begin Observation
v \ ' s- A -4 *
\Y\ »--Vlfa»-» ' 1 » % *->
Time
Accumulated
Observation
Period
(Min: Sec)
\oo
End Observation
Accumulated
Emission
Time
(Min: Sec)
0:0
A-139
-------
FUGITIVE EMISSION
INSPECTION
Company
Location
Company Rep.
ToM
Inspector
c. A- ft A* A
Affilitation
Date
Sky Conditions A//A
Precipitation
«•*//.>*
Wind Direction A//A
Wind Speed
Facility Type
W. fA ILL
Emission Source &**? ^•^•s:
Sketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points.
OBSERVATIONS
Begin Observation
Time
Accumulated
Observation
Period
(Min: Sec)
o
IT '.
Accumulated
Emission
Time
(Min: Sec)
9 .' a
o ; O
End Observation
A-1UO
-------
FUGITIVE EMISSION
INSPECTION
Company £XVD// //I /*/£/*.£ L.
1 oration W7 <#-/-/ £-/4- A/ £ Mll/<£
r.ompany Rep. ToM yA-tf.fi/tCK
Sky Conditions fl//A
Precipitation W/A
Facility Type iSR&fJH/to. tA ! ">-L
Inspector P <•
Affilitation f\ <-
' 6 O/f Pfi $ }\ A
> X /'• Vi^^57^^/ ~
,
Wind Direction
Wind Speed
Emission Source
A/A-
/V//A
ft A. y? J? iV / *£V / ) & K^
§3 S4? f\ f\. ^" ** / f ^^ •»• & ^*^-
Sketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points.
.pot t/T
OBSERVATIONS
Begin Observation
Time
Accumulated
Observation
Period
(Min: Sec)
End Observation
Accumulated
Emission
Time
(Min: Sec)
-------
Company Name /g:
Plant Address
Stack Location
Weather Conditions
RrCORD OK VISIBLE EMISSIONS
^,/ Date
Observer _
Observer's
TIME
COMMENTS
MR
<^9
MIN
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
50
59
00
&
^
r>
&
o
O
&
c>
o
^
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r~^
0
0
^
^
O
cc
^
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O
o
O
0
o
o
0
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SECONDS
15
0
0
f~->
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0
0
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r-^
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(Z3o^ ,333- 63
: /43>~- /54S-- Z£—
"/ ^ *?
.
\
1
-------
Company Name
Plant Address
RECORD OF VISIBLE EMISSIONS
•-/ Date
Observer
so-
Stack Location
•s&^ey-*
Weather Conditions
Observer's
Location
TIME
HR
SO
MIN
00
01
02
03
04
OS
06
07
08
09
10
11
12
13
14
ts
16
17
18
19
20
21
22
23
24
25
26
27
28
29
SECONDS
00
0
<£>
O
CD
O
r>
Q
0
&
0
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<=>
CD
G
O
f°->
O
O
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15
CD
O
O
0
0
O
O
O
O
O
<0
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O
O
O
o
CD
CD
O
CD
-------
Company Name
Plant Address
Stack Location
Weather Conditions
RECORD OK VISIBLE EMISSIONS
Date
Observer
Observer's
Location
TIME
MR
^
/&
MIN
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
53
59
00
O
c-j
<-^>
<_,
O
SECONDS
15
0
0
O
0
CD
30
0
O
0
^
CD
45
O
O
0
O
O
COMMENTS
•
^>2/ ^"sX*/
•
i
-------
Company Name _
Plant Address _
Stack Location
RECORD OF VISIBLE EMISSIONS
o>
C3
r~>
cp
c?
O
o
<~}
O
O
O
o
O
0
0
<^P
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cr>
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0
o
o
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SECONDS
15
rO
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cD
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O
O
0
o
r>
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c?
CD
o
r^i
O
0
CD
0
O
o
0
o
o
45
CD
CD
O
O
O
0
0
-------
Company Name
RECORD OF VISIBLE EMISSIONS
^-^,/ Date
Plant Address
Stack location
Weather Conditions
Observer
- >x
•?*f:s&~*£&*&
Observer's
Location
TIME
HR
'3
MIN
00
01
02
03
04
05
06
07
08
09
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
?9
SECONDS
00
G
0
o
C,
o
o
o
Q
o
0
^
o
0
<^
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&
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o.
30
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0
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c=>
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CINNENTS
.
;
i
r
1
|
j
6
.
•
A-146
-------
Company Name _
Plant Address _
Stack Location
RECORD OK VIS10LE EMISSIONS
Date
Weather Conditions
.^server's
Location
__ y
^=» >-y
<-3
45
<3>
O
CD
a
COMMENTS
^/^ ^^^
.
,
-------
Company Name _
Plant Address _
Stack Location
RECORD OK VISIBLE EMISSIONS
Date
Observer
Weather Conditions
Observer's
Location
TIME
MR
/+•
MIN
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
53
59
00
0
0
0
CD
CD
c^
0
O
CD
O
Q
v=>
o
CD
0
<=>
0
o
SECONDS
15
0
^
G
O
0
CD
CD
O
C5
0
CD
a
0
0
<=?
c — :
0
O
O
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">
^
O
O
o
30
CD
0
O
O
CD
O
o
CD
0
CD
CD
0
CD
O
0
0
O
O
f~^
0
o
0
c^
o
o
45
O
O
O
O
0
O
0
CD
O
o
o^
CD
CD
c^
-------
RECORD OK VISIBLE EMISSIONS
Company Name
Plant Addres
Stack Locati
Weather Com
<~^<*?eyz>r ~Z>ysZ-^e=>s-^.f Date <&^ ~S~ '~-7fr __
s ^*s**0 >***,-*• /r Observer CX^^s^s^-xs <^'
/ ^
itlons
7 Location ^<- •><£••"•*• -»«"••—•='«— - *y~ /**•*£.'
TIME
MR
*f
HIM
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
00
„
o
^
0
0
o
0
0
O
CD
O
O
&
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(^
SECOIIDS
15
<£>
c->
0
0
e>
c)
^
a
^
&
£\
£^)
r>
30
O
0
0
O
0
G
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^
0
0
0
o
C>
CD
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C)
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7^
o
o
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:d>
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^
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c>
COMMENTS
^T&S ~^~^~=Z*^3
-
,
A-
-------
RECORD OF VISIBLE EMISSIONS
Company Name <^xfx5o=>y ~I??'sZ-?*t?'-5t-/ Date ^e2 — /- 'r' r
Plant Address -> <*£Jcs&-?**'>* f Observer &• xili><^-'os^.<_
£/
Stack Location ssSs^afrrrt? ^f'^^js-^-~
Weather Conditions
Zs
TIME
HR
-C*
MIN
00
01
02
03
04
05
06
07
08
09
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
SECONDS
00
0
0
0
0
^
0
^
,__.,
<=>
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O.
O
^>
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&
€>
0
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dp
0
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15
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<->
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30
c^,
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0
c.
0
c^
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dp
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0
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COMMENTS
.
i
,
r
i
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i
i
.
•
A-150
-------
TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
'-30-
a
CU
PLANT
DATE
SAMPLING LOCATION _
INSIDE OF FAR WALL TO
OUTSIDE OF PORT. (DISTANCE A) _
INSIDE OF NEAR WALL TO
OUTSIDE OF PORT, (DISTANCE B) _
STACK I.D.. (DISTANCE A • DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM.DISTURBANCE.
CALCULATOR _
V2,
SCHEMATIC OF SAMPLING LOCATION
TRAVERSE
! POINT
NUMBER
X4 /
) 2
^^
t;
>:
. ,-«i^^
?
?
FRACTION
OF STACK 1.0.
. :.-«*»*
^s-z
./OS
./^4
.:V-V,37LS
Pf ' • ^"^7
^' .^^
,S9r
»^^S
i I
STACK
1?
.
.D.
'«'
r
PRODUCT OF
COLUMNS 2 AND 3
(TO NEAREST 1. 8 INCH)
/*
JVs
2*Vtf
4%
9/^-
/fl V«
/T.
/3 -
DISTANCE B
4
i
M '
TRAVERSE POINT LOCA1 ION
FROM OUTSIDE OF PORT
(SUM OF COLUMNS 4 & 5)
«'/*-
^^/8
(**/*
xYz
/$'/+
/VVx
Ib
n
i
A-151
-------
PRELIMINARY VELOCITY TRAVERSE
PLANT
DATE
LOCATION
STACK I.D._
BAROMETRIC PRESSURE, in. Hg_
STACK GAUGE PRESSURE, in. H20.
OPERATORS L
(5,5"
SCHEMATIC OF TRAVERSE POINT LAYOUT
TRAVERSE
POINT
NUMBER
x-i
2.
3
; 4
>r
tr-
" b
7
fe
AVERAGE
VELOCITY
HEAD
Ups), in.H20
^ .37
<^^S^.3S"
&.&>
^ ,95-
<& 1.20
<2& AZ5
•d*L !,-&
^ fts
,S/
STACK
TEMPERATURE
(Tsl. "F
/230
/3/
/3D
'!*/
/•?/
/3/
|3o
TRAVERSE
POINT
NUMBER
tf-l
1
<3
4:
^
7;
7
,o
AVERAGE
VELOCITY
HEAD
STACK .
TEMPERATURE
(Ts>. °F
A-152
-------
NOMOGRAPH DATA
PLANT.
DATE._
SAMPLING LOCATION
CONTROL BOX NO.
(D U
S" 3
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE (AMBIENT + 20°F).°F
PERCENT MOISTURE IN GAS STREAM BY VOLUME. >.;,:•
BAROMETRIC PRESSURE AT METER, in Hg *
STATIC PRESSURE IN STACK, in. Hg
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE. °F
AVERAGE VELOCITY HEAD. in. H20
MAXIMUM VELOCITY HEAD, in. H20
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE Ap. in. H20
T(navg.
Bwo
Pm
>s
Pspm
savg.
Apavg.
•^Pmax.
t
•
*
,
Ml.
jDO
13,0
tt.o
^.0
AOD
/3-c
,tl
1,25
'17
IZS
fc5
A-153
-------
FIELD DATA
VJ1
-c-
-------
DRY MOLECULAR WEIGHT DETERMINATION
PLANT
DATE
COMMENTS:
SAMPLING TIME (24 hr CLOCK)
SAMPLING LOCATION 5<1 K J/5 foL
<^ 72 ,1
SAMPLE TYPE (BAG, INTEGRATED. CONTINUOUS)
ANALYTICAL METHOD
AMBIENT TEMPERATURE _
OPERATOR I/ ./)Y
1/2
^\^ RUN
GAS ^^\^
C02
02,^
NET
l,(*
^,8-
6.C?
^O.G
2
ACTUAL
READING
/ i
1^ V
n.^
sat
NET
^,
17^
0,o
30-53
MULTIPLIER
44/100
32/100
a/100
a/ioo
MOLECULAR WEIGHT OF
STACK GAS (DRY BASIS)
Md, Ib/lb mole
0.(o$C\
5, 72. %
O.ooo
J?c5.5'5
TOTAL a?/77
vn
vn
-------
>
vn
FIELD DATA
PLAHT
DATE
SAMPLING LOCATION *• ejtUJtr
SAMPLE TYPE
RUN NUMBER
OPERATOR
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P )
FILTER NUMBER Is)
» 0
READ AND RECORD ALL DATA EVERY
A-
PROBE LEN
NOZZLE I.D
ASSUMED MC
SAMPLE BOI
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OUTLET
-------
DRY MOLECULAR WEIGHT DETERMINATION
PLANT
OATE
COMMENTS:
SAMPLING TIME (24 hr CLOCK!
SAMPLING LOCATION
SAMPLE TYPE (BAG, INTEGRATED. CONTINUOUS) 6 (S fj"
ANALYTICAL METHOD
AMBIENT TEMPERATURE
OPERATOR I/ • Yh,
1 1 2
\^ RUN
GAS ^\
C02
02
VJ1
-------
vn
oo
TRAVERSE
POINT
NUMBER
XH
^
i
i-
CLOCK TIME
GAS METER READING
FIELD DATA
PLANT.
DATE_
SAMPLING
SAMPLE TYPE
RUN NUMBER.
OPERATOR _
PROBE LENGTH AND TYPE
NOZZLE 1.0
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE. (P$) _
FILTER NUMBER Is)
-V
ASSUMED MOISTURE. % *^
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AHj,
CFACTOR
T
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M
PITOT TUBE FACTOR
REFERENCE Ap
NOTE
READ AND RECORD ALL DATA EVERY.
MINUTES
113.252
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HEAD
(Aps). in. H^O
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1.01.
T/ *\ fyf
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to
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(AH), in. HjO)
DESIRED
^
MO_
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ACTUAL
2,0*
2,0$
sv
STACK
TEMPERATURE
-------
DRY MOLECULAR WEIGHT DETERMINATION
3
>
VJ1
PLANT H CXXO*/ Uf/r«^, COMMENTS:
DATE /O-/-79 •'•*
SAMPLING TIME"(24;h( ^OC
SAMPLING LOCATION
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GAS ^\^
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02 (NET IS ACTUAL 02
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1.5
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MULTIPLIER
44/100
32/100
a/ioo
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MOLECULAR WEIGHT OF
STACK GAS (DRY BASIS)!
Md, Ib Ib mole
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r.7if
0.0 O
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TOTAL ^Fl^
;**»
-------
Company flame '^
Plant Address
RECORD OF VISIBLE EMISSIONS
'UN- Date
UU
Stack Location LV,,fcr
Weather Conditions
Observer T. f\(SX(Sir\
Observer's
Location
JVi
TIME
HR
O
JO
MIN
00
01
02
03
04
05
06
07
08
09
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
SECONDS
00
0
5"
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£
£
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A-160
-------
Company Name
Plant Address ") <
RECORD OK VISIBLE EMISSIONS
V(T.rv\jW\ _ Date '&j Uj
Stack Location jJr
Weather Conditions ( j;V
V.JT-VI
Observer
Observer's * -
Location /j>i
TIME
COMMENTS
)OOG
30
31
32
33
34
35
36
37
38
39
40 .
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
5!3
59
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0
0
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A-161
-------
Company flame
RECORD OF VISIBLE EMISSIONS
Date I
Plant Address*Vdx M.W
Observer ' •
Stack Location LV'Vi*'- V Ti)W>C Uu !g1 Observer's __/„ \\
Weather Conditions (_
J Location 1 ^O ioyT1^
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KU^JL - c?u eJ
TIME .
HR
|
3
-------
Company Name
RECORD OK VISIBLE EMISSIONS
rfr/v^f^ Date
Plant Address^S K JOV D(>^ fcC \Jyfo Observer T- MfltfGft
Stack Location t^ryt^ Scri'^fr t-M' ft Observer's , /"A ' ,. » il
Weather Conditions i Cv
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r\ V V ' (5 I>(i V P> ^
TIME COMMENTS
"Hit!
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
53
59
00
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A-163
-------
RECORD OF VISIBLE EMISSIONS
Company Name
Plant Addres
Stack Locat'
Weather Cone
P:-XXC'rN- V/p(\/Tn t,1 N^ Date H-'/ fW /M
. 1 \ 1 i*^. 1 t / / ».
sQ^N- A)W VjD'^vlc,^ WC.^og Observer T- nO>/C5YN
on Pf'-yf''- Xr-r^tt^^l/Jllr1 \ Observer's , S^.r C^.Il
itions I
Location ' D*-^ -/l^t/\'N-
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\
MIN
00
01
02
03
04
05
06
07
08
09
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
?9
SECONDS
00
^
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-------
Company Name
Plant Address _
Stack Location
7—
Weather Conditions C
RKORD OK VISIBLE EMISSIONS
^ Date _ jQ
. ,
/7/Ai
\ l\)
Observer T .
Observer's
Location
TIME
COMMENTS
MR
•l\
MIH
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
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A-165
-------
Company Name
Plant Address
Stack Location J
Weather Conditions
RFCORD OK VISIBLE EMISSIONS
Date
TIME
COMMENTS
/^IC
14
H
30
31
32
33
34
35
36
37
38
39
40.
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
53
59
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A-166
-------
RECORD OF VISIBLE EMISSIONS
Company flame
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A-167
-------
RECORD OF VISIBLE EMISSIONS
Company Name
Plant Address
Stack Location
Weather Conditions
ftM A
TIME
COMMENTS
(|R
'^
MIH
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
53
59
00
ft
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0
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3
SECONDS
15
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0
3
30
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45
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3
^
A-168
-------
TRAVERSE POINT LOCATION FOR CIRCULAR DUCT?'
/
f-30-7?
D .
PLANT
DATE
SAMPLING LOCATION
INSIDE OF FAR WALL TO \ 0
OUTSIDE OF PORT. (DISTANCE A) _
INSIDE OF NEAR WALL TO \
OUTSIDE OF PORT. (DISTANCE B) _
STACK I.O.. (DISTANCE A - DISTANCE B).
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
CALCULATOR
17
457
as.fiu
SCHEMATIC OF SAMPLING LOCATION
TRAVERSE
POINT
NUMBER
FRACTION
OF STACK I.D.
STACK I.D.
PRODUCT OF
COLUMNS 2 AND 3
(TO NEAREST 1, 8 INCH)
DISTANCE B
TRAVERSE POINT LOCATION
FROM OUTSIDE OF PORT
(SUM OF COLUMNS 4 & 5)
.of*
3 •»/»
77/5
,375
.7/7
.875
/fo
/4
-^SX
13
n
JiS.
A-169
-------
PRELIMINARY VELOCITY TRAVERSE
PLANT kixxon ~ z~rhr
DATE 4-30-7?
LOCATION /ic*?r \ ft !£.t~
STACK ID ^ \1 V^ "
BAROMETRIC PRESSURE, in. Hg *• ^ • o
STACK GAUGE PRESSURE in. H.,0 — » 2*4
OPERATORS fn
. - L I
d' J
TRAVERSE
POINT
NUMBER
^- !
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3
j
5-
ta
7
<%
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AVERAGE
VELOCITY
HEAD
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t
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TEMPERATURE
lTs). °F
£l£
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lort
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SCHEMATIC OF TRAVERSE POINT LAYOUT
TRAVERSE
POINT
NUMBER
V
AVERAGE
VELOCITY
HEAD
Qpji. in.H20
STACK
TEMPERATURE
(Ts-. °F
A-170
-------
V)
NOMOGRAPH DATA
PLANT i£*Xgn - EPR
DATE.
SAMPLING LOCATION
CONTROL BOX N(
A
OT
' •-;
UY\
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE ( AMBIENT ^0°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
^Hf9
:.- Trnavg.
Bwo
pm
PS
savg.
^Pavg.
APmax.
•^
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-0
W
d^
) ^
-------
FIELD DATA
PLANT
DATE
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
OPERATOR _
PROBE LENGTH AND TYPf
NOZZLE 1.0.
i!T
AJ6
ASSUMED MOISTURE, *.
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AH,
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (Ps)
FILTER NUMBER Is)
'*•-
/.
CFACTOR.
PITOT TUBE FACTOR
REFERENCE A p __,_£
MOTE ££~T -• • -O
4-
READ AND RECORD ALL DATA EVERY
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(Vml. tt3
VELOCITY
HEAD
-------
DRY MOLECULAR WEIGHT DETERMINATION
PLANT CT [\U/N U? M A^
DATE /L> - / ' 7 ^
SAMPLING TIME (24 hi CLOCK)
SAMPLING LOCATION ^Cf? Ul W . <£ / AJ
SAMPLE TYPE (BAG, INTEGRATED, CONTINUOUS)
ANALYTICAL METHOD ^M ")// 7"'
v±r
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AMBIENT TEMPERATURE 1 1?*'
OPERATOR \/ /h
COMMENTS:
\
^\^ RUN
^\ 1
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
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FIELD DATA
6
PLANT ^
am lO-t-'-N
s »'-V •*• t
SAMPLE TYPE £.
RUN NUMBER _L
OPERATOR
AMBIENT TEHPERATUftE / OCe
BAROMETRIC PRESSURE .. "'- '•• -''- r. " " •'• ' 7 J >* ='
STATIC PRESSURE. IP,
FILTER NUMBER ui-
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PRORF 1 FRSTH AND TYPE t> IV
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ASSUMED He
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(NIWBFR ' 1- ' t .:'
METER BOX NUMBER Klixi I i n O.!;:: :• ft r- r-, '
METER AH,, , - , i i - - - • • ii
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rurTnii* .11 '. ' u- '-":- !l -*H|
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REFERENCI
NATE / <
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: AP
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TEMPERATURE
IHLET
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2150. VUC-
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DRY MOLECULAR WEIGHT DETERMINATION
PLANT
DATE
COMMENTS:
SAMPLING TIME (24 hi CLOCK)
SAMPLING LOCATION 5l ft
SAMPLE TYPE (BAG, INTEGRATED^ CONTINUOUS) 6 fl O
AVERAGE
NET
VOLUME
3 ^3
it A3
0,0
S\fO
MULTIPLIER
44/100
32/100
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ffl/100
TOTAL
MOLECULAR WEIGHT OF
STACK GAS (DRY BASIS)
Md, Ib Ib mole
IH3
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0,00
a^-0!^
w.n
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FIELD DATA
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SAMPLE TVP
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OPERATOR _
AMBIENT TE
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kEFERENCI
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Jl .8127976044
^i \ d7, Uy7u7':::;'v
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DRY MOLECULAR WEIGHT DETERMINATION
PLANT.
OATE_
16 >• 71
COMMENTS:
SAMPLING TIME (24 hi CLOCK!
SAMPLING LOCATION
HViV. |R
SAMPLE TYPE (BAG, INTEGRATED. CONTINUOUS)
ANALYTICAL METHOD OfV/
AMBIENT TEMPERATURE /|ff*
OPERATOR \y.'f>"\
\^ RUN
GAS .^\
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02 3*
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READING
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READING
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NET
2t
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D-0.
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NET
VOLUME
^ <
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0-^
f
mw
MULTIPLIER
44 '100
32/100
M/100
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TOTAL '
MOLECULAR WEIGHT OF
STACK GAS (DRY BASIS)
Md. Ib Ib mole
'l.fffi
' 5- 5*6 7
0*0
Z2.93567
Z.°).|-8|37X
-------
FIELD DATA
PLANT.
OATE_
SAMPLING LOCATION
SAMPLE TYPE _
RUN NUMBER _
OPERATOR _
PROBE LENGTH AND TYPE
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AMBIENT TEMPERATURE .
BAROMETRIC PRESSURE .
STATIC PRESSURE. (PI _
FILTER NUMBER Is)
. >9
ASSUMED MOISTURE. %
SAMPLE BOX NUMBER
METER BOX NUMBER
METER AH0
C FACTOR
< •
PI TOT TUBE FACTOR
REFERENCE A p
MOTE
READ AND RECORD ALL DATA EVERY.
MINUTES
>
03
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POINT
NUMBER
(>
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^151
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SAMPLING
TIME, mm
CLOCK TIME
(24 hi
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ii.
40 /
£5L_
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(Vml. It3
VELOCITY
HEAD
(APSI. in. H;0
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£
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TEMPERATURE
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(Trajn),«F
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lApji. in H^O
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FIELD DATA
PLANT
DATE *
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NOZZLE I.D..
SAMPLING LOCATION / riA^;
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METER BOX NUMBER _
METER AHg l.7b
CFACTOR
PI TOT TUBE FACTOR
REFERENCE Ap
NOTE
TTT
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NUMBER
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\. CLOCK TIME
TIME, mm X^
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PLAMI.
OATE_
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SAMPLE TYPE £j
RUN NUMBER \
OPERATOR fl
AMBIENT TEMPERATURE
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STATIC PRESSURE.
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1
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TRAVERSE
POINT
NUMBER
A~\o
PLANT T^X«aV-N V\ v a^v^v \A vv-^
DATE ^-T-S -"7 °t
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DESIRED
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S" MINUT
STACK
TEMPERATURE
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75 >o,fc
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METER AH^
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NUMBER ^T-0 "*
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REFERENCI
NOTE
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DRY GAS METER
TEMPERATURE
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91
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TEMPERATURE.
°F
IMPINGER
TEMPERATURE,
°F
-------
FIELD DATA
PLANT.
DATE_
w% — VA t« U. \ vwJ
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
OPERATOR
}«v»
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE _
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PLANT
DATE
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SAMPLING LOCATION Scr6tA><»r- tEV> .
SAMPLE TYPE
RUN NUMBER .
OPERATOR _
VUe///
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE.
-------
FIELD DATA
PLANT.
DATE_
SAMPLING LOCATI
SAMPLE TYPE
RUN NUMBER
OPERATOR
PROBE LENGTH AND TJffE.
<• NOZZLE I.D..
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P.)
FILTER NUMBER Is)
ASSUMED MOISTURE. %
SAMPLE BOX NUMBER
METER BOX NUMBER
METER AH, Vj
C FACTOR
PI TOT TUBE FACTOR
REFERENCE Ap
NOTE
READ AND RECORD ALL DATA EVERY
r
MINUTES
TRAVERSE
POINT
NUMBER
GAS METER READING
VELOCITY
HEAD
(iptl. in. HjO
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjO)
DESIRED ACTUAL
STACK
TEMPERATURE
(TS).°F
DRY GAS METER
TEMPERATURE
INLET
ff.jJ.-F
OUTLET
PUMP
VACUUM.
in. HI
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
"F
n.V
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75
70
DO
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FIELD DATA
00
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TRAVERSE
POINT
NUMBER
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PLANT <"*- Vx'C' *> x*">7/ >., «? /-."«•• /
DATE rf- k>ya.>=i - X'?
SAMPLING L
SAMPLE TVP
RUN NUMBEI
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AMBIENT TEI
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PLANT
DATE.
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SAMPLE TYPE
RUN NUMBER.
OPERATOR _
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AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (Ps)_
FILTER NUMBER Is)
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PROBE
NOZZLE I.D.
ASSUMED MOISTURE. *
SAMPLE BOX NUMBER
METER BOX NUMBER .
METER AHa |_
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^
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REFERENCE Ap . "^4
NOTE :
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(Vral. It3
VELOCITY
HEAD
(AP$|. in. HjO
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjO)
DESIRED ACTUAL
STACK
TEMPERATURE
(TS).0F
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TEMPERATURE
INLET
CO
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l£
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MS
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FIELD DATA
00
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POINT
NUMBER
^ 2>
^M
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PLANT iz.xx'O' Ur&^«i>*~-
DATE '1/1&/7H
SAMPLING L
SAMPLE TYP
RUN NUMBEF
OPERATOR
AMBIENT TEI
BAROMETRIC
STATIC PRE<
FILTER NUN
\v CLOCK TIME
15 — —- ~
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AND RECORD ALL DATA FtfFHY S MINUTES
VELOCITY
HEAD
(APS). in. H20
,07
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\jp~
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/f OS \
- Ai.6 J
5?f^
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED
1.65*
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ACTUAL
1.05*
^fm
»
1
- kf 57*
STACK
TEMPERATURE
(TSI.°F
M-Tf -
IKTIIHE 1 S"
I NUMBER •**"
NUMBER I3Q./T
' t .09
IE FACTOR
i An
*V t
DRY GAS METER
TEMPERATURE
INLET
IT.iJ.-F
fa.
5^
ag
W
^
c\^
*(£
^G
R7
q&
<^g
q
6
^
$
i?
9f
^Js
C
t
t
«
R
v«
S&(el
^ 1
OUTLET
SO
8)
gl
sa
sa
si
Cf IA
Q Jj
Cf ff
g^
?j,^^
& f^
&
^o^5
^fi
^C
%£
ff$.c
-•
litzcf
— ^
PUMP
VACUUM.
m.H|
a
^
•a
^
^.
"2.
a
a
3-
3_
0
a
^
o.
3.
•^
0.
2^
^
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
-------
FIELD DATA
PLANTJEx
DATE
SAMPLING
SAMPLE TYPE
. RUN NUMBER
OPERATOR _
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE. (Ps)_
FILTER NUMBER Is) :
PROBE LENGTH AND TYPE.
NOZZLE I.D
ASSUMED MOISTURE. %
SAMPLE BOX NUMBER
METER BOX NUMBER
METER AHg
C FACTOR
PI TOT TUBE FACTOR .
REFERENCE Ap _
NOTE _
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
VELOCITY
HEAD
(APS(. in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HJOl
DESIRED ACTUAL
STACK
TEMPERATURE
a$i.°F
DRY GAS METER
TEMPERATURE
INLET
ff.jJ.-F
OUTLET
00
fi'
.N
71
I
s
3CL
_Su
.s
207,7
il.C)
10 1
l&H
ICDI
I/O
<*; (4)
2JL2L
-------
FIELD DATA
PLANT.
DATE_
a n\ ^ W
SAMPLING LOCATION.
SAMPLE TYPE fj
RUN NUMBER
OPERATOR i
.yg 0*o EtJ. -
PROBE LENGTH AND TYPE.
NOZZLE I.D. .
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE. (P$)_
FILTER NUMBER Is)
(. ',-*r
ASSUMED MOISTURE. \
SAMPLE BOX NUMBER
METER BOX NUMBER
METER AH^
C FACTOR _
, •»?*
PI TOT TUBE FACTOR
REFERENCE Ap
NOTE t-<- '
Oo •
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
ivmi. it3
M
VELOCITY
HEAD
(ipsl. in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. Hl
DESIRED ACTUAL
STACK
TEMPERATURE
; a$i.°F
DRY GAS METER
TEMPERATURE
INLET
(T0 ,„»."?
, OUTLET
PUMP
VACUUM.
in. H|
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
CVv. f-t,
C
±J-
~? "5
( V
"77
>
I
3L±
O
TZtt
55
H6.7
-&
-------
FIELD DATA
DATE
SAMPLING LOCAIIOH
SAMPLE TYPE FC\
RUN NUMBER
OPERATOR
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P.)
FILTER NUMBER Is)
PROBE LENGTH AND TYPE.
NOZZLE I.D
ASSUMED MOISTURE. *
SAMPLE BOX NUMBER
METER BOX NUMBER
METER AH,,
C FACTOR
PI TOT TUBE FACTOR
REFERENCE A p _
NOTE _
READ AND RECORD ALL DATA EVERY
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
•V- H3
VELOCITY
HEAD
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HO)
DESIRED
ACTUAL
STACK
TEMPERATURE
(T$t.°F
DRY GAS METER
TEMPERATURE
INLET
OUTLET
(T"oul'-°F
PUMP
VACUUM,
in. H|
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
"F
I 7
16
M.s
M.
HO.
4.S
HX
06
IOO
17,71
. 0,
-------
FIELD DATA
PLANT.
DATE_
i
IQ I I 1
SAMPLING LOC
SAMPLE TYPE
RUN NUMBER
OPERATOR
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P$)
FILTER NUMBER Is) ~2~E> */ °-j
PROBE LENGTH AND TYPE.
NOZZLE I.D
ASSUMED MOISTURE. \.
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AH0
CFACTOR
-4\*
PI TOT TUBE FACTOR
REFERENCE Ap
NOTE
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(Vml. It3
VELOCITY
HEAD
(ipl. in. H0
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjO)
DESIRED ACTUAL
STACK
TEMPERATURE
(TS».°F
DRY GAS METER
TEMPERATURE
INLET
«„,„). «F
OUTLET
PUMP
VACUUM.
in. HI
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
JS
>
I
QA
Jil:
it
Ji_
o.o
fiC
^T
-------
PL WIT.
OATE_
SAMPLING LOCATION
SAMPLE TVPE
RUN NUMBER
OPERATOR
AMBIENT TEMPERATURE .
BAROMETRIC PRESSURE .
STATIC PRESSURE. (Ps)_
FILTER NUMBER Is)
FIELD DATA
-.*/
PROBE LENGTH AND TY
NOZZLE 1.0.
ASSUMED MOISTURE. %.
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AHf
CFACTOR.
"f,
PI TOT TUBE FACTOR
REFERENCE A p _
NOTE _
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(Vml. It3
VELOCITY
HEAD
Ups). in. H?0
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjOl
DESIRED ACTUAL
STACK
TEMPERATURE
(TSI.°F
DRY GAS METER
TEMPERATURE
INLET
lT.jJ.-F
OUTLET
PUMP
VACUUM.
in. HI
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE,
"F
O
;.
. 2,
/- 3
VD
OJ
^l
Tsr
o
? • /
fTA.
y.
4-0
-
. o
/.#
y. 3
/.£&
-
9°
Z1.O
S0C
X.
oe*
-------
FIELD DATA
PLANT
DATE
SAMPLING LOCATION^
SAMPLE TYPE _
RUN NUMBER _
OPERATOR '
AMBIENT TEMPERATURE .
BAROMETRIC PRESSURE .
STATIC PRESSURE. |P$)_
FILTER NUMBER Is)
PROBE LENGTH AND TYPE
NOZZLE 1.0. «£/>£
ASSUMED MOISTURE. \
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AHa
CFACTOR
,a •fe*;*'
PI TOT TUBE FACTOR
REFERENCE Ap
NOTE
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(Vl. It3
VELOCITY
HEAD
(APS), in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjO)
DESIRED ACTUAL
STACK
TEMPERATURE
a$i.°F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in. H|
SAMPLE BOX
TEMPERATURE,
IMPINGER
TEMPERATURE.
"F
'-. 3
Z.-£
^{_
99
I
^D
3
y.
- 3
x. B-
/.
£^
X ?5
2£
.
s^
A
£^L
x^A
-^
£'.
>- 5
»g
/ r
^5L
/.
f5
te. O^
-------
FIELD DATA
PL ANT
DATE
MMPI 1HC LOCATIOII
SAMPLE TYPE 23
RUN NUMBER
OPERATOR
- f? , •„
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P$»
FILTER NUMBER Is)
PROBE LENGTH AND,TYPE.
NOZZLE I.D. ->//
ASSUMED MOISTURE. *
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AH0 -__
CFACTOR
PI TOT TUBE FACTOR
REFERENCE Ap
MOTE
+> '/ ' S
& '*- -^ -£*-,
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
GAS METER READING
ivj. n3
VELOCITY
HEAD
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjO)
DESIRED ACTUAL
STACK
TEMPERATURE
(Tst.0F
DRY GAS METER
TEMPERATURE
INLET
(TB,n)."F
OUTLET
PUMP
VACUUM.
in. H|
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
/,
5
^^_
-s
wo
VJ1
/•
X
S . 3
ffr
• 3
. *>
/&J
~/&
. *r
-------
FIELD DATA
TRAVERSE
POINT
NUMBER
PLANT <£TxVO»>
DATE CO ~ 1 — ><7
SAMPLING L
SAMPLE TYP
RUN NUMBEf
OPERATOR .
AMBIENT TE
BAROMETRIC
STATIC PRE
FILTER NUN
\. CLOCK TIME
TIME, mm >^
<5 ~ -feL«Ci3_
-5-
so
/•S"
5tO
^<$
iro
&•£
4-O
4-S
^O
55 » 6 i.^
•>Co~-
, /•? 7/ / ^
...f ' ' -L L— -1
KATION P^ol^VAv^a «^«.^. KVv«:
E KM. f ' < U' J V7J 3" i:
I 1
Sa.^o v^
-
•PERATURE SI S °P
:PHEKURF 2-^.ou- ,0^, =,1%, .<5j
SVIRF (P ) z • 5
RfH(f) ?«-'*' tfc f*
PROBE LFKGTH AND TYPF 3 ' 5 T^tAj 4- <. ^
^T
NOZZLE 1.0
ASSUMED Mt
SAMPLE BO)
METER BOX
METER 4Ht
C FACTOR.
PI TOT TU
REFERENCI
NOTE 1
1 I
i.~i -
IKTURE 4 "*
C NUMBER A' •^'V«-tt^ X
NUMBER ^ »- »-tei.
• V »f 1-
IE FACTOR
• An
. —
1 -A
— \5
READ AND RECORD ALL DATA EVERY_£L_ MINUTES
GAS METER READING
(Vml. It3
"i ^ i i*2» *7 ^
( o \ < ^ ^ O
lit .T_\\
5"«f., ^<4
T T- SS"«VN,'^
.-.-' ;l ••
f.
DRY GAS METER
TEMPERATURE
INLET
US"
") V
~?9
•fc^
^ 5
\t>0
lio
l i 1-
Ui.
11 8
^6,.5^
55 /
(
^ —
OUTLET
•*:. -
.^ •
PUMP
VACUUM.
in. Hf
7
"7
1
-7
7
-7 •
-,
->
T
")^
- —
?f £ a
=- — •=
SAMPLE BOX
TEMPERATURE.
°F
^^^^^
Sfr-£vf ^
^- — "^
IMPINGER
TEMPERATURE.
°F
-------
FIELD DATA
PLANT.
OATE_
PROBE LENGTH AND
NOZZLE 1.0. __«_£
SAMPLING LOCATION
SAMPLE TYPE
BUM MIMBFR
QPFRATOR
. S .
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE I
STATIC PRESSURE. . It3
VELOCITY
HEAD
(Aps). in. H^O
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjO)
DESIRED ACTUAL
STACK
TEMPERATURE
(T$I.°F
DRY GAS METER
TEMPERATURE
INLET
(TB,n)."F
OUTLET
PUMP
VACUUM.
in. HI
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
"F
60 ±
/D
^777
!o3
8O
Vo
ti5-
£LX
3^7
-------
FIELD DATA
PLANT.
DATE_
SAMPLING LI
SAMPLE TYPE
RUN NUMBER.
OPERATOR _
'i
f(A\
PROBE LENGTH AND
NOZZLE I.D.
3E
AMBIENT TEMPERATURE g 0
BAROMETRIC PRESSURE
STATIC PRESSURE, (P$) *-k
FILTER NUMBER Is)
ASSUMED MOISTURE. %.
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AH~_
CFACTOR.
-------
FIELD DATA
PLANT
PROBE LENGTH AND TYPE.
DATE /6/'/7*> . _ . M077IFID • »2«
1
vo
VD
I
TRAVERSE
POINT
NUMBER
SAMPLING LI
SAMPLE TYP
RUN NUMBEF
OPERATOR
AMBIENT TEI
BAROMETRIC
STATIC PRE!
FILTER HUM
^\ CLOCK TIME
TIME. rain Xp^00^
S" — — /4rU^L
¥ /t/7
y
/7'7 /($'%•¥:
• :
x-AT'nNl^ry-er 4trJkV4?v O<
E P.S /
i O*^_
tt 'f^fl/'^f
jflr
ASSUMED Ml
SAMPLE BO
METER BOX
1KTURF 1 *~
K NUMBER ~~
NUMBER ASl-S 3
METER AH,. 1 , *S?4
HPFRATIIRF ?C
PBF«IIRF -l-l..^?.
^|RF |P ) • ^O
PER it) ^> *--^ -5y/f
c FACTOR " - ^7
PI TOT TU
REFERENC
NOTE
BE FACTOR
E Ap •
^^
RE AD AND RECORD ALL DATA EVERY f MINUTES
GAS METER READING
IVm). It3
V7/ ^-3^
f> C) . 0 ^O
'- — ^r.&fs i
»•*
;) .M/? (<23.ftv +
y>j$fjC4bO1~
* '
VELOCITY
HEAD
IAps). in. HjO
i
/3.6 )
/^V"
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjO)
DESIRED
/ -<3
^.
~ jAi
ACTUAL
M
*7r
STACK
TEMPERATURE
(T$».°F
—
/
1i-
7>'^
)30
DRY GAS METER
TEMPERATURE
INLET
.^--,
OUTLET
/[> if
/ <; r p«A.
i.
PUMP
VACUUM.
.in. H(
^
N,
-•:
&.
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
"F
-
-------
-------
Appendix B
Laboratory Reports
-------
Plant EPA~ GftPifa
if PARTI CULATE SAMPLE ANALYSES Analyst
H/ Sampling Location^. &U&4-. £&&<. <3ufi-&
GvrC~ Date
"Run * /
Teit Date /?-«?7~7? Test Period ?-37 / /0-I-7V Stack*
Befker jVo^yme
FHA /-S-/
FIITFRj # £54«/0
/^
15
FIITFR' #
'• FH Tr,T*l ,
RHU
™A . . , ,
IflTAI
"\
. 'ill
:'l
!•'*
Tare(l)
grams'
I/O, l f
,<-ffplil
T*
Comment* __, _ „,„_,
Plant &?A~ fab.
i Test Date ^Zl'?'*
!• ". ' '
i Beaker
FHA 1-S-Z.
! S FILTER, it 3SV~L.
I Vta 3")
"WUP
//O. 2j>3$~
. VL»a*7
*
trSS5
O.0o75"
/0-/a--" \
Process*
IBIJL
jr-
CL C coo Of i
f
,1
•i-
ii;l
!>/^V Sampling Location d* %&**'• SctUA. ^tfHc^n * 3-
7^ Test Period 3-3-7 J /O -/-?? Stack*
Vo^me
3?O
i.
•i!:'
;
i'
jii
•.•J;i
:''' * .Comments
Plant £Ptf- "fa
Test, Date •9*^7'
//^. f/S'S
<4-l*DO
Tare (2)
grams
//O. ff/ffS
,¥•&$
FinfU,,
nO. 53^
. tl^Dl
Final(2)
a rams
"°iy|^>
Mb
^
o.oo&o
i.OOI3
'!•
I
jcess*^
La'-
G.QItft -0.0600077
",
I
i • <
i
V
ft
|![ *'••-•• : • ' ::!; '
^^IX « Samolinq Location^. /^U*** $CSUiQ-t o un # J3
r^7^ Test Period /-Z7 / /0-/-77 Stack*
Net wt.
qrams
O.d 13ft
0.00/0
•
Process*
i Beaker
rF
FHA AS-3
FILTER, # J5400
FILTER; #
FH TOTAL
BHW! .
BHA
TOTAL
K>,
•
•J
•|,i ,
lume
til
/'/-i
i.'
•It '
if
|i
*
if
q i^ams
fG£» Cf 36^»
V^/7
Tare (2)
q rams
/OS. %3b2~
.yl0l%
i
•in
qrams
/o£y &Sfi&
, VC?«2->
,;*
;;
Final(2)
grams
, ^(pJcj
r
•
A Wt.
grams
O. 0/33
Bl'k. Cor.
qrams
O.o 000077
•• •
t_
i
Net wt.
grams
O.o/o
O.OO/;
|g ooi£- I o.
Comments _.
ACETONE BLK tS-31
- WATER BLK : "1
CODE: , FHA-Frontj half acetone wash ;.BHW«Back half water(!mplnger contents + water wash) BHA-Back half
» , acetone'wash FH TOTAL-Front,half catch weight ,TOTAL-Total train catch weight >
: ' . ilil ' ' . '.:•. . ' • , . . _ ..;,
-------
Plant
; \
i • i
PARTICIPATE SAMPLE ANALYSES
Sampling Location
Analyst
Date
Run #
Comment»
Plant.
Test Date
Test 'Date #-27~79
Beaker iVolume
FHA '•' /S-'f HfO
FILTER, tf ^?ffV«/3
FIITFR' #
FH TCTfcL
RHU .v':'
P.HA ,: ; j
iiji
t
Test Period O^
1!
1-
IftTAI :• I.. | :
to 8 .9f2o
lU^of
!
"urtfl)
/DSJ.'T?^
|t.-)yt/
»vui)
fO£.<9'!W?7
tfjtftH
^
O.OZV7
i
0.0000077
• '
f*8Fa«-
0.0ZS2
0.0137
Sampling Location^
' "Test Period : 'Test Period <9-77 / ft /O-/-7*) Stack #
'•i^r^
FHA ; /.s-6
, - ; FILTER, # «?^^>3
.:/:- FILTER; #
! i.ivV FH TOTAL .
BHW •:.:: .
Z3S
':'
•j*
'•'
BHA
';•'••' TOTAL , i
r?flij)
/0&. £34-b
.tKoZf
Tare (2)
grams'
/OS. 534/
'ttojCj
1
1
1
'
j
'W
/&5 ?yTQ
. v^^L
Final (2)
grams
/OS. S&T&
, VLQ6-.
V
i
1
grams
-------
PARTICIPATE SAMPLE ANALYSES
Analyst
Date SO ~S° -''
* :'•'.'""*:
Plant trr/y "" (lowJlA^ Samplinq Location (/lU&. f?uM< d>t*-2. Run # /'
Test Date #-27-'7Y Test Period tf~/~79 Stack # • '• >
Tar^)
/03* S^3O
.^<)
• f it>Lo
^
G.G/6,4
Pi
Blj
•ocess#
i ''
5ram?r'
r>.OOOOo77
f§ra)!!$-
0. OlW
A.&IO2.
1 • Comments : -^
. ' '. ' . :' ••I : - : ' ., i; . ' ' :,|
Plant c=rn "C&jfe&'L' Samplinq Location (2/£V<*. rst&44* * (9-gfe. Run # «2_ '
' v Test: Date *5~27-7*/ Test Period
.,'/' . '•,, ':; '" j Beaker
* FHA AS"-g
^ FILTER, rf .^54^7
: £ FILTER' #
1 ^ FH TOTAL .
; . BHW
•:•• "•• •.'.•BHA :
; Z TOTAL ;
Volume
mT
V2^>
• : i
-'
)
"'•1BU)' '
//O. 64bO
,L((af~ff
'
^~Z7 TTD /o 1-13 Stack #
i Tare (2)
! grams'
tio. CM
,*HaC~]
^5
3
'
* Comments i ' •'•
'i '•. plant QPfr—C&0A&l*, Sampli
:!•'" Test Date •• '.'"V'BHA , . • : !;
PS • • : i TOTAL .. j-:i:
:iffti)
/Ol~ ¥33 0
ilfolg
ng Locatii
eriod 9
Tare!
qran
Final (1)
grams
/ j£>.c>7S7
-------
• - •'•'
'"• • r"ft?j^- f* *
Plant CTi n _~~ \-&
Test Date ;•:•; ,:i-r^ ;: i'!:.
! t PARTICULATE SAMPLE ANALYSES i Analyst
*d&^ Sa
^ Te
ime
35^
; FILTER, U &5WZ. .1
:4 FIITFR' # ;!
.'• FH TCT*L i
. •: •• RHU' !•..:) , •:
',
Tare (1 )
qrams
Tipli
st'P
J0t>.(ol>3%
lflalci '•
i
' . •: RHA •-•• | •••
107AI
'!
. Comments '
• ••'. •'•: •'.'-. •; |
; '•'' Plant &%&-
i Test Date <9~27"r
•. '1 '". . •• 'i .•-•'-'
.'''••• •.':,'• i
i ;'•'•.-: Be|ker
'•• FHA L$-/(
j § FILTER, it 3$W£
™ t FILTER' »
*•' \ % FH TOTAL
BHW
• "• •:. BHA
i £ TOTAL i
tf°m^
\
Q*t*:»
7<^ r : Te
me
4 So
,
|:
1
,',
' * Comments ' ;
' ! ^ .-'.
i Plant £fti-''\
i , Test Date cf~T.ft
'iflil>
nq Location ^/lte&-> T/WWS. rT~.
(£$&• Date /O-J 0-7*1
Run # /' • '
eriod
/0&f (/b$$
, «^L>/9
•
t
i
"urtfl)
|D6? . t^?P
. r-4»3a
Final (2)
/0u?*fo&>i&
.«/C«>V2
^
0. 00*7 ">
;Pr
Blk
ocess#
fafer.
0.00«^d77
mpl i
st P
i
i - .
' •; 'i
/OS, *74rft<5'
^tftoOlt
ng Location {/LUA' / t/l&n*-. rJ7 Run # ?
eriod ^-27 >4> ytf~/-79 Stack #
! fa re (2)
',l; i !, grams .
/05". 74-f11?
^/toCfc
'
i •
Final(l)
grams
/O5tlSf1cl
,33.
.
;
Mfe
it '*
Pr
).
, ''!
B1qk
r?w-
'<0*QO4<(
Q . OO/f
ocess#
•
•
O.OO?-^ -dtOOoocSTl
\
1
V ^ > -:' ' ^ ^' •
-^^U 'samplinq Location (/U**. 'T/ietrt/*'. Pfr Run # -3
'-77 Test Period <9—27 73 /*-/-7? Stack #
•'. !•':•: i: \ !!
;i , . :i ;i | Beaker Volume
: ii : FHA L>~l?>
i • FILTER, # J£?W>
, :! .. FILTER, # -.
,- ,.i:: FH TOTAL ''
''» "' - "BHW'y •• ;,
•? 60
;!i
' ii'i"
','y.kf :; BHA :- i j:!.:;:
JfV^I • •"• TOTAL • • 'i j ;'•:.
»'• '"--^ • " '•• • Comments i ' Ii
i'&'MJ ACETONE BLK
!*•]:{ WAIER BLKh
[:f|
-• (Vvr • ' •' :/•' •• .- i i ii[
i
• T§flW, .
/Q3> tfolbf
,i/^^3
Tare (2)
q rams'
/^^. O2-b(f
i*f£ 93
i
i
i
'Final(l)
arams
/OX . p6/)O
i , *yi» <3(/
Final (2)
grams
/b'S. Of9£
. ^^/
i'
i i
H
i
grams
•£>*03^4
•i
*$&-
£>.OO£,C
O,C&2.(t
Process^
pi
Ntt"
^ O0000T1
1 ' •
t • .
J
!
Net wt.
grams
G. O3O(a
G. OO/t>
t ,)•
i
''i.
;i
. . . . .-
CODE: i FHA-Front half acetone wash BHW-Back half water(lmplnger contents + water wash) BHA-Back half
|ru TOTAJ-c-ont|u-1f c«*-u we^-UJ- TQTA1~'Totfl '
-------
PARTICULATE SAMPLE ANALYSES
nalyst_
Date
-/.<2^2>
i W6"7D
Final(2)
g rams '
1 c?> , OJ^?
.4L~?S"
Awt.
0^)i)^4
Common is
Plant C^i/J C&-£-/fc€/\~ Sampling Location /7tJ^^M_--o^-^^" Run # ^-
Test Date <9~Z#-7
/^^ i? 220
WtjU U>
Tare (2)
g rams
/O4. %2/S
• ^(oHCp
Final(l)
g rams
IC?^ .^^^
<-Ho $"5*
Final (2)
g rams
JOM'i&i£-5'
.4^55"
A Wt.
grams
0.00t>7
Process^
B,VaS?r.
Q.CO00071
Net wt.
qrams
£.OOt£
frOGt^-
Process^
Blk. Cor.
I grams
O.OOOCOT]
i
! :
" *
* Comments
Plant ^Ffl C&3/2&^' Sampling Location f^^^^'L^C^^^^U' Run # j^
Test Date ^-Z^ -79 / Test Period 9/^7 ^ 'TO /
FILTER, rf
FH TOTAL
BHW
BHA
TOTAL
Comments
ACETONE BLK
WATER BLK "
CODE:
Beaker
ff
LS~/£
35W
i/olume
ml
^25(5'
Tare(l)
grams'
//
t-lb^Ch
Tare (2)
qrams
//^/. 4//3
.^S"^
1
Final(l)
qrams
|IO •Wl^t/
, H(f70
Final (2)
grams
}ID . 1 1 ^O
.V6 7J
Awt. iBlk. Cor.
qrams qrams
0, 0 Oil \p.OWo 7 "7
!
j
i
.
Net wt.
grams
O.OQS7
O.&OI4
FHA=Front half acetone wash BHW=Back half water(impinger contents + water wash)
acetone wash FH TOTAL=Front half catch weight TOTAL=Total train catch weight
BHA=Back half
-------
(Plant
Test Date
PART ICULATE SAMPLE ANALYSES.
Sampling Location_
Test Period .
Saiiipllng
Test Pefiod <9-Z7
Run
/O-/-V9 Stack
.
Tare (2)
qrams
/O7.
Final (2)
a rams'
Sampling Location
i Test Period a
Run #
Stack
Tare (2)
qrams
Final (1)
qrams
Final (2)
grams
process^
Process^
/OOfcft
WATER BLK T
CODE: .iFHA-Froritil ha if-acetone wash ^ BHW=Back half water(lmplnger contents + water wash) BHA-Back half
acef • 'fwaa1- flTH 1ifrA1.«
"-tch.«-«»qht „ TnTAL-70<-«l train catch weigjit
7
-------
.'• • -I! '«' ' • .' i1 .' ' ' • '•<••
: Riant £P/9~ &
• " • Test Date ^-^~7
!:l : : , ,
"f . : "PARTI CULATE SAMPLE ANALYSES' ^v
te4&et* Samplinq Location <£fsiu&-* c&
Analyst
CSs^- Date /O-SO-tf
Run * / ' '
I/ Test Period /<0-y-79 Stack* Process*
• ' Be|ker |VorVme
','•' I FHA /-S-/f /SO
'.! .-'-, FILTER1 # ^SyO* .
FIITFR' »
i , FH TCT£L .,.,
'is
,f
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Tare(l)
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/OS. -4303
. *W,o~7*/
'••'}• • -' EHA • •• ':"'
"!• : TOTAL
• .'' •
1(1B>
/&S.49OI
. '+to'~)
10^, SO li'
• y-~)i 5~
4 wt. Blk. Cor.
qrams grams
• Oil 4 -6Cb«>T7
1 :;
'i:
l|
i
ftfjfli-
•C>(O'2>
•»Oo3S
•
i • Comments ; ! ; . D/ */3
i, •.:".•• | -i
'"•':'•'.' ; i '' ':
: 1»1 J- 3~-P /I" /
; Plant f^i rJ t
Test Date *t> /£»
Volume
ml
39t>
: ;
L-.l
'«nij>'^
/O4-64O&
, */^V3i
Tare (2)
grams
/0*fc b4Qb
. */i*fa
; : .
', &*M*~ Run # 2. i 'l:f
-X'74? Stack * Process*
Finalfl)
grams
itrf ,(r»5c?3
. <4l,tt£
' Final(2)
a rams'
»O«.i,\"D 3
• 'iff TO
t
i
Awt. Blk. Cor.
qrams qrams
-Onfl'7 .CQOoe>?7
•.
»5W-
,DC>6>7
-OOol3
01 Comments : .OA^O
f. '..-'• .' _,"• '' ;'' "i; ; • :
Plant ^'rj." L&^/s&l' Samplinq Locatlon^x^^^t^^^t^c
Test Date ^-i?^*7
•III
&*^- Run * ^ If
9 Test Period ^-«5V )^O y<9-/-?9 Stack # Process*
! ' Beaker Volume
i : _ ff nil
: THA ! L$-2-\
r FILTER, *i i?5"V/5
< FILTER; *'
;.."! FH TOTAL j
/(/O
•fi
;:l|
i !•!
•' '-\\ '•: BHA '•• \ \ : !!
':;1 TOTAL i1 j ;
,i ' Comments : ;
'.'-!< ACETONE BLK
i WATER BLK. '
Ill
•'•"
''Sail)
/ 0*7. 0355
. YfotfO
Tare (2)
q rams
/07. 22-5^5
.Vto^b
i
:|
Flnal(l)
qrams
/O*7 21^ ft
. *\(JrfL>
Final(2)
grams
/ JO"?' 33 C A
, LHa>
i
i
i
!
. '! '•
A wt. iBlk. 'Cor.
qrams qrams
.Ocpn ,nOry»f7
I
!
? !
i i
Nefa«t.
»OO*t
»OO/ b
! • ' .r^/OA
i • '.
i "•.;"" : ' '
. iit
,1
•
CODE: ' FHA-FrontRhaIf acetone wash BHW-Back half water(Implnger contents •«• water wash) BHA-Back half
1 acetone;wash FH TOTAL«=Front half catch weight TOTAL-Total train catch weight i
-------
P(Iant
Tes t Date /b -I-74
i:PARTICULATE SAMPLE ANALYSES
Sampling Location,
Test Period "7*27
Analyst,
Run
/<3~/-7? Stack
Date
Process)?
7
00
Be
FHA
(Volume
mi
FILTER! # ^StflS
FILTER, #
FH TOTAL
BHW
PHA
TOTAL
Comments
Plant
Test Date..
•'!/•'• .1
Bffi — •
Beaker Volume
,• mT
FHA
FILTE*
FILTER, #
FH TOTAL
BHW
BHA
TOTAL
Comments
Plant
Test Date
'/too
FHA
FILTER #
1 ff|
>n 7\
•AL
FILTER
FH TOT
BHWi
BHA
TOTAL
Comments
ACETONE BLK
WATER BLK
CODE: !
. 2737
JOl .
ing Location
Tes t Peri od ^ •
//>-/-? ^ Stack #
Tare (2)
grams
Final (1)
• grams'
Sampling
Test; Period
Stack #
aw
-OI
Process^
O/ N
Process/^
Beaker
/-S*<94
JSvSle
K
l/ol
m
/5^. ?
• f&i'i
P 1
t?W
^
Final (2)
grams
ipC.li ?M>»
.V5*V^
-
A Wt.
qrams
'OO^-fS'
'
•
1
1 1
"'o-rams"-'
»CCfMrT?7
_
'.
*
M^JU-
• GoS?
.Oo lC
^r
OOCI7
FHA-Front!'haIf acetone wash' !BHW»Back half water(tmplnger contents + water wash) BHA-Back half
ace£ ,wa|; FH^—>Fr|;- half --tchr-'ghtt •'"TALi-'—Tl tf-'- cat-1- well1-'
-------
*t • •.. '• ' • ' tl'-'Hii •:'... • • : •• : •' ;:
•'. ': , - . ': •• - :'!!l'i . '' PARTI CULATE SAMPLE ANALYSES * i A. Analyst
Riant fcfTtf- C&^hfiQ**' Sampling Location S&W&- *>KJU&
6V^- Date /0~/O~79
Run # /
Test Date /0-/~79* Test Period <9-Z7 <*> S0-/~79 Stack #
; ; Be|ker
r •'.;'' FHA /-S— P-8
FILTER, tf ^5V/Z
:,.j!
Vol yme
/t>s
FIITFR' #": i;;
•:; •'"•' i FH TCT*' i .J; .
• .-:•• BHU I . .'M>
Tare(t)
grams'
/03.0/66*
Mto8/
:• ' : ' RHA • '-I-!
IflTAI
•j'i ;
•.:lnfl,
/03,o/k/7
«f U>5*5T
! '
"'urtJU' :J
te*V. 3vUi7
T./**o5"
Fi nal (2.)
g rams
|nM.7*i,ac
i.Woo
pSs
/ >2tH % I
Process^
l
Blj
'1
•Oflroov?
Comments •!'!...•.
: ' i, • ' ' ' ' :' !|' ..';•....•:.
• :!"•' ' ''1 •"! • 1 ' i
•";:. Plant &PA- G**f&\^ ::SamDli
; Test Date /0-7~74 i ;;Test;F
| . • • j Beaker
__£___
i. FHA ^S~^S,
I 5 FILTER, rf i,55V52
- ff il TCR" -tf — H — - —
(/) r 1 L> 1 C>I\A Tr '
i ^ FH TOTAL i
7 . BHW i
^ : "• BHA ;
; S TOTAL !
:•!!!
V°mYme
2&5
,•:
^— -
,-.
:U
. .1 i ij; . /.•
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,
' - ! ' :!
.: ' '. • "!j!:
ftg: Locat i on ^)>U^^u c^»t^5r
eriod Q/"Z7 To /O-/V9
i •, .; -T . •
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/^2,/4^4x
^ W-iL»O
- L _ • _ '.
•j "
i •
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grams'
In^.oTll'
*T -^fl?
•
Run # "Z-
Stack #
t
VD^.C^^J
5i 3lV")«V
•
t
Mb
• -t
!' ''''
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fext.1 1^
"7f// ^ /
1,
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'i
BH
|;
G>/71 /? ,000007
t
•
.
t :'
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/f, ol3
StbO/O
1 * Comments i ' . :i .-• • ; ' ' , "i
;i , Plant c^r/7 6&&y&^ l Sampling Location ^£slu>v~, r-T?l&jfr~ Run # 3
: Test Date ' ; Test Period 9 S&7 ***> /O"l"7el Stack #
". , ! ' ' . ' Beaker
' 5' -r*
FHA ! AS-&7
FILTER, # ?5
/^5"» /#4l>^
u'SH'L
-
1
• * /
Tare (2)
g rams '
/Of. / 8 40
i WS 41,
!
|
i
;Final(l)
grams
lo? //jW^I
• 1 i3>*f/5
Final (2)
gpams
lOS.m^ 1
/, ^«?IO
i
A Wt.
grams
- ^A-T/
Pi
w
t
•ocess#
c.gcor.
,000007
i
*
j
•V*-
»f (,i*i
'X'StX
f*2*^ l4^
• •, } Comments ' '• "!! .. i : • -; •
1;, '• ;' ACETONE BLK
iy...<-i'''' ••:'i WATER BLKi • "" "
'"!'
, mi
'••'i' ' '! •
• j
'"•* •*)•;••• ' p -; i • ••'tilt " i • • • •
; ;;!:,' CODE: • FHA-Frontl'ha If acetone wash
>.. :' -.'I ' acetone 1!wash LFH TOTAL-Fronl
J
BHW°Back half water (implnger contents + water wash) BHA-Back half
: half catch weight TOTAL- Total train catch weight
-------
PARTICULATE SAMPLE ANALYSES
Analyst.
Date
Plant czrn ^^pe/V Sampling LocationTt*t^#6ix &toM2tfo- Run ff /
test Date /O^l^f^ ' Test Period 7/£>7 7*o A>-/~74,y")75
^*?3\3
4Mb
0.3188*1
„£#!
.CXX)Ot>7
f^et wt.
^'2??^
^//35
. '/•(*> 1 0
Comments
Plant T^rrr" CgL&-,Ki&\- Sampling Locatiors3(>2^^u^t^ O(J^uct^~ Run ff 2-
Test Date /£>"/'7^ Test Period ^~^7 f^> /O~i~~l^ Stack ff
Beaker
ff
FHA LS~>b
Z FILTER, rf P5^?/
£ FILTER' #
? ^ FH TOTAL .
o - BHW
^ BHA
J; TOTAL
Volume
mT
V3?
i
/O4-.5'?37
i^5>1
Tare (2)
g rams
/^•^-. S^SI
H^Hl
Final (1)
g rams
/6^i (^"^1^
. sio;x
Final(2)
a rams
\ o^ . Wj^n
,<"/£> 3k.
Process/^
Awt. |Blk. Cor.
grams { grams
tC)^^^. /t>6C)oo"7
»C/1 ^'
i
'< \
i
Net wt.
grams
• octer.2
*0%&5
.} Tl b
86 Comments
Plant
£Pft~
Samp 1 i ng Locat i o
Run
Test Date /o-/-7?; Test Period ^-^ 7 72) /O-/~7^ Stack # Process^
Beaker
^
FHA 15-3&
FILTER, # ^25^5=4
FILTER., ff
FH TOTAL
BHW
Volume
3&Q
BHA
TOTAL j
^nU>
/&&., 3O3O
a-Stm
Tare (2)
g rams
/#6. 302 &
. vSyy-
!
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flT^-
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- O^HH
Blk. Cor.
grams
. C>O6O 9
M^a»i-
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,C)fe>^l.^
. )
Comments .Ojj ^f"7
ACETONE BLK
WATER BLK
1
!
CODE: FHA=Front half acetone wash BHW=Back half water(implnger contents + water wash)
wagh FH tOTAi.=Fr.ont hal/ catcK.weightm TOTAL=Total tjaln catch weight
BHA=Back half
-------
ill
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20
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-------
ANALYTICAL DATA
PLANT. _V:fJ*
DATE_ . ?:
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
SAMPLE BOX NUMBER
CLEAN UP MAN.
*• *>
f ft
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
CONTAINER.
CONTAINER
LABORATORY RESULTS
"B
FRONT HALF SUBTOTAL
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
CONTAINER ____
ETHER-CHLOROFORM
EXTRACTION
BACK HALF SUBTOTAL
TOTAL WEIGHT
e
rag
me
ig
MOISTURE
IMPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
a
ml
SILICA GEL
FINAL WEIGHT Vu-
INITIAL WEIGHT . °-°°
NET WEIGHT .
IV-5
"8
8
SUBTOTAL
TOTAL MOISTURE
B-21
-------
ANALYTICAL DATA
PLAMT PA
DATE
SAMPLING LQCATIQtfC/f/V^/C
SAMPLE TYPE
RUN NUMBER
FT-
2?r
SAMPLE BOX NUMBER
CLEAN UP MAN
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
COMMENTS:
LABORATORY RESULTS,
CONTAINER.
CONTAINER
FRONT HALF SUBTOTAL
f
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
\
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
IMPINGERS
j^L U\J
FINAL VOLUME ml
INITIAL VOLUME _££''.
MPT WEIGHT /
/^ B (
>cJ ' e ,'g
'0 t i
SllflTflTAI /^
TOTAL MOISTURE
i?g
Fig
Rg
I*
-"*
B-22
-------
ANALYTICAL DATA
DATE _
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER.
SAMPLE B!X NUMBER
CLEANUP MAN .
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
CONTAINER.
CONTAINER
LABORATORY RESULTS
. *8
FRONT HALF SUBTOTAL
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
EXTRACTION
CONTAINER
MOISTURE
IMPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
nil
ml
ml
i
.1
.1
TOTAL MOISTURE
< ~?
SUBTOTAL
B-23 .
-------
ANALYTICAL DATA
flr>^
PLANT J" 5}
DATE
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
SAMPLE BOX NUMBER
CLEAN UP MAN IL:
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS,
CONTAINER .
CONTAINER
FRONT HALF SUBTOTAL
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
IMPINGERS
FINAL VOLUME _i-Q^—ml
INITIAL VOLUME _2££L- ml
ml
_
'
ETHER-CHLORGFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
TOTAL WEIGHT
SILICA GEL
FINAL WFIGHT .A> <•
INITIAL WFIGHT i^
NET WFIGHT I \
UL« .
O f
J,U c
I
,"g
, |
SIIRTnTAI
TOTAL MOISTURE
V-<
~t~~L
\
\
\
\
A.A
-------
ANALYTICAL DATA
PLANT _ _.
OAFE_ . ?.."
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER at.
SAMPLE BOX NUMBER
CLEAN UP MAN ""
--7 *
W\
art 22)
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
W*<(
CONTAINER
LABORATORY RESULTS
"8
CONTAINER
-?«
FRONT HALF SUBTOTAL
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER
BACK HALF SUBTOTAL
TOTAL WEIGHT
\,
/
/
.•^
1 ,
\
N
>8
>8
ng
M
MOISTURE
IMPINGERS
FINAL VOLUME —&A-
INITIAL VOLUME _2£Q-
NET VOLUME "?
ml
ml
ml
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
.8
.8
TOTAL MOISTURE
B-25
-------
ANALYTICAL DATA
PLANT _ Rx XfiZD
OATE ..
SAMPLING LQCATIGN-CrusUr
SAMPLE TYPE
RUN NUMBER
SAMPLE BOX NUMBER
CLEAN UP MAN
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
IMPINGERS ft ^
FINAL VOLUME _1?J> ml
INITIAL VOLUME JlPlL ml
NET VOLUME - xIL ml
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
o. - -
•"*>'!
SUBTOTAL
LABORATORY RESULTS
CONTAINER.
CONTAINER
FRONT HALF SUBTOTAL
CONTAINER ____
ETHER-CHLOROFORM
\/
CQNTAWFP
BACK HALF SUBTOTAL
TOTAL WEIGHT
A .
/\ .
/ \!
TOTAL MOISTURE
3-26
-------
ANALYTICAL DATA
PLANT. f=:X£0
OATE_
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER.
SAMPLE BOX NUMBER
CLEAN UP MAN.
ft* ^
X*
& PA-
VK
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS
CONTAINER .
CONTAINER
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
IMPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
ml
ml
L> ml
SILICA GEL <,
FINAL WEIGHT > ' ^ •
INITIAL WEIGHT 3-°°
NET WEIGHT L-L!
FRONT HALF SUBTOTAL
\
ETHER-CHLOROFORM
EXTRACTION
CONTAINER
BACK HALF SUBTOTAL
TOTAL WEIGHT
\ /
X
/ "\
/ \
/ \
K
«tg
pg
i
TOTAL MOISTURE
SUBTOTAL
B-27
-------
ANALYTICAL DATA
PLANT
- tf A
SAMPLING LOCATION tScrtikJ3&r i'n !
-------
ANALYTICAL DATA
DATE _ 9-5.li 7
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
' 1
r>
f
SAMPLE BOX NUMBER ^
CLEAN UP MAN A/£ ; V K
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS
CONTAINER .
CONTAINER
FRONT HALF SUBTOTAL
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
ETHER-CHLOROFORM
EXTRACTION
CONTAINFR
BACK HALF SUBTOTAL
TOTAL WEIGHT
\/
A
/ \
/ \
' \
g
e
g
i
MOISTURE
IMPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
ml
P_2 — ml
fL. ml
SILICA GEL
FINAL WEIGHT *-Gtj
INITIAL WEIGHT 1 P°
NET WEIGHT —SI
C
."I
.1
SUBTOTAL
TOTAL MOISTURE
8-29
-------
ANALYTICAL DATA
PLANT ^*
DAFE_
SAMPLING LOCATION-,.
SAMPLE TYPE .
RUN NUMBER
SAMPLE BOX NUMBER.
CLEAN UP MAN "
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS
CONTAINER.
CONTAINER
,,ngl
FRONT HALF SUBTOTAL
BACK HALF
. IMPINGER CONTENTS ANO WATER WASH OF
IMPINGERS. CONNECTORS. ANO BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
ANO BACK HALF OF FILTER HOLDER
MOISTURE
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
TOTAL WEIGHT
IMPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
'2^0'd
i^
2/3
2~od
13
ml
ml
ml
r
t
i
g
."g
g
SUBTIini
TOTAL MOISTURE
B-30
-------
ANALYTICAL DATA
PLANT.
DATE_.
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
SAMPLE BOX NUMBER
CLEAN UP MAN .
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS
CONTAINER.
CONTAINER
FRONT HALF SUBTOTAL
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
CONTAINER ______
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
\
\A 1
mg
i Big
A_i
TOTAL WEIGHT
/
\«
MOISTURE
IMPINGERS
FINAL VOLUME .
INITIAL VOLUME
NET VOLUME .
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
ml
1
1
C
SUBTOTAL
TOTAL MOISTURE
B-31
-------
ANALYTICAL DATA
PLANT C
OATE_ .
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
SAMPLE BOX NUMBER.
CLEAN UP MAN '
L/fdW'
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS
CONTAINER.
CONTAINER
FRONT HALF SUBTOTAL
•It
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER ...,
BACK HALF SUBTOTAL __^
TOTAI WFIGHT /
V
A
' \
\
i
i\
E
g
!
I
MOISTURE
IMPINGERS
FINAL
INITIAL VOLUME
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
«'
ml
*. g
g
e
."«
.1
TOTAL MOISTURE
B-32
-------
ANALYTICAL DATA
PLANT ±.>'^
OATE_ . 1_
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
C/€
SAMPLE BOX NUMBER
CLEAN UP MAN
f \ r"l*s\
-He ?.'*&
'
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
CONTAINER
LABORATORY RESULTS
; fat
CONTAINER
FRONT HALF SUBTOTAL
be
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS.
AND BACK HALF OF FILTER HOLDER
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
TOTAL WEIGHT
/ \
"g
ne
*
MOISTURE
IMPINGERS ^
FINAL VOLUME _£:
INITIAL VOLUME _3_
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
SUBTOTAL
TOTAL MOISTURE
'B-33
-------
ANALYTICAL DATA
PLANT.
SAMPLING LOCATION &?&*€&.
?4$T/rULfiT£ G&A
SAMPLE TYPE
RUN NUMBIR
SAMPLE BOX NUMBER
CLEAN UP MAN
COMMENTS;
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
CONTAINER .
CONTAINER
LABORATORY RESULTS,
FRONT HALF SUBTOTAL
BACK HALF
. IMPINCER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
IMPINGERS a^
FINAL VOLUME _iZ.Z_ "I
INITIAL VOLUME _±r °Ji_ ml
NET VOLUME . " & ^
SILICA GEL
FINAL WEIGHT 2
INITIAL WEIGHT
NET WEIGHT
'3 E
g
8
I
.6
.2
SUBTOTAL
CONTAINER ;
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
TOTAL WEIGHT
.mg
-mr<
.mg
TOTAL MOISTURE
-------
ANALYTICAL DATA
PLANT eX? 0/V/
OATE_ . ~
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
SAMPLE BOX NUMBER
CLEAN UP MAN
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER 2-5J/ ¥
LABORATORY RESULTS
CONTAINER.
CONTAINER
FRONT HALF SUBTOTAL
.mg
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
IMPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
ml
ml
.1
.1
.1
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
.mg
.mg
."*
TOTAL
TOTAL MOISTURE
SUBTOTAL
B-35
-------
ANALYTICAL DATA
PLANT_
DATE
SAMPLING LOCATION .-£1**
SAMPLE TYPE
RUN NUMBER.
SAMPLE BOX NUMBER
CLEAN UP MAN
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
COMMENTS:
LABORATORY RESULTS,
CONTAINER
CONTAINER
FRONT HALF SUBTOTAL
BACK HALF
. IMPING ER CONTENTS AND WATER WASH OF
IMPINCERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
CONTAINER
ETHER-CHLORGFORM
EXTRACTION
CONTAINER.
y—7
\T
_mg
BACK HALF SUBTOTAL
.nig
TOTAL WEIGHT
/ v
MOISTURE
IMPINGERS
FINAL VOLUME .
INITIAL VOLUME.
NET VOLUME .
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
Jipo
ml
ml
ml
SUBTOTAL
TOTAL MOISTURE
B-36
-------
ANALYTICAL DATA
PLANT t^^NCcn ~
OAFE_ .*)fl
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER .
SAMPLE BOX NUMBER
CLEAN UP MAN '.
•
JO* O
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS). CONTAINER.
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER Q?J"V/J . CONTAINER
LABORATORY RESULTS
FRONT HALF SUBTOTAL.
-t!>8
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINCERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
IMPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
li
ml
U2_ t
.1
.1
.1
SUBTOTAL
\
ETHER-CHLOROFORM
EXTRACTION
BACK HALF SUBTOTAL
TOTAL WEIGHT
TOTAL MOISTURE
.mg
.mg
\
B-37
-------
ANALYTICAL DATA
r
PLANT S:
OATE_ .
SAMPLING LOCATION
SAMPLE TYPE
RUNNUMBtR
SAMPLE BOX NUMBER.
CLEAN UP MAN
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS
CONTAINER
CONTAINER
FRONT HALF SUBTOTAL
'4*
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINCERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
TOTAL WEIGHT
\
IMPINGERS
FINAL VOLUME .
INITIAL VOLUME .
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
' •>;?
C_ ml
_Jd:'ip_ mi
ml
y1 .- .' i **\
^ F)7\ j
, "7
• -..'- J _
I
t
t
IfllRTflTM
_mg
.«&
,mg
TOTAL MOISTURE.
B-38
-------
ANALYTICAL DATA
PL ANT _
SAMPLING LOCATION .
SAMPLE TYPE
RUN NUMBER
SAMPLE BOX NUMBER.
CLEAN UP MAN
COMMENTS:
/--; '" ->• V
I H'/i/£ fa'-v )
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS
CONTAINER
*
CONTAINER
tkt
FRONT HALF SUBTOTAL
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
ETHER-CHLOROFORM
EXTRACTION
^
BACK HALF SUBTOTAL
mi
TOTAL WEIGHT
/
,~
mi
MOISTURE
IMPINGERS
FINAL VOLUME .
INITIAL VOLUME.
NET VOLUME .
.Q(s
ml
^'Q—. ml
_" 5— ml
SILICA GEL ^ ,^
FINAL WEIGHT •<-'?
INITIAL WEIGHT ^'g.
NET WEIGHT 12
t
:i
.8
SUBTOTAL
TOTAL MOISTURE
B-39
-------
ANALYTICAL DATA
PLANT
DATE_ . _ JEL_
SAMPLING LOCATION
SAMPLE TYPE
RUNNUMBtR
U/eA
SAMPLE BOX NUMBER
CLEAN UP MAN
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS,
CONTAINER.
CONTAINER
.*!
FRONT HALF SUBTOTAL
.fc
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMP1NGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
IMPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
!L- ml
SUBTOTAL
ETHER-CHLOROFORM
EXTRACTION
\
CONTAINER.
V
BACK HALF SUBTOTAL
TOTAL WEIGHT
TOTAL MOISTURE.
_mg
.me
-«t
.m*
\
B-AO
-------
ANALYTICAL DATA
PLANT tlX£
OAFE_ . .(fiL(
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER.
/
SAMPLE BOX NUMBER
CLEAN UP MAN
Agf A
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
CONTAINER.
CONTAINER
LABORATORY RESULTS
. fc
FRONT HALF SUBTOTAL
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS, AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
CONTAINER _____
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
v
BACK HALF SUBTOTAL
TOTAL
D.
/ •
.mg
mg
\
mg
MOISTURE
IMPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
. ml
.ml
.ml
SUBTOTAL
TOTAL MOISTURE
1*7
-------
ANALYTICAL DATA
PLANT _j5
OATE_ . .
SAMPLING LOCATION _
SAMPLE TYPE
RUN NUMBER
SAMPLE BOX NUMBER.
CLEAN UP MAN
M
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS,
CONTAINER.
CONTAINER
FRONT HALF SUBTOTAL
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMP1NCERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
.me
CONTAINER.
BACK HALF SUBTOTAL
-mfc
TOTAL WEIGHT
\
IMPINGERS ^ r
FINAL VOLUME _J,/X_
INITIAL VOLUME ±i£_
NF_TVOHIMP ~" r~'
SILICA GEL 2^. „
FINAL WFICiHT „£**• •..*:.,
INITIAI WFIRHT "^^
NET WEIGHT 33-~...
.ml
.ml
ml
. t -
t
.~t
t
SIIRTflTAI
TOTAL MOISTURE
-------
ANALYTICAL DATA
PLANT.. ^"£&?r
OATE_ f-U^L
SAMPLING LOCATIOK
SAMPLE TYPE ?WTif:u.LAK
RUN NUMBER «2
SAMPLE BOX NUMBER
CLEAN UP MAN.
COMMENTS:
jZg-A'--* K_5
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS
CONTAINER.
CONTAINER
FRONT HALF SUBTOTAL
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINCERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
/
ETHER-CHLOROFORM
EXTRACTION
.mg
BACK HALF SUBTOTAL
TOTAL WEIGHT
X . me
/ \ mi
/ \
MOISTURE
IMPINGERS
FINAL VOLUME _yf4
INITIAL VOLUME _™
NET VOtllMF ""/.',
SILICA GEL ^fl J
FINAI WFIGHT 7.
IHITIAI WFIGHT --", ....
NET WEIGHT M tV
ml
ml
ml
j
r
s
TOTAL MOISTURE
8-43
-------
ANALYTICAL DATA
PLANT _____
DATE _ .
SAMPLING LOCATION-
SAMPLE TYPE
RUN NUMBER
0*J
SAMPLE BOX NUMBER
CLEAN UP MAN _
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS,
CONTAINER.
CONTAINER
FRONT HALF SUBTOTAL
BACK HALF
. IMPING ER CONTENTS AND WATER WASH OF
WRINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
TOTAL WEIGHT
/ liig
\ /
TV
MOISTURE
IMPINGERS _
FINAL VOLUME _±=L(rL_ ml
INITIAL VOLUME _^__ ml
/
SILICA GEL
FINAI WFIGHT ^~
INITIAI WFIfiHT £.*•
NFT WFIGHT *
T»5 e
V . *
w f
1
"g
t
SIIRTOTAI
TOTAL MOISTURE
-------
ANALYTICAL DATA
PLANT S±2. ,
OATE_ . ...„
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
SAMPLE BOX NUMBER.
CLEAN UP MAN
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS
CONTAINER.
CONTAINER
FRONT HALF SUBTOTAL
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINCERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
rflMTAIMFB
ETHER-CHLOROFORM \
EXTRACTIPM \ .., . --- T
CONTAINER , \ -^^^
BACK HALF SUBTOTALS^ _
TOTAL WFIGHT \ /
) mf
- : ^=» my
/ mp
/ - me
mi
MOISTURE
IMPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
™l
/ff ml
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT 2-°°
NET WEIGHT
I
.1
.1
SUBTOTAL
TOTAL MOISTURE.
17 Q
-------
J i!
PLANT.
OATE_
SAMPLING LOCATION
SAMPLE WE
RUN NUMBER 3
OPERATOR
wi,
PROBE LENGTH AND TYPE.
NOZZLE I.D
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE.
STATIC PRESSURE. (P,l_
FILTER NUMBER is)
ASSUMED MOISTURE. %.
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER 4M0
CFACTOR
PITOT TUBE FACTOR.
INFERENCE Ap
NOTE ;
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
'*•'• "'
VELOCITY
HEAD
Uptt. in. HjO
ORIFICE PRESSURE
DIFFERENTIAL
IAH). in. HjOl
DESIRED ACTUAL
STACK
TEMPERATURE
ITI.'F
DRY GAS METER
TEMPERATURE
INLET
,ITB|B)."F
OUTLET
PUMP
VACUUM.
in. H|
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
"F
-------
ANALYTICAL DATA
PLANT C^_X_
DATE-./4 ~JL~
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER.
\
SAMPLE BOX NUMBER
CLEAN UP MAN
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS
CONTAINER.
CONTAINER
FRONT HALF SUBTOTAL
BACK HALF
. IMPINCER CONTENTS AND WATER WASH OF
IMPINCERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
IMPINGERS
FINAL VOLUME ^2Z— "I
INITIAL VOLUME _2fifl— ml
.ml
CONTAINER __
ETHER-CHLORCFORM
EXTRACTION
\
CONTAINER.
BACK HALF SUBTOTAL
/x
-mg
TOTAL WEIGHT
SILICA GEL
FINAL WEIGHT .
INITIAL WEIGHT .
NET WEIGHT
ICO e
1.1 t
t
f
SUBTOTAL .
321
TOTAL MOISTURE
-------
ANALYTICAL DATA
PLANT_ E**0n-. EPA
DATE _ \0-_J_-
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
jpoxf
CJ
SAMPLE SOX NUMBER —
CLEAN UP MAN
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS,
CONTAINER
CONTAINER
FRONT HALF SUBTOTAL
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
CONTAINER _____
ETHER-CHLOROFORM
EXTRACTION
BACK HALF SUBTOTAL
TOTAL WEIGHT
_mg
I
.mg
MOISTURE
IMPINGERS __
FINAL VOLUME _JL;L
INITIAL VOLUME _2:<3£
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
ml
ml
CT?
SUBTOTAL
TOTAL MOISTURE
:*£—g
-------
ANALYTICAL DATA
PLANT_
DATE_ . Ifi-I -1.1
SAMPLING LOCATION- (irU-
SAMPLE TYPE
RUN NUMBER
SAMPLE BOX NUMBER
CLEAN UP MAN '
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
LABORATORY RESULTS
CONTAINER.
CONTAINER
FRONT HALF SUBTOTAL
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINCERS. CONNECTORS. AND BACK
* HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
MOISTURE
IMPINGERS
FINAL VOLUME _2.-^L~ "I
INITIAL VOLUME _j£42__ m«
•-on mi
CONTAINER —
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
TOTAL
SILICA GEL •
FINAL WFHiHT ^~
INITIAL WFIGHT eM
WCT wFtfiHT
0? t
5D e -g
*/ f g
SIIRTOT4I
TOTAL MOISTURE
-------
ALBUQUERQUE LABORATORY
CUSTOMER
ATTENTION
ADDRESS
CITY
S.O. NO.
TYPE OF ANALYSIS
Sample
Identification
Run 1 - Dryer
Scrubber Inlet
Run 1 - Dryer
WESTON, ENVIRONMENTAL CONSULTANTS-DESIGNERS
Barry L. Jackson
1 Weston Way
Westchester, Pennsylvania 19380
4374
nLv ISsMl
iStSI
isisi
ImimHr f Ei&^^^^V^^^^^I
REPORT OF RNRLYSIS
DETERMINATION of NATURAL URANIUM, 246S8 32
ISOTOPIC URANIUM, ISO.TOPIC CUSTOMER ORDER NUMBER SAMPLES RECEIVED 11/27/79
THORIUM, RADIUI'1-226, LEAD-210 and POLONIUM-210
Sample Date Total Type of
Number Collected Weight (g) Analysis
1 ' 10/01/79 7.9157 Uranium
U-234
U-235
U-238
Th-223
Th-230
3 Th-232
Ra-226
Pb-210
Po-210
2 10/01/79 0.4010 Uranium
Scrubber Outlet U-234
Blank
U-235
U-238
- ' ' Th-228
Th-230
Th-232
Ra-226
Pb-210
Po-210
3 — -.- Uranium
U-234
U-235
U-238
Th-228
Th-230
Th-232
Ra-226
Pb-210
Po-210
in AIR FILTER . SAMPLES
ug/g t)Ci/g
650,000
200,000 ± 40,000
< 13, 000
190,000 ± 40,000
36 ± 13
13,000 ± 1000
36 ± 13
20 ± 6
320 ± 80
170 ± 40
310,000
92,000 ± 4000
6000 ± 400
94,000 ± 4000
• 170 ± 80
1400 ± 100
120 ± 60
6.8 ± 2.0
250 ± 30
140 ± 30
63
96 ± 4
3.0 ±0.6
100 ± 10
<0.20
<0.20
<0.20
0.08 ± 0.05
4.5 ± 2.1
<5.4
Q REPORTED VIA TELEPHONE
D REPORTED VIA TWX
•
&r\c
t&VJtc
• •
fcflinft WJjcfa
/I Ul Y*J APPROVED BY ,„„„„„,.
PAGE 1 OF 1 PAGE
„.
Jtt.d',i£' 2(P1/80»
••^) "* °""*°CI=:rDATE
P.O. BOX 3874 ALBUQUERQUE. NEW MEXICO 87110
PHONE I505I 345-3461 TWX: 910-985-0678
MICHAEL A. ORTIZ', Laboratory Manager
B-50
-------
Appendix C
Sample Calculations
-------
SAMPLE CALCULATIONS
Test Run 1 CRUSHER TRANSFER POINT EXHAUST DUCT
1. Volume of dry gas sampled at standard conditions (68°F, 29-92
in. Hg), dscf.
17.647 x Y x V x ( P.
v m v b
m(std) »
Vm(std)
Where:
(Tm * *
17.647 x 0.995 x 52.20 x ^24.77 > -fj^-}
(95 + 460 )
V / .» » Volume of gas sample measured by the dry gas meter,
corrected to standard conditions, dscf.
Vm * Volume of gas sample measured by the dry gas meter at
meter conditions, dcf.
Pfe » Barometric pressure, in. Hg.
&H » Average pressure drop across the orifice meter,
in. H20.
T » Average dry gas meter temperature, °F.
17-647 » Factor that includes ratio of standard temperature
(528°R) to standard pressure (29-92 in. Hg)7°R/in. Hg.
Y » Dry gas meter calibration factor.
2. Volume of water vapor in the gas sample corrected to standard conditions, scf.
Vw(std) * (0-0^07 x Vwc) * (0.04715 x W
- (0.04707 x 0.0 1 + CO.04715 x 9.5 1 - 0.448
Where:
^w(std) 3 Volume of water vapor in the gas sample corrected to
standard conditions, scf.
V - Volume of liquid condensed in impingers, ml.
we
C-1
-------
- 2 -
W
wsg
0.04707
» Weight of water vapor collected in silica gel, g.
• Factor which includes the density of water
(0.002201 lb/ml), the molecular weight of water
(18.0 Ib/lb-mole), the ideal gas constant
[21.85 Un. ffgj (ft3]/Ob-mole) (°R)] ; absolute
temperature at standard conditions (528°R), absolute
pressure at standard conditions (29.92 in. Hg), ffVml.
0.04715
Factor which includes the molecular weight of water
(18.0 Ib/lb-mole), the ideal gas constant
[21.85 (in. Hg)(ft3)/(1b-mole)(°R)l7 absolute
temperature at standard conditions (528OR), absolute
pressure at standard conditions (29*92 in. Hg), and
453.6 g/lb, ft3/g.
3. Moisture content.
ws
w(std)
w(std)
m(std)
B
ws
Where:
ws
O.MtS
+ M.02
0.011
Proportion of water vapor, by volume, in the gas
stream, dimension less.
. Mole fraction of dry gas.
M
- B
ws
Md
Where:
d
» i - 0.011 « 0.989
Mole fraction of dry gas, dimensionless
5. Dry molecular weight of gas stream, Ib/lb-mole.
MW,
0.440(*C02) + 0.320 (*02) + Q.28Q
% CO)
C-2
-------
- 3 -
MWd - (0.440 x 0.0 )+ (0.320 x 20.9) + [0.280 ( o.O * 79.1 )]
" 28.97 (ambient air)
Where:
MW, » Dry molecular weight, Ib/lb-mole.
• Percent carbon dixoide by volume, dry basis.
$0. « Percent oxygen by volume, dry basis.
%N_ - Percent nitrogen by volume, dry basis.
$CO • Percent .carbon monoxide by volume, dry basis.
0.440 » Molecular weight of carbon dioxide, divided by 100.
0.320 * Molecular weight of oxygen, divided by 100.
0.280 ~ Molecular weight of nitrogen or carbon monoxide,
divided by 100.
6. Actual molecular weight of gas stream (wet basis), Ib/lb-mole.
MW - (MW x' M) + [18 (1 -
MW - (28.97 x 0.989) + D8 0 ' 0.989)]
» 28.85
Where:
MW « Molecular weight of wet gas, Ib/lb-mole.
18 - Molecular weight of water, Ib/lb-mole.
7. Average velocity of gas stream at actual conditions, ft/sec. ,
T / \ 1*
s Cavg)
' 85'"9 * Cp x <^' avg. x
P
C-3
-------
- 4 -
.1*9 x 0.855 x 0.037 x [24 jf V 2$5
85
27.64
Where:
* Average gas stream velocity, ft/sec.
85.49 * Pftot tube constant, ft/sec X
rOb/lb-mole)(in.Hg)'U
L (°R) (in. H20) J -
C a Pi tot tube coefficient, dimensionless.
P
Ap * Velocity head of stack gas, in H2<3.
T » Absolute gas stream temperature, R.
P » Absolute gas stack pressure, in. Hg.
8. Average gas stream dry volumetric flew rates, dscf/min.
1058.8 x V x A x M-j x Pg
Ts
o . 1058.8 x 27.64x 0.785 x 0.989 x 24.76
S(std) - T5^ * 460)
1,050. (ACFM = 1,300 = 27.64 x 0.785 x 60)
Where:
^s(std) * Volumetric flow rate of dry stack gas, corrected to
standard conditions, dscf/min.
2
A • Cross-sectional area of stack, ft .
1058.8 * Factor which includes standard temperature (528°R),
standard pressure (29.92 in. Hg), and 60 sec/min,
(°R) (sec)
(in. HgJ(min) "
9. Isokinetic variation calculated from intermediate values, percent.
C-4
-------
- 5 -
17-316 x T x V
m(std)
v x 8 x Pa x M. x (D )2
s son
I - 17.316 x 75.5 x 41.02
27.64 x 96 x 24.76x 0.989 * (0.242 7*
- 99.9
Where:
I » Percent of isokinetic sampling.
8 » Total sampling time, minutes.
On * Diameter of nozzle, inches.
17.316 * Factor which includes standard temperature (528°R) ,
standard pressure (29.92 in. Hg) , the formula for
calculating area of circle TTD* . ,
i , conversion of
square feet to square inches ( 144), conversion of
seconds to minutes (60) , and conversion to
percent (100). (in. Hq) (in2) (min) .
(°R) (ft2) (sec)
10. Part icul ate concentration, gr/dscf.
C » 0.015432 x M
Vm(std)
C, » 0.015432 x -r£!2 "0.0024
Where:
C, * Particulate concentration, gr/dscf.
Mt • Total weight of particulate caught by train, mg.
0.015432 * Conversion factor of gr/mg.
11. Particulate mass emission rate, Ib/hr.
- 0.0085714 x C1 x Q$(stdj
- 0.0085714 x 0.0024 x 1050. » 0.021
05
-------
- 6 -
Where:
PMR » Particulate mass emission rate, Ib/hr.
0.0085714 * Conversion factor relating minutes to hours (60), and
grains to pounds (7.000),(Ib) (min)/(gr) (hr).
C-6
-------
Appendix D
Equipment Calibration Data
-------
Date
VllY It
Barometric pressure,
30
- _ in. Hg
0L- Box No..
Dry gas meter No.
Orifice •
manometer
setting,
AH,
in. H20
0.5
1.0
2.0
4.0
r aSv$
8.0
Gas volume
wet test
meter
5
5
10
lO.tv/
JO ^-3f
10
Gas volume
dry gas
meter
V
T3 LSI
ffi'^cL
tf 'A1*.. .
f r Wfr
/£' AS
& '*&
Temperature
Wet test
Meter
°F
H'
.iT-fc
,«\n«!»
.^i;
.«£•
An(3
I, "7 8
/ ^7
/.??
/.''V
1 1 n P
i 0*7
Calculations
AH
0.5
1.0
2.0
4.0
6.0
8.0
AH
13.6
0.0368
0.0737
0.147
0.294
0.431
0.588
Y
Vw PD (^ + 460)
M b TITej V w /
•••
AH@
0.0317 AH Rtw + 460) el2
1 » 1 ~~~ ~~ ~~ ~~^~~ 1
Pb (td + 460) L Vw J
= Ratio of accuracy of wet test meter to dry test meter. Tolerance = * 0.01
= Orifice pressure differential that gives 0.75 cfm of air at 70° F and 29.92
inches, of mercury, in. HgO. Tolerance - ± 0.15
D-l
-------
i?7fi
7 .,^2*
Barometric pressure, Pj, = J in. Hg
Box No.,
Dry gas meter Ho.
Orifice •
manometer
setting,
AH,
in. H20
0.5
1.0
2.0
4.0
6.0
8.0
Gas volume
wet test
meter
YW»
ft3
5
5
10
10
10
10
Gas volume
dry gas
meter
vd.
ft3
ic.ccc-
jy.tj«f
jr.ti*
'« if, i
•*'• i'i ij
vc r7Y
1C 2-7 -L
£e • t/P
Temperature
Wet test
Meter
*Wf
°F
L^
\,r
ItS*
L-r
Dry gas meter
Inlet
t
-------
Box Nn.
Orifice
manometer
setting,
AH,
in. H20
0.5
1.0
C3/.5-
C^a.0
6.0
8.0
Gas volume
wet test
meter
Vw.
5
5
©5
10
10
10
Gas volume
dry gas
meter
ft3
ffifll
7o?.'u/ /
7£*.73*
lea. 732.
Temperature
Wet test
Meter
°F
s-S
s<>'
f7°
S%°
Dry gas meter
JB*^-»
°F
s-i
SB° d
(sfy
ni° 71
jg^j-^-gt
°F
^3-°^'
3° 4£*
5° 75'
)" 93v
Average
td.
°F
^T°
/>£°
69*
77*
Time
e,
min
I&JJ
l.ft
1.?8
73.37
Average
Y
',*>!?
tMOl
r^5f
[??/(•
Wt*
I 7930
7.776.3
7,8/93
/. s^r^
Lltltl
Calculations
AH
0.5
1.0
2.0
4.0
6.0
8.0
All
AH
13.6
0.0368
0.0737
0.147
0.294
0.431
0.588
Y
Vw PD (td * 460)
w .1 n. i AM If*. . >i^-ft 1
HPb 13.6J ltw + 460/
AH@
0.0317 AH [~(tw + 460) el2
1 1
Pb (td + 460) L vw J
Y = Ratio of accuracy of wet test meter to dry test meter. Tolerance a * 0.01
AH(j = Orifice pressure differential that gives 0.75 cfm of air at 70° F and 29.92
inches of mercury, in. H20. Tolerance - ± 0.15
D-3
-------
K I
Date
Baron
Orifice-
manometer
setting,
AH,
in. H20
0.5
1.0
2.0
4.0
6.0
8.0
eX£ /M . :yf U / 1 ' /
1
netric pres
Gas volume
wet test
meter
5
5
10
10
10
10
Calculations
AH
0.5
1.0
2.0
4.0
6.0
8.0
AH
13.6
0.0368
0.0737
0.147
0.294
0.431
0.588
sure, Pjj « _ .-in. Hg
Gas volume
dry gas
meter
ft3
l/?q?
? c t'«j e\
%i.Wv
c/cy/y
yjt/cX BOX
Dry gas meter
Temperature
Wet test
Meter
°F
&V0
fctf
6iV°
(J1/
Dry gas meter
Inlet
°F
£Jl
L-fiJ
73
%7
Outlet Average
°F °F
IcV &
kff0 67"
67* TO"
01 1^
nn /.JLJ.LP
no.
Time
e.
min
/2.5TD
9.17
/3 , 6i"
*?.&""
Average
Y
r
Vw PD (to* + 460)
vd(pb * T3T6-) (*» + 46°)
Y
ff£3
•,Wl
yw
SIM
AH0
1.7/kl
/.P37/
SL.CZlfl
Z.C699
A9/67
AH@
0.0317 AH Rtw + 460) el?
Pb (td * 460) L Vw J
t
-- -•• • ---.,--,- _.....
Y " Ratio of accuracy of wet test meter to dry test me'ter. Tolerance ° * 0.01
Orifice pressure differential that gives 0.75 cfm of air at 70° F and 29.92
inches of mercury, in. H20. Tolerance - * 0.15
D-4
-------
- /f7f
BOX Mn. 3 3 5" 3
Barometric pressure, PS • '.in. Hg
Dry gas meter Ho.
Orifice-
juanometer
setting,
AH.
in. H20
0.5
1.0
6.0
8.0
Gas volume
wet test
meter
10
10
10
alculations
Gas volume
dry gas
meter
VHi.
Temperature
Wet test
Meter
(A*
Dry gas meter
Inlet
Outlet
70
7i
Average
ir
Time
e.
min
Average
AHp
1,1
AH
jj.5
1.0
2.0
"4.0
5.0
JB.O
AH
13.6
0.0368
0.0737
0.147
0.294
0.431
0.588
Y
Vw Pfa (*d * 460)
V (p ^ aH \ A + 46Q\
\ 13.6/ \ , /
•
__.___. ...
AH0
0.0317 AH Rtw + 460) ft!2
Pb (td + 460) L Vw J
T * Ratio of accuracy of wet test meter to dry test meter. Tolerance » * 0.01
Orifice pressure differential that gives 0.75 cfm of air at 70° F and 29.92
inches of mercury, in. H£0. Tolerance - ± 0.15
0-5
-------
:zr -v£
fl
330..
1Z£~,
-VJL ~. 24/
//
D-6
-------
PITOT TUBE IDENTIFICATION NUMBER:
CALIBRATED BY:_
DATE:
RUN NO.
1
2
3
"A" SIDE CALIBRATION
APstd
cm HzO
(in. H20)
AS*
o.t>r
0,3*-
AP(s)
cm H20
(in. H£0)
f*?<
o.W
«>,4i
AVERAGE
Cp(S)
.H7
.prs
.^3
• 15^
DEV.
RUM NO.
1
2
3
"B" SIDE CALIBRATION"
APsttl
cm H20
(in. H20)
/•**
o,;c
0,3T_
Al'(s)
cm H20
(in. H20)
/.r^
o.ff
0.43
AVERAGE
Cp(S)
-^
.//r
.&fe3>
DEV.
DEV. = C|,(S) - Cp(S)(avq.) (MUST BE < 0.01)
Cp DIFFERENCE: Aavg - Bavg = (MUST BE < 0.01)
Pitot tube calibration data.
-------
PITOTTUBE IDENTIFICATION NUMBER:
CALIBRATED BY:
DATE:
RUN NO.
1
2
3
"A" SIDE CALIBRATION
APstd
cm H£0
(in. H20)
f.*3
6.$,^
O.^T-
AP(s)
cm H20
(in. H£0)
/.-H
_n
Q>^
AVERAGE
Cp(S)
.Ptl
.ttrt
.fr2>
DEV.
RUN NO.
1
2
3
"B" SIDE CALIBRATION"
APsttl
cm H20
(in. H20)
I.*}
O.L\"
0, ^v
AP(s)
cm H20
(in. H2fl)
/.Tl
.Ff
O-Wf
AVERAGE
CP(S)
.H3
.^r*?
.^"3
DEV.
DEV. = CD($) - Cp(S)(avq.) (MUST BE < 0.01)
Cp DIFFERENCE: Aavg • Bavg = (MUST BE < 0.01)
Pilot tube calibration data.
D-8
-------
PITOT TUBE IDENTIFICATION NUMBER: T.
CALIBRATED BY:
DATE:
RUN NO.
1
2
3
"A" SIDE CALIBRATION
Apstd
cm H20
(in. H20)
I.***
04 f
0,3*.
AP(s)
cm H?0
(in. H20)
/.•?r
O.9o
0.
-------
PITOT TUBE IDENTIFICATION NUMBER: .3
CALIBRATED BY:
DATE:
RUM NO.
1
2
3
"A" SIDE CALIBRATION
APstd
cm H20
(in. H20)
/•^
0-c.r
0.3*-
AP(s)
cm M20
(in. H20)
I'll
o.n
o.*/H
AVERAGE
Cp(S)
J5t
-«fc,^
.^^
DEV.
-ol?
.0«1
DEV. = C|,(S)-CD(S)(iivn.) (MUST BE < 0.01)
Cp DIFFERENCE: Aavg - Bavg =
RUM NO.
1
2
3
"B" SIDE CALIBRATION"
Apstcl
cm H2fl
(in. H20)
A-2-3
o.tr
^.5"*-
Al'(s)
cm H20
(in. H20)
/.78
O-S-1
o.v3
AVERAGE
Cp(S)
.a-%/
.ftM
,n?
DEV.
(MUST BE < 0.01)
Pilot tube calibration data.
-------
Calibration Check: Nomograph
laboratory \Kj€-S>Vlo v-\ \
Dale *7~ V % - *7 "?
(\) C.Factor Adjustment
I'robc I
lfCp>0.87orCp<0.83
JUJ (0.85)2
,c(- >1
(0.85)2
= C( ).
(2) Accuracy (±.\Q °(«,
(a) K-factor line. A// and Ap scales
Aline Set
Ap = 0.001; A//= 0.1
Ap= 10.0: A//= 10.0
Ap = 0.1;A//= 1.0
Ap= 1.0
Ap= 1.0
I- J'
i-3'
»-4|
T-S1
t-r1
fc
17
'•'t-
Au
51
So
sc
to
Cx
It
^v^BF -.
i, c.^'
Probe 2
Probe 3
= C
(0.85)2
= c( I
(0.85)2
C2
"• (0.85)2
(0.85)2
A// Reading
\
\.OT_
\o.o
Nomograph 1_
0-\oi.
Nomograph if
\. OQ
0.99
""0.01 Q.\Q\
O.\ob
(b) C, /s and £>„ scales
5"
a.t
o. \\T_
O .\Ot
ft^VAjC^
so .-^ n
s .^
o.^l
4-.H
0 . t?O
c. C
2.0
1.5
1.0
0.7
0.5
On
0.5
0.4
0.3
0.25
0.2
/,(°F)
2500
1500
1000
500
200
Ap
0.02
0.8
0.1
3.0
0.9
I
o.^T
8.1
o. 31
*
^."0
0.6"^
Nomograph 1_
0.^9
S.t
o .3"2-
•^•1
C3-tS
^7 Readings . ._.. —
-z, Nomograph -8^-
Q.SV C»^8
e.b 9.0
o.^i o.>l
^ °
o'. tt ^' tT.
•g
O'.^<
«•.?
G .3'
J*\ l_
D-11
-------
CONTINUING
EDUCATION
o
ro
U certifies that
CHARLES DOBROSKI
ad completed
VISIBLE EMISSIONS EVALUATION SEMINAR
Recertified
-. I
-i . J4P»^v
Date:
Recertified:
Certified
Date:
PROJECT DIRECTOR OF VISIBLE EMISSIONS
TRAINING PROGRAM
CENTER FOR AIR ENVIRONMENT STUDIES
I
Date:
VICE PRESIDENT FOR
CONTINUING EDUCATION
-------
MBA ST4#
CONTINUING
Recertified: » \ Data:
EDUCATION
TED MOXON
haA completed
VISIBLE EMISSIONS EVALUATION SEMINAR
:&uH.
Certified
Recertified:
Data:
PROJECT DIRECTOR OF VISIBLE EMISSIONS
TRAINING PROGRAM
CENTER FOR AIR ENVIRONMENT STUDIES
I
Date:
VICE PRESIDENT FOR
CONTINUING EDUCATION
-------
CONTINUING
EDI/CATION
/4 certified that
JEFFREY D, O'NEILL
kaA completed
VISIBLE EMISSIONS EVALUATION SEMINAR
Date:
Recertified:
Certified
Date:
PROJECT DIRECTOR OF VISIBLE EMISSIONS
TRAINING PROGRAM
CENTER FOR AIR ENVIRONMENT STUDIES
/
Date:
VICE PRESIDENT FOR
CONTINUING EDUCATION
-------
CONTINUING
o
_n
Date:
DIRECTOR. CENTER FOR AIR
ENVIRONMENT STUDIES
EDUCATION
/d certifies tkat
BARRY L, JACKSON
leted
VISIBLE EMISSIONS EVALUATION SEMINAR
comp
Recertified:
Date:
VICE PRESIDENT FOR
CONTINUING EDUCATION
-------
Balances
Mettler Analytical Balances
Performance Data, Contd.
H51AN
H54AR
m»
H7BAR
HJ11
H31i
o
ItJ
31^
0 *
. H543 -
MS*
Specially designed, low-cost
Student Models H72 and H78AR
now available _...
Two economical balances with
digital readout and weight knobs at.-
eye level above weighing com- - -
partment. Big readout numerals
and clearly labeled controls make
it easy for the novice. Weight knob
direction arrows and rapid filling
guide keep students on target and-
shorten weighing time signffi- - -
cantly. Designed to hold their own
through the academic storm: a
weight knob interlock avoids ab-
rupt weight application. Slip
clutches prevent forcing of weight
knobs. And, in the H78AR, an air
release system safeguards knife.:
edges. : - -
Model H78AR buyers receive a
condensed instruction label that
can be attached to balance. Pads
of weighing instructions and over-
head transparencies on operating
procedures are included in pack-
ing carton.
See specifications in table.
Serviced by
fifefiffliar
INSTRUMENT CORPORATION
609-448-3000
DATE
SERVICED
SERIAL NO.
w^nwiwEts -
7-1-W38BI06
Jof
H7SAR
Economical student
model. Same as H72
eicepl with air releaM
-^t^?;4x-- (
0-160
160 -
*
- ±0.05. _
--,-- • 0.1 ,.
0-1000 _
10
0.1 -:
100 —
.159
±0.25 r
1
159
~^~ 159
8.9x18 -
- - 46x24" ~_^.. _ . .
41 --
17x20
20 t
18/40
11
1 -909-78 AR ;
1195.00
1-909-78 AR
D-16
-------
Appendix E
Project Participants
-------
APPENDIX E
PROJECT PARTICIPANTS
The following Weston employees participated in this project:
Peter J. Marks
Vice President, Laboratory Services
Barry L. Jackson
Supervisor, Air Testing
Gregory A. Celiano
Assistant Project Scientist
Charles Dobroski
Assistant Project Scientist
Theodore Moxon
Senior Laboratory Technician
Andrew Watkins
Assistant Project Scientist
Nancy Goldberg
Chemist
Wayne Kimbal1
Civil Engineer
David Ralston
Laboratory Technician
Robert Newton
Laboratory Technician
Virginia McGlincy
Laboratory Technician
Jeffery D. O'Neill
Project Scientist
Robert Caprara
Laboratory Technician
Thomas Davis
Laboratory Technician
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
Environmental Engineers Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
E-1
-------
Scott Stanley
Laboratory Technician
Thomas Feeley
Laboratory Technician
Robert Karpovich
Laboratory Technician
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
E-2
------- |