United States
Environmental Protection
Agency
Office of Air Quality
Planning and Standards
Research Triangle Park NC 27711
EMB Report 79-MET-3
January 1980
Air
&EPA Metallic Minerals
Emission Test Report
Anaconda
Butte, Montana
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ANACONDA COPPER COMPANY
BUTTE, MONTANA
PROCESS ORE SAMPLES - ANALYTICAL RESULTS
Sample Description
1
Percent Moisture
Percent Sol ids
Run I 10/25/79
5:01 PM (EP)
Run II 10/26/79
5:45 PM (EP)
Run 1 10/26/79
3:09 PM (WB)
Run II 10/25/79
10:41 PM (WB)
Run III 10/26/79
9:00 PM (WB)
Run III 10/26/79
1:41 AM (EB)
0.44
0.36
2.19
0.14
0.54
3.69
99.56
99.64
97.81
99.86
99.46
96.31
Description of samples were taken directly from sample bottles
additional information is available.
- no
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SOURCE EMISSIONS TEST REPORT
Anaconda Copper Company
Butte Operations
Butte, Montana
s.
JeTfrey' D.TJ'Neill
Project Scientist
CLAXM 4
Barry L^Ja
Supervisor
Air Testing
RFW Report No. 0300-81-12
Contract No. 68-02-2816
Work Assignment No. 11
Prepared by
Weston Designers-Consultants
West Chester, Pennsylvania 19380
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TABLE OF CONTENTS
LIST OF TABLES i i
LIST OF FIGURES iv
SUMMARY 1
INTRODUCTION 5
PROCESS DESCRIPTION 9
General g
Process Operation 11
DESCRIPTION OF TEST LOCATIONS 15
Crusher Grizzley East Duct 15
Crusher Hood Duct 15
Crusher Baghouse No. 1-2 Inlet Duct 15
Crusher Baghouse No. 1-2 Outlet Stack 15
Truck Dump Baghouse No. 3~4 Inlet Duct 15
Truck Dump Baghouse No. 3.-4 Outlet Stack - 15
DESCRIPTION OF SAMPLING TRAINS 23
Particulate Sampling Trains 23
Particle Size Distribution Sampling Apparatus 23
TEST PROCEDURES . 27
Preliminary Tests 27
Crusher Grizzley East Duct 27
Crusher Hood Duct 28
Crusher Baghouse No. 1-2 Inlet Duct 28
Crusher Baghouse No. 1-2 Outlet Stack 28
Truck Dump Baghouse No. 3-4 Inlet Duct 29
Truck Dump Baghouse No. 3-4 Outlet Stack 29
ANALYTICAL PROCEDURES 31
Particulate Sample Recovery 31
Particulate Analyses 31
Particle Size Sample Recovery and Analyses 32
DISCUSSION OF TEST RESULTS 33
APPENDIX A — Raw Test Data
APPENDIX B -- Laboratory Reports
APPENDIX C -- Sample Calculations
APPENDIX D — Equipment Calibration Records
APPENDIX E — Project Participants
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LIST OF TABLES
Table No. Title Page
1 Crusher Grizzley East Duct
Summary of Test Data 35
2 Crusher Hood Duct '
Summary of Test Data ' 36
3 Crusher Baghouse No. 1-2 Inlet Duct
Summary of Test Data 37
k Crusher Baghouse No. 1-2 Outlet Stack
Summary of Test Data 38
5 Truck Dump Baghouse No. 3~^ Inlet Duct
Summary of Test Data 39
6 Truck Dump Baghouse No. 3~A Outlet Stack
Summary of Test Data 40
7 Grizzley East Duct
Summary of Test Results 41
8 Crusher Hood Duct
Summary of Test Results 42
9 Crusher Baghouse No. 1-2 Inlet Duct
Summary of Test Results 43
10 Crusher Baghouse No. 1-2 Outlet Stack
Summary of Test Results kk
11 Truck Dump Baghouse No. 3-*» Inlet Duct
Summary of Test Results 45
12 Truck Dump Baghouse No. 3-/* Outlet Stack
Summary of Test Results ' *" U6
13, 1^, 15 Crusher Grizzley East Duct
Particle Size Distribution Runs 1, 2, 3 47, 49, 51
16, 17, 10 Crusher Hood Duct
Particle Size Distribution Runs 1, 2, 3 . 53, 55, 57
19, 20, 21 Crusher Baghouse No. 1-2 Inlet Duct
Particle Size Distribution Runs 1, 2, 3 59, 61, 63
i i
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LIST OF TABLES
(cont inued)
Table No. Title
22 Crusher Baghouse No. 1-2 Outlet Stack
Particle Size Distribution Run 1 65
23, 24, 25 Truck Dump Baghouse No. 3-4 Inlet Duct
Particle Size Distribution Runs 1, 2, 3 67, 69, 71
26 Truck Dump Baghouse No. 3-4 Outlet Stack
Particle Size Distribution Run 1 73
27 Crusher Grizzley East
Summary of Visible Emissions 75
28 Crusner Grizzley West
Summary of Visible Emissions 77
29 Crusher Hood Area
Summary of Visible Emissions 78
• 30 . Crusher Baghouse No. 1-2 Outlet.Stack .
Summary of Visible Emissions " 80
31 Truck Dumping Area
Summary of Visible Emissions 81
32 Truck Dump Baghouse No. 3-4 Outlet Stack
Summary of Visible Emissions 82
33 Coarse Ore Stockpile
Summary of Visible Emissions 83
34 Coarse Ore Transfer Point
Summary of Visible Emissions 84
35 EPA Method 22
Summary of Fugitive Emissions Results 85
i i i
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LIST OF FIGURES
Figure No. Title Page
1 Flow Sheet of New Primary Crushing Plant 10
2 Crusher Grizzley East Duct
Port and Sampling Point Locations 16
3 Crusher Hood Duct
Port and Sampling Point Locations 17
k Crusher Baghouse No. 1-2 Inlet Duct
Port and Sampling Point Locations 18
5 Crusher Baghouse No. 1-2 Outlet Stack
Port and Sampling Point Locations 19
6 Truck Dump Baghouse No. 3-A Inlet Duct
Port and Sampling Point Locations 20
7 Truck Dump Baghouse No. "$-k Outlet Stack
Port and Sampling Point Locations 21
° Particulate Sampling Train
EPA Method 5 25
9 Particulate Sampling Train
EPA Method 5 26
IV
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SUMMARY
The Emission Measurement Branch of the U.S. Environmental Protection
Agency contracted Roy F. V/eston, Inc. to conduct a source testing and
analysis program at Anaconda Copper Company's Butte, Montana copper
processing facility.
The program was designed to determine various emission parameters asso-
ciated with selected Primary Crusher and Truck Dumping Area test sites
as indicated below:
Number of Test Repetitions
Particle Visible Fugitive
Particulate Size Emission Emission
Source Description
Grizzley East Duct 33-
Crusher Hood Duct 33-
Crusher Baghouse No. 1-2 Inlet Duct 33-
Crusher Baghouse No. 1-2 Outlet Stack 3 1 1
Truck Dump Baghouse No. 3-4 Inlet Duct 33-
Truck Dump Baghouse No. 3-4 Outlet Stack 3 1 2
Crusher Grizzley East - - 3
Crusher Rrizzley West - - 3
Crusher Hood Area - - 3
Truck Dumping Area - - 3
Coarse Ore Stockpile - - 3
Coarse Ore Transfer Point - - 3
Fine Ore Feeder -
The following test protocol was used during the survey:
Parameter
Particulate
Particle Size
Visible Emission
Fugitive Emission
Test Method
EPA 51
Andersen 2000,
EPA 93
EPA 22**
Inc.'
3
3
3
3
3
3
2
3
Code of Federal Regulations, Title 40, Part 60, Appendix A, "Standards
of Performance for New Stationary Sources," August 18, 1977.
'Operating Manual for Andersen 2000, Inc., "Mark III Particle Sizing
Stack Samplers," Andersen 2000, Inc., P.O. Box 20769, Atlanta, Georgia.
Federal Register, Vol. 39, No. 219, November 12, 1974.
Waft method, revised July 28, 1978.
-1-
-------
The particulate matter concentration and mass rate results are summarized
be 1 ow:
Test
Number
Date
1 10-25-79
2 10-25-79
3 10-26-79
Series Average
GRIZZLEY EAST DUCT
Particulate Concentration
Grains/DSCF
0.129
0.058
0.068
Particulate Mass Rate
Pounds/Hour
19.2
9.67
11.5
13.5
Test
Number
Date
1 10-25-79
2 10-25-79
3 10-26-79
Series Average
CRUSHER HOOD DUCT
Particulate Concentration
Grains/DSCF
1.55
1.48
1.00
Particulate Mass Rate
Pounds/Hour
251.
244.
166.
220.
Test
Number
Date
1 10-25-79
2 10-25-79
3 10-26-79
Series Average
CRUSHER BAGHOUSE NO. 1-2 INLET DUCT
Particulate Concentration
Grains/DSCF
2.805
2.624
1.694
Particulate Mass Rate
Pounds/Hour
1,549.
1,558.
1,010.
1,372.
CRUSHER BAGHOUSE NO. 1-2 OUTLET STACK
Test
Number
1
2
3
Series
Date
10-25-79
10-25-79
10-26-79
Average
Particulate Concentration
Grains/DSCF
0.005
0.005
0.007
Particulate Mass Rate
Pounds/Hour
3.58
2.93
5.01
3.84
-2-
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TRUCK DUMP BAGHOUSE NO. 3-4 INLET DUCT
Test Particulate Concentration Particulate Mass Rate
Number Date Grains/DSCF Pounds/Hour
1 10-26-79 0.168 92.1
2 10-26-79 0.134 75.5
3 10-26-79 0.097 55.4
Series Average 74.3
TRUCK DUMP BAGHOUSE NO. 3-4 OUTLET STACK
Test Particulate Concentration Particulate Mass Rate
Number Date Grains/DSCF Pounds/Hour
1 10-26-79 0.020 12.0
2 10-26-79 0.019 11.0
3 10-26-79 0.011* 8.56
Series Average 10.5
The measured particulate removal efficiency of the Crusher Area Baghouse
'was 99.69% and that of the truck Dump Area Baghouse was 85.65%.
Detailed particulate test data and test result summaries are presented
in Tables 1 through 12 in the Discussion of Test Results section of
this report. Particle size distribution test results are shown in
Tables 13 through 26. Data summaries for the visible emission tests
are presented in Tables 10, 12, and 27 through 34. See Table 35 for
summary of fugitive test data.
-3-
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INTRODUCTION
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 the Anaconda Copper Company's Butte, Montana
copper processing facility. The objective of the testing program was
to measure emission parameters relating to the ore crushing operations
at the plant.
The locations tested, plus the number and types of tests performed at
each site are listed below:
1. Crusher Grizzley East Duct
a. Three particulate tests by EPA Method 5.
b. Three particle size distribution tests by cascade
impaction (Andersen).
2. Crusher Hood Duct
a. Three particulate tests by EPA Method 5.
b. Three particle size distribution tests by cascade
impaction (Andersen).
3. Crusher Baghouse No. 1-2 Inlet Duct
a. Three particulate tests by EPA Method 5.
b. Three particle size distribution tests by cascade
impaction (Andersen).
A. Crusher Baghouse No. 1-2 Outlet Stack.
a. Three particulate tests by EPA Method 5.
b. One particle size distribution test by cascade
impaction (Andersen).
c. One opacity test by EPA Method 9 simultaneous with
particulate test run one.
5. Truck Dump Area Baghouse No. 3-*» Inlet Duct
a. Three particulate tests by EPA Method 5.
-5-
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b. Three particle size distribution tests by cascade
impact ion (Andersen).
6. Truck Dump Area Baghouse No. 3-*» Outlet Stack
a. Three particulate tests by EPA Method 5-
b. One particle size distribution test by cascade
impact ion (Andersen).
c. Two opacity tests by EPA Method 9 simultaneous
with particulate test runs one and two.
7. Crusher Grizzley East
a. Three opacity tests by EPA Method 9 and three
fugitive tests by Method 22. Visual determination
of plume opacity and frequency performed con-
currently with particulate tests.
8. Crusher Grizzley West
a. Three opacity tests by EPA Method 9 and three
fugitive tests by Method 22 performed in conjunc-
tion "with particulate tests.
9. Crusher Hood Area
a. Three EPA Method 9 and Method 22 tests performed
in conjunction with the particulate tests.
10. Fine Ore Feeder
a. Two EPA Method 22 tests conducted during particulate
test runs two and three on the Crusher unit.
11. Truck Dumping Area
a. Three EPA Method 9 and Method 22 tests performed
in conjunction with the particulate tests at the
truck dumping area.
12. Coarse Ore Transfer Point
a. Three EPA Method 9 and Method 22 tests conducted
independently of particulate tests.
-6-
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13. Coarse Ore Stockpile
a. Three EPA Method 9 and Method 22 tests performed
independently of particulate tests.
All tests were conducted during the period 2k through 26 October 1979 by
Weston personnel and were observed by Mr. Dennis P. Holzschuh, EPA
Technical Manager.
Test data and result summaries are presented in Tables 1 through 12 of
this report. Particle size distribution results are shown in Tables
13 through 26. Data summaries for the visible emission tests are pre-
sented in Tables 10, 12, and 27 through 35. Also included is a descrip-
tion of the test locations, test equipment, test procedures, sample re-
covery, and analytical methods used during the test program. Raw test
data, laboratory reports, sample calculations, equipment calibration
records, and a list of project participants-are provided in Appendices
A though E, respectively.
-7-
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PROCESS DESCRIPTION
GENERAL
A schematic flow diagram is presented in Figure 1. Copper ore is
transferred from the open pit Berkley mine to the primary crusher by
haul trucks with a capacity of 91 to 15^ Mg (100 to 170 T), at an
average rate of kO trucks per hour. Haul trucks unload ore into one of
two hoppers, with capacity of 363 Mg (^00 T). From hopper, two vibrating
grizzlies with critical size of ten centimeters (four inches) convey
undersize to storage and eventually to secondary crushing. The oversize
is transferred to a Traylor gyratory-type primary crusher with a capacity
of 2,270 Mg (2,500 T) per hour which produces an ore of less than four
inches. This ore is moved along with the undersize to one of six coarse
ore bins with each having a capacity of 3,200 Mg (3,500 T) or to a
storage area of 46,000 Mg (50,000 T). From these two storage facilities,
ore is fed into a 680 Mg (750 T) surge bin. Vibrating screens, with a
2.5 centimeter (one inch) critical size, take oversize to one of three
Symons secondary gyratory crushers. The crushed ore, along with the
undersize, is conveyed at an hourly rate of 2,^00 Mg (2,600 T) to one
of twelve fine ore bins, each with a capacity of 900 Mg (1,000. T). The
fine ore is fed to the rod mills where wet processing begins. The final
mill product is a concentrate slurry of approximately 27 percent copper.
The concentrate slurry is transported 33.5 kilometers (20 miles) in triple
compartment railcars to a smelter in Anaconda, Montana.
Following are descriptions of the control equipment that was tested.
Truck Unloading
An hourly average of 1,900 Mg (2,000 T) of copper ore is unloaded.
Emissions are ducted to a Fuller/Dracco, eight compartment, multi-bag,
automatic filter unit. Operating parameters are an air flow rate of
3,200 m /minute (112,500 cfm), an air/cloth ratio of 2.9 feet/minute,
snaking each compartment for seven minutes per hour, and nylon material.
Primary Crushing
Emissions are controlled by a Chem-jet wet suppression system and a bag-
house. The Chem-jet system uses an aqueous solution of Nalco 8800 at
a ratio of 1:3,000. Sprays are located near the grizzlies, at the
entrance under the feeder belts to the crusher, and near the conveyor
belt leaving the crusher. Emissions are vented from two-grizzlies,
primary crusher and conveyors leaving the crusher. Operating parameters
are identical with the truck unloading unit.
-9-
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Undersize
Minus 6"
Surge Pocket
400-Ton Capacity
1 Link-Belt Apron Feeder
60" x 15', 4,000 tph
No. 5-A Shuttle Conveyor
48" Wide, 700 fpm, 4,000 tph
6 Coarse Ore Bins
3,500-Ton Capacity Each
6 Hewitt Robins 60"
Vibrating Feeders
Run-of-Pit Ore
2 Truck Hoppers
400-Ton Capacity Each
2 Vibrating Grizzley Feeders
7' x 35' Variable Speed
No. 1 -A Conveyor
60" Wide, 700 fpm, 5,000 tph
No. 7 Conveyor
48" Wide, 600 fpm, 3,000 tph
To Secondary Crusher Surge Bins
Oversize
Plus 6"
2 Woodpicking Conveyors
84"-Wide
Gyratory Crusher
60" x 89", 2,500 tph
No. 2 Conveyor
48" Wide, 650 fpm, 4,000 tph
Stockpile
50,000-Ton Capacity
4 Link-Belt Apron Feeders
60" x 24'
No. 3-A Conveyor
48" Wide, 600 fpm, 3,000 tph
FIGURE 1 FLOWSHEET OF NEW PRIMARY CRUSHING PLANT
(CRUSHING, STORAGE, AND CONVEYING SYSTEMS FROM
_ _ THE BERKELEY PIT TO THE SECONDARY CRUSHING PLANT)
-10-
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PROCESS OPERATION
Primary Crusher
To determine If the process was representative, weight scale gauge
readings for ore leaving the primary crusher were taken every half
hour. Visual inspection of the crushing operation and of the two
conveyor belts discharging into the crusher showed no gross abnormalities
during the emission test period of October 25 and 26, 1979. The scale
readings during testing are listed below:
Time
Metric tons (tons/hour)
5
6
7
8
9
10
11
12
1
2
:00
:00
:00
:00
:00
:00
:00
:00
:00
:00
P
P
P
P
P
P
P
P
a
a
•
•
•
•
•
•
•
•
•
•
m
m
m
m
m
m
m
m
m
m
•
•
•
•
•
•
•
•
•
•
3:00 a..m.
2,130
2,300
2,050
2,200
950
1,900
2,150
1,050
2,380
1,200
2,050
(2,340)
(2,530)
(2,260)
(2,420)
(1,050)
(2,090)
(2,370)
(1,160)
(2,620)
(1,320)
(2,260)
Thus, during most of the test the crushing rate was close to the hourly
design rate of 2,270 metric tons.
A summary of .Methods 9 and 22 observations follows:
Method 9
Location
East Grizzley
East Grizzley
East Grizzley
West Grizzley
West Grizzley
West Grizzley
Crusher Hood
Crusher Hood
Crusher Hood
Baghouse Outlet
Date
10-25-79
10-25-79
10-26-79
10-25-79
10-25-79
10-26-79
10-25-79
10-25-79
10-26-79
10-25-79
Time
1630-1837
2050-2223
0040-0228
1630-1837
2050-2224
0040-0235
1645-1841
2050-2223
0036-0237
1630-1800
Opacity Readings (%)'
Average Maximum
0
0
0
0
0
1
2
2
1
0
3
0
1
0
0
8
6
12
8
1
-11-
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Method 22
Location
East Grizzley
East Grizzley
East Grizzley
West Grizzley
West Grizzley
West Grizzley
Crusher Hood
Crusher Hood
Crusher Hood
Date
10-25-79
10-25-79
10-26-79
10-25-79
10-25-79
10-26-79
10-25-79
10-25-79
10-26-79
Observation
Period (minutes)
90
79
90
93
79
90
86
80
79
Fugitive Emiss
ions
Emission
Time %
(minutestsecs)
(0:00)
(0:00)
(0:16)
(0:25)
(0:00)
(3:39)
(18:21)
(25:23)
(12:19)
0
0
0
0
0
k
21
31
15
Truck Unloading
To determine if the process was representative, visual inspections showed
no problems and gauge readings were taken as mentioned for the primary
crusher. The scale readings during the test period on October 26, 1979
follow:
Time
3:00 p.m.
k:QO p.m.
5:00 p.m.
6:00 p.m.
7:00 p.m.
8:00 p.m.
9:00 p.m.
10:00 p.m.
Metric tons (tons/hour)
800
330
250
900
080
050
950
2,050
2,
1,
2,
1,
2,
2.
(3,080)
(2,480)
(2,090)
(2,290)
(2,260)
(1,050)
(2,260)
Thus, during most of the test the crushing rate was close to the hourly
design rate of 2,270 metric tons.
A summary of Methods 9 and 22 observations follows:
-12-
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Location Date
Truck Dumping Area 10-26-79
Truck Dumping Area 10-26-79
Truck Dumping Area 10-26-79
Baghouse Outlet 10-26-79
Baghouse Outlet 10-26-79
Method 9
'Tjme_
1450-1549
1615-1714
1715-1814
1445-1628
1726-1836
Opacity Readings (%)
Average Maximum
2
1
2
1
1
5
6
6
5
5
Method 22
Location Date
Truck Dumping Area 10-26-79
Truck Dumping Area 10-26-79
Truck Dumping Area 10-26-79
Observation
Period (minutes)
60
60
60
Fugitive Emissions
Emission
Time %
(m?nutes;secs)
9:16
11:15
9:15
15
19
15
Process Samples
Grab ore samples were taken from conveyor belts that fed the primary
crusher during testing of the two stacks. These samples were taken to
ascertain if a correlation between ore moisture content and inlet
emissions could be developed. The sampling is summarized below:
Date
10-25-79
10-25-79
10-26-79
10-26-79
10-26-79
10-26-79
Stack Tested
Primary Crusher
Primary Crusher
Primary Crusher
Truck Unloading
Truck Unloading
Truck Unloading
Test Run
1
2
3
1
2
3
Time
5:01 p.m.
10:41 p.m.
1:4l a.m.
3:09 p.m.
5:45 p.m.
Sample Location
East Conveyor
West Conveyor
East Conveyor
West Conveyor
East Conveyor
9:00 p.m. West Conveyor
-13-
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DESCRIPTION OF TEST LOCATIONS
Crusher Grizzley East Duct
Two V I.D. test ports, 90° apart, were placed on a straight section of
the 32" I.D. metal stack at a location four diameters (101) downstream
and four diameters (101) upstream from the nearest flow disturbances.
EPA Method 1 criteria for this test location required a minimum of 36
traverse points. See Figure 2 for port and sampling point locations.
Crusher Hood Duct
Two V I.D. test ports were placed at right angles on the 38" I.D. metal
stack 1.3 diameters from both upstream and downstream flow disturbances.
Forty-eight sampling points (2*t per axis) were required for testing.
See Figure 3 for port and sampling point locations.
Crusher Baghouse No. 1-2 Inlet Duct
Four V I.D. test ports were located on the longest side of the 52" x
78" I.D. rectangular duct. The ports were placed one diameter from both
downstream and upstream flow disturbances. The test site required a
minimum of 48 traverse points (12 per port). Figure k illustrates port
and sampling point locations.
Crusher Baghouse No. 1-2 Outlet Stack
Two 4" I.D. test ports were installed in a straight section of the 7V
loD. metal stack. The ports were placed five diameters downstream and
two diameters upstream from the nearest gas stream flow disturbances.
Method 1 criteria required a minimum of 32 traverse points (16 per axis)
for this location. Figure 5 shows port and sampling point locations.
Truck Dump Baghouse No. 3-4 Inlet Duct
Two V I.D. test ports were placed 90° apart on the 72" I.D. metal duct
leading from the truck dumping area. The ports were placed 8.33 diameters
downstream and 2.0 diameters upstream from the nearest gas stream flow
disturbances. EPA Method 1 required a minimum of 12 traverse points
(6 per axis) for this ideal test location. See Figure 6 for port and
sampling point locations.
Truck Dump Baghouse No. 3-4 Outlet Stack
Two 4" I.D. test ports were placed 90° apart on a straight section of the
7V1 I.D. stack at a location five diameters downstream and two diameters
upstream from the nearest flow disturbances. Thirty-two traverse points
(16 per axis) were sampled during the testing program. See Figure 7
for port and sampling point locations.
-15-
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Anaconda Coppex, Company
Butte, Montana
Figure 2
Crusher Grizzley East Duct
Port and Sampling Point Locations
Duct Cross Sectional View
Traverse
Point
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
Distance from
Inside Near
Wall, Inches
1/2
1-3/8
2-3/8
3-1/2
4-5/8
6
7-1/2
9-1/2
12-1/4
19-3/4
22-1/2
24-1/2
26
27-3/8
20-1/2
29-5/0
30-5/8
31-1/2
Rail ing
-.16-
-------
jAnaconda Copper Company
Butte, Montana
Figure 3
Crusher Hood Duct
Port and Sampling Point Locations
Crusher Hood
Duct Cross Sectional View
-17-
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
2k
Distance From
Inside Hear
Wai 1 , Inches
1/2
1-1/2
2-1/8
3
4
5 .
6-1/8
7-3/8
8-3/4
10-3/8
12-1/4
15-1/4
22-7/8
25-3/4
27-5/8
29-1/4
30-5/8
31-7/8
32-7/8
34
35
36
36-3/4
37-1/2 "
-------
Anaconda Copper Company
Butte, Montana
Figure k
Crusher Baghouse No. 1-2 Inlet Duct
°ort and Sampling Point Locations
Test . i
Portsb'T*"
52"
78"
Side Cross Sectional View
Traverse
Point
Number
Distance From
Inside Near
Wall, Inches
1
2
3
4
5
6
7
8
9
10
11
12
2-1/8
6-1/2
10-7/8
15-1/4
19-5/8
2k
28-3/8
32-3A
37-1/8
41-1/2
45-7/8
50-1/4
-18-
-------
Anaconda Copper Company
Butte, Montana
Figure 5
Crusher Baghouse No. 1-2 Outlet Stack
Port and Sampling Point Locations
13'
Roof Line
Duct Cross Sectional View
Traverse
Point
Number
1
2
3
k
5
6
7
8
9
10
11
12
13
14
15
16
Distance From
Inside Near
Wall, Inches
1-1/4
3-5/8
6-1/4
9-1/4
12-1/2
16-1/4
21
27-3/4
46-1/4
53
57-3/4
61-1/2
64-3/4
67-3/4
70-3/8
72-3/4
Ox
T
33'
I.D.
FAN
-19-
-------
Anaconda Copper Company
Butte, Montana
Figure 6
Truck Dump Baghouse.No. 3-4 Inlet Duct
Port and Sampling Point Locations
TRUCK
DUMPING
AREA
Ground Level
-72"I.D.
Traverse
Point
Number
1
2
3
4
5
6
Distance From
Inside Near
Wa 1 1 , 1 nches
3-1/8
10-1/2
21-1/4
50-3/4
61-1/2
68-7/8
Duct Cross Sectional View
-20-
-------
.Anaconda Copper Company
Butte, Montana
Figurey
Truck Dump Baghouse No. 3-4 Outlet Stack
Port and Sampling Point Locations
74" I. D..
13'
Duct Cross Sectional View
Traverse
Point
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
Distance From
Inside Near
Wall lnehp<:
1-1/4
3-5/8
6-1/4
9-1/4
12-1/2
16-1/4
21
27-3/4
46-1/4
53
57-3/4
61-1/2
64-3/4
67-3/4
70-3/8
72-3/4
Ox
33'
I.D.
FAN
-21-
-------
DESCRIPTION OF SAMPLING TRAINS
Participate Sampling Trains
The test train utilized for participate sampling at all test locations
was the standard EPA Method 5 train (see Figure 8).
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 preweighted 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 pitot 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 since no combustion
products were found in any of the stack gas effluent samples.
Figure 9 shows the EPA Method 5 train utilized at the two Baghouse Out-
let Stack locations. 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 impinger, rather than the
flexible vacuum tubing.
Particle Size Distribution Sampling Apparatus
A stainless steel nozzle was connected directly to an 8-stage Andersen
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
-23-
-------
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.
-2k-
-------
0.75TO1 in.
TEMPERATURE SENSOR
t
> 0.75 in.
t
, PROBE
: TEMPERATURE CONTROLLED
HEATED AREA
THERMOMETER
PITOT TUBE
TEMPERATURE SENSOR
PROBE \
\—*
• STACK WALL
REVERSE-TYPE
PITOT TUBE
PITOT MANOMETER
ORIFACE
CHECK VALVE
BYPASS VALVE
X
X
VACUUM GAUGE
THERMOMETERS
DRY GAS METER
MAIN VALVE
AIR TIGHT PUMP
VACUUM
LINE
FIGURES PARTICULATE SAMPLING TRAIN
EPA METHOD 5
-------
I
ro
.TEMPERATURE
SENSOR
THERMOMETER
CHECK VALVE
THERMOMETERS
VACUUM LINE
VACUUM GUAGE
""M STACK
WALL
REVERSETYPE
PITOT TUBE
PITOT MANOMETER
ICE BATH
DISTILLED WATER
ORIFICE
AND
MANOMETER
FIGURE 9 PARTICIPATE SAMPLING TRAIN-ERA METHOD 5
-------
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 pitot 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 Grizzley East Duct
A series of three tests were conducted at the Crusher Grizzley East Duct
to measure the concentration and mass rate of particulate matter emissions.
Thirty-six traverse points (10 per port axis) were sampled for 2.5 minutes
each, resulting in a total test time of 90 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 7.
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 5 minutes,
which permitted collection of sufficient samples for analysis without
overloading the filter substrates. Sample volume, temperature, and
pressure data were recorded every 2.5 minutes during sampling. See Tables
13 through 15 for distribution plots.
-27- .
-------
Crusher Hood Duct
Three Method 5 tests were performed on the Crusher Hood Duct. Forty-
eight points were traversed (24 per axis) for two minutes each, yielding
a test period of 36 minutes.
Procedures for isokinetic sampling were identical to those described in
the Crusher Grizzley East Duct section.
See Tables 2 and 8 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 five minutes
in length. Sample volume, temperature, and pressure data were recorded
at 2.5 minute intervals. See Tables 16 through 18 for distribution plots.
Crusher Baghouse No. 1-2 Inlet Duct
Three 96-minute Method 5 test runs were performed at the baghouse inlet.
A total of 48 points were sampled for two minutes each per test.
Isokinetic sampling procedures were identical to those previously de-
scribed. Table 3 shows test data summarization and Table 9 presents test
results.
Three particle size distribution tests were conducted at an average point
of velocity in the gas stream. Test set one was four minutes in length,
while tests two and three were three minutes long. Readings were recorded
every minute during each test. See Tables 19 through 21 for distribution
plots.
Crusher Baghouse No. 1-2 Outlet Stack
Three Method 5 test runs were conducted on the Crusher Baghouse No. 1-2
Outlet Stack. Thirty-two sampling points (16 per axis) were sampled for
three minutes each, yielding a test period of 96 minutes.
Sampling procedures were identical to those previously described. See
Tables 4 and 10 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 60 minutes with readings taken every five
minutes. See Table 22 for particle size distribution plot.
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 30.
-28-
-------
Truck Dump Baghouse No. 3-4 Inlet Duct
Three test runs were conducted by EPA Method 5 procedures at the inlet
to the Ho. 3"^ baghouse. A total of twelve traverse points (6 per axis)
were sampled for five minutes each, resulting in a total test time of
60 minutes. Tables 5 and 11 show test data and test results, respectively.
Three particle size distribution tests were performed at a point of
average velocity over a 15-minute period. Readings were taken every five
minutes during sampling. Tables 23 through 25 show the particle size
distribution.
Truck Dump Baghouse Mo. 3"** Outlet Stack
Three EPA Method 5 tests were performed at the outlet simultaneously with
particulate test runs at the inlet. Thirty-two points were traversed
(16 per port axis) for two minutes each, yielding a test period 6k minutes
in length.
Procedures for isokinetic sampling were identical to those described for
the first test location. Test data and test result summaries are pro-
vided in Tables 6 and 12, respectively.
One particle size distribution test was performed at a point of average
velocity. The sample time was 90 minutes in.length and readings were
taken every five minutes. Table 26 shows the particle size distribution
plot.
Visual determination of plume opacity were performed by a certified ob-
server according to Method 9 procedures. Opacity readings were taken
during particulate test runs one and two. A summary of results is pre-
sented in Table 32.
-29-
-------
ANALYTICAL PROCEDURES
Participate 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 filter holder was rinsed with 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 immedi-
ately weighted.
An acetone sample was retained for blank analysis.
Particulate Analyses
The filters (Sample 1) and any loose fragments were desiccated for 24
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.
-31-
-------
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 to Weston's laboratory.
Each cascade impactor filter was fired at 525°C and preweighed 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.
-32-
-------
DISCUSSION OF TEST RESULTS
Particulate test data and test result summaries are presented in Tables
1 through 12 of this section. Tables 13 through 26 list the particle
size distribution of the particulate matter for all locations. Visible
emission test data summaries are shown in Tables 10, 12 and 27 through
3^. See Table 35 for fugitive emission test result summaries.
No unusual sampling difficulties or process operating problems were
encountered during any of the test periods.
The quantity of partf-culate matter discharged to the atmosphere from the
Crusher Baghouse No. 1-2 Outlet Stack was <_ 0.007 grains/DSCF and <_ 5.01
pounds/hour. The certified visible emission observer recorded plume
opacities of <_ 10 percent for this source.
The particulate matter discharged from the Truck Dump Baghouse No. 3~^
Outlet Stack was <_ 0.020 grains/DSCF and 12.0 pounds/hour. Opacity
readings recorded by the certified observer were <_ 20 percent.
The particulate removal efficiency of the Crusher Baghouse No. 1-2 averaged
99.69 percent for the three test sets; efficiency of Truck Dump Baghouse
No. 3-i* averaged 85.65 percent.
Note that the illumination at the Fine Ore Feeder was <( 10 foot-can.dles
which is the level considered necessary for proper application of the
method. Illumination was )> 10 foot-candles at all other test points.
The trace metals analysis results from samples supplied to York Research
Corporation are included in Appendix B.
-33-
-------
Anaconda Copper Company
Butte, Montana
Table 1
Crusher Grizzley East Duct
SUMMARY OF TEST DATA
Test Data '
Test Run Number 1 2 3
Test Date 10-25-79 10-25-79 10-26-79 Average
Test Period • 1630 - 1820 2050 - 2235 0040 - 0235
Samp I Ing Data
Sampling Duration, minutes 90.0 90.0 90.0
Nozzle Diameter, Inches 0.188 0.188 0.188
Barometric Pressure, inches mercury 24.04 2k.Ok 24.04
Average Orifice Pressure Differential, inches water 1.57 1.90 1.91
Average Dry Gas Temperature at Meter, °F 96. 95. 94.
Total Water Collected by Train, ml 33.2 15.5 8.0
standard Volume of Water Vapor Collected, cubic feet 1.56 0.73 0.38
Dry Gas Meter Calibration Factor, dimensionless 0.998 0.998 0.998
Sample Volume at Meter Conditions, cubic feet 72.88 80.83 80.63
Sample Volume at Standard Conditions, cubic feet' 55.73 61.95 61.94
Gas Stream Composition
C02. percent by volume 0.0 0.0 0.0 0.0
02, percent by volume 20.9 20.9 20.9 20.9
CO, percent by volume 0.0 0.0 0.0 0.0
N2, percent by volume 79.1 79.1 79.1 79.1
Moisture in Gas Stream, percent by volume 2.7 1.2 0.6 1.5
Mole Fraction of Dry Gas 0.973 0.988 0.99') 0.985
Molecular Weight of Dry Gas 28.97 28.97 28.97 28.97
Molecular Weight.of Wet Gas . 28.67 • 28.84 ' 28.90 28.80
Gas Stream Velocity and Volumetric Flow
Static Pressure, inches water -1.7 -1.65 -1.7 -1.68
Absolute Pressure, inches mercury 23.92 23.92 23.92 23J92
Average Temperature, °F 76. 76. 70. yij.
Pitot Tube Calibration Coefficient, dimensionless 0.848 0.848 0.848
Total Number of Traverse Points 36.0 36.0 36.0
Velocity at Actual Conditions, feet/second 67.6 74.3 73.9 72 0
Stack/duct Cross-Sectional Area, square feet 5.59 5.59 5.59
Volumetric Flow at Actual Conditions, cubic feet/minute 22,700. 24,900. 24,800. 24 100
Volumetric Flow at Standard Conditions, cubic feet/minute 17,400. 19,400. 19,600. 18*800
Percent Isokinetic 103.3 103.0 101.6 ,02.6
Unit/Process Operations Data Monitored by GCA/Technology Division
Standard Conditions « 68 F (20 C) and 29-92 inches (760 mm) mercury, dry basis.
-35-
-------
Anaconda Copper Company
Butte, Montana
Table 2
Crusher Hood Duct
SUMMARY OF TEST DATA
Test Data
Test Run Number
Test Date
Test Period
Samp I 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
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
ASsolute Pressure, inches mercury
Average Temperature, °F
Pitot Tube Calibration Coefficient, dimension less
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
10-25-79
1638 - 1843
96.0
0.238
24.04
2.43
95.
16.
0.75
0.999
90.07
69.29
O.o
20.9
0.0
79.1
1.1
0.989
28.97
28.85
2
10-25-79
2047 - 2226
96.0
0.238
24.04
2.51
97.
26.5
1.25
0.999
92.49
70.95
0.0
20.9
0.0
79.1
1.7
0.983
28.97
28.78-
10-26-79
0040 - 0238
96.0
0.238
24.04
2.43
83.
18.
0.85
0.999
90.20
70.91
0.0
20.9
0.0
79.1
1.2
0.988
28.97
28.84
Average
0.0
20.9
0.0
79.
1,
0.986
28.97
28.82
-1.7
23.92
75.
0.846
48.0
51.3
7.88
24,200.
18,900.
-1.6
23.92
72.
0.846
48.0
52.2
7.88
24,700.
19,200.
-1.6
23.92
64.
0.846
48.0
51.1
7.88
24,200.
19,200.
-1.6
23.92
70.
-
-
.51.5
-
24,400.
19,100.
97.4
98.0
97.9
97.8
Unit/Process Operations Data
Monitored by GCA/Technology Division
Standard Conditions
68°F (20°C) and 29.92 inches (760 mm) mercury, dry basis.
-36-
-------
Anaconda Copper Company
Butte, Montana
Table 3
Crusher Baghouse No. 1-2 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
-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
10-25-79
1638 - 1835
96.0
0.179
24.04
0.73
79.
14.7
0.69
1.032
48.59
39.58
0.0
20.9
0.0
79.1
1.7
0.983
28.97
28.78
10-25-79
2045 - 2230
96.0
0.179
24.04
0.85
71.
14.1
0.66
1.032
52.12
43.05
0.0
20.9
0.0
79.1
1.5
0.985
28.97
28.80
10-26-79
0045 - 0250
96.0
0.179
24.04
0.83
70.
13.4
0.63
1.032
51.46
42.64
Average
0.0
20.9
0.0
79.1
1.5
0.985
28.97
28.81
0.0
20.9
0.0
79.1
1.6
0.984
28.97
28.80
Static Pressure, inches water
ASsolute 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
-2.5
23.86
75.
0.848
48.0
49.3
28.17
83,300.
64,400.
-2.7
23.84
72.
0.848
48.0
52.6
28.17
89,000.
69,300.
-2.9
23.83
71.
0.848
48.0
52.8
28.17
89,200.
69,600.
-2.7
23.84
73.
_
51.6
87,2007
67,800.
103.2
104.4
102.9
103.5
Unit/Process Operations Data
Monitored by GCA/Technology Division
Standard Conditions
68°F (20°C) and 29-92 inches (760 mm) mercury, dry basis.
-37-
-------
Anaconda Copper Company
Butte, Montana
Table 4
Crusher Baghouse No. 1-2 Outlet Stack
SUMMARY OF TEST DATA
Test Data
Test Run Number
Test Date '
Test Period
Samp I 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
C02. percent by volume
Oj, 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
ASsolute 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
10-25-79
1630 - 1805
96.0
0.197
24.04
1.31
78.
16.5
0.78
1.036
64.85
53.21
0.0
20.9
0.0 .
79.1
1.4
0.986
28.97
28.81
2
10-25-79
2049 - 2237
96.0
0.197
24.04
1.29
68.
26.7
1.26
1.036
64.40
53.79
0.0
20.9
0.0
79.1
2.3
0.977
28.97
28.72
10-26-79
0045 - 0240
96.0
0.197
24.04
1.52
52.
26.0
1.22
1.036
69.11
59.65
0.0
20.9
0.0
79.1
2.0
0.980
28.97
28.75
Average
0.0
20.9
0.0
79.1
1.9
0.981
28.97
28.76
-0.49
24.00
78.
0.848
32.0
55.4
29.87
99,200.
76,900.
-0.26
24.02
76.
. 0.848
32.0
55.1
29.87
98,700.
76,300.
-0.38
24.01
73.
0.848
32.0
58.8
29.87
105,000.
82,100.
-0.
-
76.
~
~
56.1
"
101,000.
78,400.
101.7
103.6
106.8
104.0
Unit/Process Operations Data
Monitored by GCA/Technology Division
Standard Conditions = 68 F (20 C) and 29-92 inches (760 mm) mercury, dry basis.
-38-
-------
Anaconda Copper Company
Butte, Montana
Table 5
Truck Dump Baghouse No. 3-4 Inlet Duct
SUMMARY OF TEST DATA
Test Data
Test Run Number 1 2 3 Average
Test Date 10-26-79 10-26-79 10-26-79
Test Period 1445 - 1625 1730 - 1845 2037 - 2145
Sampling Data
Sampling Duration, minutes 60.0 60.0 60.0
Nozzle Diameter, inches 0.227 0.227 0.227
Barometric Pressure, inches mercury 24.44 24.44 24.44
Average Orifice Pressure Differential, inches water 1.69 1.69 1.75
Average Dry Gas Temperature at Meter, °F 65. 73. 72.
Total Water Collected by Train, ml 13.1 10.4 11.4
-tandard Volume of Water Vapor Collected, cubic feet 0.62 0.49 0.54
Dry Gas Meter Calibration Factor, dimensionless 1.032 1.032 1.032
Sample Volume at Meter Conditions, cubic feet 't'.gi 45.27 45.46
Sample Volume at Standard Conditions, cubic feet' 35.68 38.02 38.26
Gas Stream Composition
C02, percent by volume 0.0 0.0 0.0 0.0
02, percent by volume 20.9 20.9 20.9 20.9
CO, percent by volume 0-0 0.0 0.0 0.0
N2, percent by volume 79.1 79.1 79.1 79.1
Moisture In Gas Stream, percent by volume '•? '-3 1.4 1.5
Mole Fraction of Dry Gas 0.983 0.987 0.986 0.985
Molecular Weight of Dry Gas ' 28.97 . 28.97 28.97 28.97
Molecular Weight of Wet Gas .28.78 28.83 28.82' 28.81
Gas Stream Velocity and Volumetric Flow
Static Pressure, inches water -0.53 -0.65 -0.45 -0.54
Absolute Pressure, inches mercury 24.40 24.39 24.41 24 4o
Average Temperature, °F 43. 43. 38. j^'
Pitot Tube Calibration Coefficient, dimensionless 0.848 0.848 0.848 1
Total Number of Traverse Points 12.0 12.0 12.0
Velocity at Actual Conditions, feet/second 45.0 45.2 45.9 4q 4
Stack/duct Cross-Sectional Area, square feet 28.27 28.27 28.27 1
Volumetric Flow at Actual Conditions, cubic feet/minute 76,300. 76,700. 77,900. 77 ggo
Volumetric Flow at Standard Conditions, cubic feet/minute 64,.100. 64,500. 66,400. 6s'oOo'
Percent Isokinetic 93.3 gg.j, g6>6 96.]
Unit/Process Operations Data Monitored by GCA/Techno logy Division
'standard Conditions = 68°F (20°C) and 29.92 inches (760 mm) mercury, dry basis.
-39-
-------
Anaconda Copper Company
Butte, Montana
Table 6
Truck Dump Baghouse No. 3"** Outlet Stack
SUMMARY OF TEST DATA
Test Data
Test Run Number 1 2 3
Test Date 10-26-79 10-26-79 10-26-79 Average
Test Period 1445-1630 1730-1845 2037-2145
SampI Ing Data
Sampling Duration, minutes 64.0 64.0 64.0
Nozzle Diameter, inches 0.197 0.197 0.197
Barometric Pressure, inches mercury 24.44 24.44 24.44
Average Orifice Pressure Differential, inches water 1.03 1.03 1.1
Average Dry Gas Temperature at Meter, °f 54. 5^. 57^
Total Water Collected by Train, ml 8.0 3.2 s'.O
standard Volume of Water Vapor Collected, cubic feet 0.38 0.15 0.24
Dry Gas Meter Calibration Factor, dimensionless 1.036 1.036 K036
Sample Volume at Meter Conditions, cubic feet 37.72 37-99 38.75 I
Sample Volume at Standard Conditions, cubic feet' 32.91 33.17 33.63
Gas Stream Composition
C02, percent by volume 0.0 0.0 0.0 0.0
02, percent by volume 20.9 20.9 20.9 20*9
CO, percent by volume • 0.0 0.0 0.0 0.0
N2, percent by volume 79.! 79.1 79.1" .79.1
Moisture in Gas Stream, percent by volume 1.1 0.45 0.70 0.75
Mole Fraction of Dry Gas 0.989 0.995 0.993 0.992
Molecular Weight of Dry Gas 28.97 28.97 28.97 28.97
Molecular Weight of Wet Gas . ' 28.85 28.92 28!89 28.89
Gas Stream Velocity and Volumetric Flow
Static Pressure, inches water -0.34 -0.35 -0.27 -o 32
Absolute Pressure, inches mercury 24.42 24 41 24 42 9/1*^9
Average Temperature, °F 55. 51^ 51 _ _ °
Pitot Tube Calibration Coefficient, dimensionless 0.844 0.844 o'844
Total Number of Traverse Points 32.0 32.0 32*0
Velocity at Actual Conditions, feet/second 46.6 45*9 47°2 Uf,~ft
Stack/duct Cross-Sectional Area, square feet 29.87 29.87 29.87 1
Volumetric Flow at Actual Conditions, cubic feet/minute 83,600. 82,30o! 84,60o! 83 SOfl"
Volumetric Flow at Standard Conditions, cubic feet/minute 69*200. 68*600. 70*900° 69*600*
Percent Isokinetic ,OM ,Q6-6 ,0/)>7 l(}5>1(
Unit/Process Operations Data Monitored by GCA/Technology Division
Standard Conditions = 68 F (20 C) and 29.92 inches (760 mm) mercury, dry basis.
-40-
-------
Anaconda Copper Company
Butte, Montana
Table 7
Grizzley East Duct
Summary of Test Results
Test Data
Test Number 1 2 3 Average
Test Date 10-25-79 10-25-79 10-26-79
Test Time 1630-1820 2050-2235 0040-0235
Gas Flow
Standard Cubic Feet/minute, dry 17,400. 19,400. 19,600. 18,800.
Actual Cubic Feet/minute, wet 22,700. 24,900. 24,300. 24,100.
Part!culates
Front Half Acetone Wash
Fraction, g 0.1596 0.1142 0.2483 0.1740
Filter Catch Fraction, g . 0.3067 0.1198 0.0251 0.1505
Total Particulates, g 0.4663 0.2340 0.2734 0.3246
Part Iculate Emissions
Grains/dry standard cubic foot2 0.129 0.058 0.068 °«°85
Pounds/hour 19.2 9.67 11.5 13'5
Based on Total Particulates captured by train.
Standard Conditions = 68 F and 29.92 inches mercury.
-------
Anaconda Copper Company
Butte, Montana
Table 8
Crusher Hood Duct
Summary of Test Results
Test Data
Test Number 1 2 3 Average
Test Date 10-25-79 10-25-79 10-26-79
Test Time 1638-1843 2047-2226 0040-0238
Gas Flow
Standard Cubic Feet/minute, dry 18,900. 19,200. 19,200. 19,100.
Actual Cubic Feet/minute, wet 24,200. 24,700. 24,200. 24,400.
Partlculates
Front Half Acetone Wash
Fraction, g 0.3740 0.2108 0.2654 0.2834
Filter Catch Fraction, g 6.5815 6.5955 4.3482 5.8417
Total Particulates, g 6.9555 6.8063 4.6136 6.1251
Particulate Emissions
2
Grains/dry standard cubic foot 1,55 1.48 1.00 1.34
Pounds/hour 251. 244. 166. 220.
Based on Total Particulates captured by train.
Standard Conditions = 68°F and 29.92 inches mercury.
-42-
-------
Anaconda Copper Company
Butte, Montana
Table 9
Crusher Baghouse No. 1-2 Inlet Duct
Summary of Test Results
Test Data
Test Number 1 2 3 Average
Test Date 10-25-79 10-25-79 10-26-79
Test Time 1638-1835 20^5-2230 00^5-0250
Gas Flow
Standard Cubic Feet/minute, dry 64,^00. 69,300. 69,600. 67,800.
Actual Cubic Feet/minute, wet 83,300. 89,000. 89,200. 87,200.
Particulates
Front Half Acetone Wash
Fraction, g 4.3337 3.0514 2.6202 3.5211
Filter-Catch Fraction, g 2.3105 4.2701 2.0518 2.8775
Total Particulates, g 7.1942 7.3215 4.6800 6.3986
Participate Emissions
Grains/dry standard cubic foot2 2.81 2.62 1.69 2-37
Pounds/hour 1,549. 1,558. 1,010. 1,372.
Based on Total Particulates captured by train,
f\
Standard Conditions = 68 F and 29.92 inches mercury.
-------
Anaconda Copper Company
Butte, Montana
Table 10
Crusher Baghouse No, 1-2 Outlet Stack
Summary of Test Results
Test Data
Test Number 1 2 3 Average
Test Date 10-25-79 10-25-79 10-26-79
Test Time 1630-1805 2049-2237 0045-0240
Gas Flow
Standard Cubic Feet/minute, dry 76,900. 76,300. 82,100. 78,400,
Actual Cubic Feet/minute, wet 99,200. 98,700. 105,400. 101,100.
Partlculates
Front Half Acetone Wash
Fraction, g 0.0166 0.0127 0.0240 0.0180
Filter Catch Fraction, g 0.0021 0.0029 0.0027 0.0026
- Total Particulates, g •' 0.0187 0.0156. 0.0275 0.0206
Part Iculate Emissions
Grains/dry standard cubic foot2 0.005 0.005 0.007 0.006
Pounds/hour 3.58 2.93 5.01 3.84
Baghouse Particulate Removal
Efficiency, percent 99.77 99.81 99.50 99.69
Visible Emissions^
^15 percent opacity, minutes
observed 0 - -
10 percent opacity, minutes
observed i -
5 percent opacity, minutes
observed 3 -
0 percent opacity, minutes
observed 86i - -
Unobserved readings, minutes
observed 0 -
Based on Total Particulates captured by train.
n
Standard Conditions = 68°F and 29.92 inches mercury.
Opacity results listed are in minutes of the observed reading during
the test period.
-44-
-------
Anaconda Copper Company
Butte, Montana
Table 11
Truck Dump Baghouse No. 3~4 Inlet Duct
Summary of Test Results
Test Data
Test Number 1 • 2 3 Average
Test Date 10-26-79 10-26-79 10-26-79
Test Time . 1445-1625 1730-1345 2037-2145
Gas Flow
Standard Cubic Feet/minute, dry 64,100. 64,800. 66,400. 65,100.
Actual Cubic Feet/minute, wet 76,300. 76,700. 77,900. 77,000.
Particulates
Front Half Acetone Wash
Fraction, g 0.0809 0.1144 0.0609 . 0.0881
Filter Catch Fraction, g 0.3064 0.2205 0.1724 0.2331
Total Particulates, g 0.3873 0.3349 0.2413 0.3212
Particulate Emissions
Grains/dry standard cubic foot2 0.168 0.134 0.097 °'133
Pounds/hour 92.1 75.5 55.4 74.3
Based on Total Particulates captured by train,
o
Standard Conditions = 68°F and 29.92 inches mercury.
-------
Anaconda Copper Company
Butte, Montana
Table 12
Truck Dump Baghouse No. 3-4 Outlet Stack
Summary of Test Results
Test
Gas
Part
Part
Visi
^
Data
Test Number
Test Date
Test Time
Flow.
Standard Cubic Feet/minute, dry
Actual Cubic Feet/minute, wet
iculates
Front Half Acetone Wash
Fraction, g
Filter Catch Fraction, g
Total Part iculates , g
iculate Emissions
2
Grains/dry standard cubic foot
Pounds/hour
Baghouse Part iculate Removal
Efficiency, percent
ble Emissions
: 25 percent opacity, minutes
observed
20 percent opacity, minutes
observed
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
10-26-79
1445-1630
69,200.
83,600.
0.0373
0.0058
0.0431
0.020
12.0
86.97
0
i
3/4
1 3/4
12 1/4
54 3/4
0
.2 3 Average
10-26-79 10-26-79
1730-1845 2037-2145
68,600. 70,900. 69,600.
82,300. 84,600. 83,500.
0.0298 0.0272 0.0314
0.0104 0.0035 0.0066
0.0402 0.0307 0.0380
0.019 0.014 0'°18
11.0 8.56 10-5
85.43 84.55 85'65
0 - °
.
-i / 1
3/4 - 3/4
21/4 - 2
9 A i Q
„ ... 3/8
52 - 53 3/8
0 - °
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.
-46-
-------
Anaconda Copper Company
Butte, Montana
TABLE 13
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: 10-25-79
Location: Anaconda Copper Company
Sampling Location: Grizzley East Duct
Traverse Point No. Sampled: X-1
Pbar (in. Hg.) 24.04-
Stack Temp (°F) 74.
Sample Time (Min.) 5.0
Sample Volume (cf) 3.79
Moisture (% H20) 1.0
Meter Temp (°F) 100.
Flow Setting, AH
(in. H20) 1-55
Nozzle Diameter (in.)°-179
Sample Flow Rate (at stack conditions): 0.58cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
5.4
3.2
1.1
0.1
0.3
0.2
0.5
0.4
%
48.2
28.6
9.8
0.9
2.7
1.8
4.5
3.5
Cumulative
%
100
51.8
23.2
13.4
12.5
9.8
8.0
3.5
EAD
(Microns)
12.5
8.0
5.2
3.7
2.3
1.2
0.74
0.49
Backup
Filter
0.0
0.0
0,0
TOTAL
11.2
-47-
-------
Crusher Grizzley East
Particle Size Distribution
Run 1
u
*i
fi
o
cc
u
1
O
oe
UJ
o
LU
U.
U.
10.0
|-°
8.0
7.0
6.0
5.0
4.0
3.0
2.0
1.0
0.9
0.8
0.7
0.6
0.5
O.k
0.3
0.2
0.1
0.01 0.05 O.I 0.2 0.5 I
10 20 30 40 50 80 70 60
CUMULATIVE PERCENTAGE
90
95
M 99
By Weight Less Than Diameter)
-------
Anaconda Copper Company
Butte, Montana
TABLE 14
PARTICLE SIZE DISTRIBUTION
Run: 2
Date: 10-25-79
Location: Anaconda Copper Company
Sampling Location: Grtzzley"East Duct
Traverse Point No. Sampled: X-9
P. (in. Hg.) 24.04
bar
Stack Temp ( F) 74.
Sample Time (Min.) 5.0
Sample Volume (cf) 3.74
Moisture (% H20) 1.0
Meter Temp (°F) 97.
Flow Setting, AH
(in. H20) 1-55
Nozzle Diameter (in.) 0.179
Sample Flow Rate (at stack conditions): °'58 cfm
1
2
3
k
S
6
7
8
Net Wt.
(mg)
1.6
1.8
0.6
0.1
0.1
0.2
0.3
0.1
32.0
36.0
12.0
2.0
2.0
4.0
6.0
2.0
Cumulative
%
10000
68.0
32.0
20.0
18.0
16.0
12.0
6.0
EAD
(Microns)
12.5
8.0
5.2
3.7
2.3
1.2
0.71*
0.49
Backup
Filter
0.2
4.0
4.0
TOTAL
5.0
-------
Crusher Grizzley East
Particle Size Distribution
Run 2
Ul
O
t
u
1
85
LU
O
tc
O
I
O
oc
LU
<
LU
>
\-
U
111
U.
10.0
2-°
8.0
7.0
6.0
5.0
U.O
3.0
2.0
1.0
°-2
0.8
0.7
0.6
0.5
O.k
0.3
0.2
0.1
0.01 O.OS O.I 0.2 0.5 I 2
10
SO
20 30 40 SO 60 70 60
CUMULATIVE PERCENTAGE
(% By Weight Less Than Diameter)
95
N 96
98.6 68.9
99.99
-------
Anaconda Copper Company
Butte, Montana
TABLE 15
PARTICLE SIZE DISTRIBUTION
Run: 3
Date: 10-25-79
Location: Anaconda Copper Company
Sampling Location: Grizzley East Duct
Traverse Point No. Sampled: X-2
Sample Flow
Plate
No.
1
2
3
4
5
6
7
8
Backup
Filter
Rate (at stack
Net Wt.
(nig)
2.6
0.6
0.2
0.1
0.1
0.3
0.4
0.2
0.4
condi tions) :
%
53.1
12.2
4.1
2.0
2.0
6.1
8.2
4.1
8.2
(in. H20)
Nozzle Diamet
0.60cfm
Cumulative
%
100.
46.9
34.7
30.6
28.6
26.6
20.5
12.3
8.2
P. (in. Hg.)
bar- 3
Stack Temp ( F)
Sample Time (Min.)
Sample Volume (cf)
Moisture (% H20)
Meter Temp (°F)
Flow Setting, AH
(in. H20)
Nozzle Diameter (in.)
24.04
74.
5.0
3.90
1.0
97.
1.55
0.179
EAD
(Microns)
12
7.8
5.3
3.7
2.3
1.2
0.73
0.47
TOTAL
4.9
-51-
-------
o
o
o
£
I
vn
o
oc
LU
UJ
10.0
9.0
8.0
7.0
6.0
5.0
4.0
3.0
2.0
1.0
0.9
0.8
0.7
0.6
0.5
O.k
0.3
0.2
0.1
Crusher Grizzley East
Particle Size Distribution
Run 3
0.01 0.05 O.I 0.2 0.5 I
10
90
20 30 40 50 60 70 80
CUMULATIVE PERCENTAGE
(% By Weight Less Than Diameter)
95
.1 99.9
99.99
-------
Anaconda Copper Company
Butte, Montana
TABLE 16
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: 10-25-79
Location: Anaconda Copper
Sampl Ing
Traverse
Location: Crusher
Point No. Sampled:
Sample Flow Rate (at stack
Plate
No.
1
2
3
4
5
6
7
8
Backup
Filter
Net Wt.
(mg)
45.9
3U3
7.0
2.7
1.4
1.2
0.6
0.8
1.6
Company
Hood Duct
X-3
condi tions) :
%
49.6
33.8
7.6
2.9
1.5
1.3
0.6
0.9
1.8
Pbar (in. Hg.)
Stack Temp (°F)
Sample Time (Min.)
Sample Volume (cf)
Moisture (% H.O)
Meter Temp (°F)
Flow Setting, AH
(in. H20)
Nozzle Diameter (i
0.75:fm
Cumulative
%
100. •
50.4
16.6
9
6.1
4.6
3.3
2.7
1.8
24.04
70.
5.
4.89
1.3
107
2.65
n.) 0-242
EAD
(Microns)
11.3
7.0
4.5
3.5
2.1
1.1
0.64
0.43
TOTAL
92.5
-53-
-------
in
§
u
1
fi
I
vn
£
f ^
oc
<
tu
>
o
10.0
2-°
8.0
7.0
6.0
3.0
!.0
°'t
0.8
0.7
0.6
0.5
o.:
0.1
Crusher Hood Duct
Particle Size Distribution
Run 1
0.01 0.05 O.I 0.2 0.5 1 2
10
90
20 30 40 50 60 70 80
CUMULATIVE PERCENTAGE
(% By Weight Less Than Diameter)
95
91 99
9.1 99.9
-------
Anaconda Copper Company
Butte, Montana
TABLE 17
PARTICLE SIZE DISTRIBUTION
Run: 2
Date: 10-25-79
Location: Anaconda Copper Company
Sampling Location: Crusher Hood Duct
Traverse Point No. Sampled: X-11
Pu (in. Hg.) 24.04
bar
Stack Temp ( F) 70.
Sample Time (Min.) 5.0
Sample Volume (cf) ^-89
Moisture (% H20) 1.3
Meter Temp (°F) 107
Flow Setting, AH
(in. H20) 2.65
Nozzle Diameter (in.) 0.242
Sample Flow Rate (at stack condi tions): 0.75 cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
40.9
17.6
8.4
1.3
1.4
0.6
0.6
0.4
%
56.1
24.1
11.5
1.8
1.9
0.8
0.8
0.6
Cumulative
%
100.
43.9
19.8
8.3
6.5
4.6
3.8
3.0
EAD
(Microns)
11.3
7.0
4.5
3.5
2.05
1.05
0.64
0.43
Backup
Filter
1.8
2.4
2.4
TOTAL
72.9
-55-
-------
95-
Crusher Hood Duct
Particle Size Distribution
Run 2
EFFECTIVE AERODYNAMIC PARTICLE DIAMETER, microns
O O OOOOOOO— 10 VjO .p- VI ON ->J OOVO C
— • ro u* &• vn o\ *
-------
Anaconda Copper Company
Butte, Montana
TABLE 18
PARTICLE SIZE DISTRIBUTION
Run: 3
Date: 10-25-79
Location: Anaconda Copper Company
Sampling Location: Crusher Hood Duct
Traverse Point No. Sampled: X-6
Sample Flow
Plate
No.
1
2
3
4
5
6
7
8
Backup
Filter
Rate (at stack
Net Wt.
(mg)
33.8
27.0
4.9
1.8
0.7
0.3
0.5
0.6
1.7
conditions) :
%
47.5
37.9
6.9
2.5
1.0
0.4
0.7
0.8
2.3
(in. H20)
Nozzle Diamet
0.77cfm
Cumulative
%
100.
52.5
14.6
7.7
5.2
4.2
3.8
3.1
2.3
Pbar (in. Hg.)
Stack Temp ( F)
Sample Time (Min.)
Sample Volume (cf)
Moisture (% H^Q)
Meter Temp ( F)
Flow Setting, AH
(in. H20)
Nozzle Diameter (in.
2k. Ok
70.
4.
3.99
1.3
103.
2.65
\ 0.242
EAD
(Microns)
11.
6.8
4.6
3.2
2.0
1.0
0.63
0.42
TOTAL
71.2
-57-
-------
vn
oo
M
O
u
1
O
cc
O
X
O
oe
UJ
<
LU
>
O
10.0
2'°
8.0
7.0
6.0
5.0
k.O
3.0
2.0
1.0
0.9
0.8
0.7
0.6
0.5
0.4
0.3
0.2
0.1
Crusher Hood Duct
Particle Size Distribution
Run 3
o.oi o.os o.i 0.2 o.s i
10 20 30 40 50 60 70 80 90
CUMULATIVE PERCENTAGE
(2 By Weight Less Than Diameter)
05
.1 99.0
-------
Anaconda Copper Company
Butte, Montana
TABLE 19
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: 10-26-79 P (in. Hg.) 24.44
I* ' _
Location: Anaconda Copper Company Stack Temp ( F) 73.
Sampling Location: No. 1-2 Baghouse InletSample Time (Min.) *«0
Traverse Point No. Sampled: A~8 Sample Voljjme (cf) 2.26
Moisture (% H£0) I-6
Meter Temp (°F) 55.
Flow Setting, AH
(in. H20) °-81*
Nozzle Diameter (in.) °'179
Sample Flow Rate (at stack conditions): 0.48cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
214.2
3.2
8.7
1.4
0.5
0.5
0.2
0.1
%
93.4
1.4
3.8
0.6
0.2
0.2
0.1
0.1
Cumulative EAD
% (Microns)
100. 14.0
6.6 8.6
5.2 5.6
1.4 4.0
0.8 2.6
0.6 1.3
0.4 0.82
0.3 0.55
Backup
Filter 0.5 0.2 0.2
TOTAL 229.3
-59-
-------
No. 1-2 Baghouse Inlet
Particle Size Distribution
Run 1
i
ON
O
i
u
z
o
LU
—I
CJ
K
ce
u
UJ
u
10.0
§'°
8.0
7.0
6.0
5.0
4.0
3.0
2.0
1.0
0.9
0.8
0.7
0.6
0.5
0.3
0.2
0.1
O.Dl 0.05 O.I 0.2 0.5 I
10 20 30 40 SO 60 70 BO
CUMULATIVE PERCENTAGE
BO
M 98
99.1 99.9
99.99
(% By Weight Less Than Diameter)
-------
Anaconda Copper Company
Butte, Montana
TABLE 20
PARTICLE SIZE DISTRIBUTION
P. (in. Hg.)
Run: 2
Date: 10-26-79
Location: Anaconda Copper Company stack Temp ( F)
Sampling Location: No. 1-2 Baghpuse InletSample Time (Min.-)
Traverse Point No. Sampled: B-8 Sample Volume (cf)
Moisture (% »2
-------
c
O
o
(£.
LLJ
NJ
o
O
<
LU
>
o
LU
10.0
?'°
8.0
7.0
6.0
5.0
3.0
2.0
1.0
°'S
0.8
0.7
0.6
0.5
0.3
0.2
0.1
No. 1-2 Baghouse Inlet
Particle Size Distribution
Run, 2
0.01 0.05 Q. I 0.2 0.5 I 2
10 20 30 40 50 60 70 80
CUMULATIVE PERCENTAGE
90
95
M 99
99.99
By Weight Less Than Diameter)
-------
Anaconda Copper Company
Butte, Montana
TABLE 21
PARTICLE SIZE DISTRIBUTION
Run: 3
Date: 10-26-79 . P. (in. Hg.) 24.Ml
oar •
Location: Anaconda Copper Company Stack Temp ( F) 73.
Sampling Location: No. 1-2 Baghouse InletSample Time (Min.) 3.0
Traverse Point No. Sampled: A-1 Sample Volume (cf) 1«6l
Moisture (% H20) 1.6
Meter Temp (°F) *»9-
Flow Setting, AH
(in. H20) °-8/*
Nozzle Diameter (in.) °-179
Sample Flow Rate (at stack conditions): 0.46cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
195.9
4.5
1.4
0.2
0.1
0.1
0.1
0.4
%
96.6
2.2
0.7
0.1
0.05
0.05
0.05
0.2
Cumulative EAD
% (Microns)
100. 13.8
3.4 8.8
1.2 5.9
0.5 4.1
0.4 2.7
0.35 1.3
0.3 0.9
0.25 0.6
Backup
Filter 0.1 0.05 0.05
TOTAL 202.8
-63-
-------
No. 1-2 Baghouse Inlet
Particle Size Distribution
Run 3
I
C
o
u
'I
*l
ec.
LU
o
LU
CJ
CC
£
O
o
cc.
LU
u.
LU
10.0
9.0
8.0
7.0
6.0
5.0
k.O
3.0
2.0
1.0
°-2
0.8
0.7
0.6
0.5
0.3
0.2
0.1
_L
0.01 0.05 O.I 0.2 0.5 I
10 20 30 40 50 60 70 80 90
CUMULATIVE PERCENTAGE
% By Weight Less Than Diameter)
95
96 98
99.1 99.9
99.99
-------
Anaconda Copper Company
Butte, Montana
TABLE 22
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: 10-25-79
Location: Anaconda Copper Company
P (in. Hg.)
Stack Temp (°F)
Traverse Point No. Sampled:B-6, A-6
Moisture (% H20)
Meter Temp (°F)
74.
Sampling Location: No. 1-2 Baghouse OutleSample Time (Min.) 60.
Sample Volume (cf) 51.95
1.9
82.
Flow Setting, AH
(in. H20) 2.1
Nozzle Diameter (in.)0.232
Sample Flow Rate (at stack conditions): 0.69cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
1.3
0.8
0.3
0.5
0.3
0.3
0.6
0.5
%
25.5
15.7
5.9
9.8
5.9
5.9
11.8
9.8
Cumulative
%
100.
74.5
58.8
52.9
43.1
37.2
31.3
19.5
EAD
(Microns)
11.5
7.2
4.8
3.4
2.2
1.1
0.66
0.45
Backup
Filter
0.5
9.7
9.7
TOTAL
5.1
-------
-99
No. 1-2 Baghouse Outlet
Particle Size Distribution
Run 1
EFFECTIVE AERODYNAMIC PARTICLE DIAMETER, microns
O O OOOOOOO— IM U> .p- VI ON «>l OOVOC
— ls» v*> .p- U1 O> -«J OOVO O O O O O O O O O C
-
/
1
1
1
f
1
•
•
..
1
*
•J
'
j
1
/
1
1 .
0.01 0.05 O.I 0.2 0.5 I
10 20 30 40 50 60 70 80 SO
CUMULATIVE PERCENTAGE
(% By Weight Less Than Diameter)
W 98
89.8 88.9
99.99
-------
Anaconda Copper Company
Butte, Montana
TABLE 23
PARTICLE SIZE DISTRIBUTION
Pbar (in. Hg.)
Stack Temp (°F)
Run: 1
Date: 10-26-79
Location: Anaconda Copper Company
Sampling Location: No. 3-4 Baghouse InletSample Time (Min.)
Traverse Point No. Sampled: X-4 Sample Volume (cf)
Moisture (% H20)
Meter Temp (°F)
Flow Setting, AH
(in. H20)
24. 44
40.
15.
12.06
1.5
74. .
1.9
Nozzle Diameter (in.) 0.227
Sample Flow Rate (at stack conditions): 0.66cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
3.3
6.4
8.1
4.6
2.2
0.7
0.7
0.8
%
11.8
22.9
29.
16.5
7.9
2.5
2.5
2.9
Cumulative
%
100.0
88.2
65.3
36.3
19.8
11.9
9.*
6.9
EAD
(Microns)
11.4
7.2
4.9
3.4
2.1
1.1
0.65
0.44
Backup
Filter
1.1
4.0
4.0
TOTAL
27.9
-67--
-------
o
u
u
oc
CO
>
o
1^
It
u.
UJ
10.0
9.0
8.0
7.0
6.0
5.0
k.O
3.0
2.0
1.0
8:1
0.7
0.6
0.5
o.k
0.3
0.2
0.1
No. 3-A Baghouse Inlet
Particle Size Distribution
Run 1
0.01 0.05 O.I 0.2 0.5 1
10
90
20 30 40 50 60 70 BO
CUMULATIVE .PERCENTAGE
(% By Weight Less Than Diameter)
95
91 99
-------
Anaconda Copper Company
Butte, Montana
TABLE 2k
PARTICLE SIZE DISTRIBUTION
Pbar (in. Hg.)
Stack Temp (°F)
Run: 2
Date: 10-26-79
Location: Anaconda Copper Company
Sampling Location: No. 3-4 Baghouse InletSample Time (Min.)
Traverse Point No. Sampled: X-6 Sample Volume (cf)
Moisture (% H20)
Meter Temp (°F)
Flow Setting, AH
(In. H20)
24.44
4o.
15.
12.25
1.5
Ik.
1.9
Nozzle Diameter (in.) 0.227
Sample Flow Rate (at stack conditions): 0.67cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg)
2.2
4.4
6.8
3.7
0.9
0.6
0.7
0.4
%
10.5
21.1
32.5
17.7
4.3
2.9
3.4
1.9
Cumulative
%
100.
89.5
68.4
35.9
18.2
13.9
11.0
7.6
EAD
(Microns)
11.4
7.9
A.9
3.4
2.1
1.1
0.65
0.44
Backup
Filter
1.2
5.7
5.7
TOTAL
20.9
-69-
-------
i
^j
o
o
u
1
A
ce.
o
I
o
o
ce.
in
>
H
o
tu
u.
u.
UJ
10.0
9.0
8.0
7.0
6.0
5.0
4.0
3.0
2.0
1.0
°'2
0.8
0.7
0.6
0.5
0.4
0.3
0.2
0.1
No. 3-*t Baghouse Inlet
Particle Size Distribution
Run 2
0.01 O.OS O.I 0.2 0.5 I 2
10 20 30 40 50 80 70 60 90
CUMULATIVE PERCENTAGE
% By Weight Less Than Diameter)
95
99 99
99.1 99.9
99.99
-------
Anaconda Copper Company
Butte, Montana
TABLE 25
PARTICLE SIZE DISTRIBUTION
Run: 3
Date: 10-26-79 P. (in. Hg.) 24.44
Location: Anaconda Copper Company Stack Temp ( F) 40.
Sampling Location: No» 3-4 Baghouse Inlet Sample Time (Min.) 15.
Traverse Point No. Sampled:Y-5 Sample Volume (cf) 12.23
Moisture (% hy)) 15.
Meter Temp (°F) 76.
Flow Setting, AH
(in. H20) 1.9
Nozzle Diameter (in.) 0.227
Sample Flow Rate (at stack conditions): 0.67cfm
Plate
No.
1
2
3
4
5
6
7
8
Net Wt.
(mg) -
3.6
5.2
7.6
2.1
1.7
0.5
0.5
0.8
%
15.5
22.4
32.8
9.1
7.3
2.2
2.2
3.5
Cumulative EAD
% (Microns)
100. 11.4
84.5 7.9
62.1 4.9
29.3 3.4
20.2 2.1
12.9 1.1
10.7 0.65
8.5 0.44
Backup
Filter 1-2 5.0 5.0
TOTAL 23.2
-71-
-------
ho
I
(A
8
u
LU
_i
o
i
o
o
en
LU
10.0
9.0
8.0
7.0
6.0
3.0
2.0
1.0
0.9
0.8
0.6
o.;
0.1
No. 3-*» Baghouse Inlet
Particle Size Distribution
Run 3
0.01 0.05 0.1 0.2 0.5 I
5 10 20 30 40 50 80 70 80
CUMULATIVE PERCENTAGE
(% By Weight Less Than Diameter)
90 95
9.9 99.9
-------
Anaconda Copper Company
Butte, Montana
TABLE 26
PARTICLE SIZE DISTRIBUTION
Run: 1
Date: 10-25-79 Pbar ^'n* Hg^ 2k'°k
Location: Anaconda Copper Company Stack Temp ( F) 52.
Sampling Location: No. 3-4 Baghouse OutleJample Time (Min.) 90.
Traverse Point No. Sampled: A-6 Sample Volume (cf) 82.72
Moisture (% H20) 0.75
Meter Temp (°F) 82.
Flow Setting, A H
(in. H20) 2.2
Nozzle Diameter (in.) 0.197
Sample Flow Rate (at stack conditions):0.75 cfm
Plate
No. -
1
2
3
4
5
6
7
8
Net Wt.
(nig)
11.3-
10.7
5.5
1.8
1.0
0.5
0.4
0.3
%
35.0
33.1
17.0
5.6
3.1
1.6
1.2
0.9
Cumulative EAD
% (Microns)
100. 11.2
65. 6.8
31.9 4.5
14.9 3.2
9.3 2.0
6.2 1.0
4.6 0.62
3.4 0.42
Backup
Filter 0.8 2.5 2.5
TOTAL '
-73-
-------
No. 3-k Baghouse Outlet
Particle Size Distribution
Run 1
EFFECTIVE AERODYNAMIC PARTICLE DIAMETER, microns
O O OOOOOOO— N> 10 £- VSl ON ^J OOVOC
— ls» V*> .f VI ON --J OOVCO O O O OOOOOC
1
J
1
f
X
/
'
X
/
^
^
s
0.01 O.OS Q.I 0.2 O.S I
10 20 30 40 50 00 70 80 90
CUMULATIVE PERCENTAGE
% By Weight Less Than .Diameter)
95
99 99
99.99
-------
Bate: October 25-26, 1979
SUM.-.ARY OF VISIBLE EMISSIONS
Table 27
Type of Plant: Copper mine
»* pe oT Discharge: Gjrlzzley chute Location of Discharge; East Grizzley
ight of Point of DJscharge; 10-20' above flr. Description of Sky; N/A
nd Direction: N/A Wind Velocity: N/A
Detached Plume:
Color of Plume: N/A
I
N/A
server No.;t
stance from'Observer to Discharge Point:
10'
Duration of Observation: 5-1/4 hours
Direction of Observer from Discharge Point: East
10' '
I
Ight of Observation Point;
scription of 'Background:
above discharge point
Grev metal
lumber
1
2
3
1|
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
SUMMARY OFAVERAGE OPACITY
Tl
Start
1630
1636
1642
16'tS
1654
1700
1706
1712
1718
1724
1742
1748
1754
1800
1806
1812
1824
1830
1836
2050
pe Opacity
End
1636
1642
1648
1654
1700
1706
1712
1718
1724
1730
1748
1754
1800
1806
1812
1818 '
1830
1836
1842
2056
Sum
0
0
80
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Average
0
0
6.7
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0 .
0
0
Set
Number
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
T
Start
2056
2102
2108
2114
2.t20
2126
2132
2138
2144
2150
2156
2202
2208
2214
2220
0040
0046
0052
0058
0104
me
End
2102
2108
2114
2120
2126
2132
2138
2144
2150
2156
2202
2208
2214
2220
2226
0046
0052
0058
0104
0110
Opa
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
'•o
0
0
pity
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0 i
0
0
0
Iketch Showing How Opacity Varied with Time:
8
pacity
)
c-
1
— ----••--••-- •- " • -
'
1 hr 2 hrs 3 hrs 4 h'rs
Time, Hours
-75-
-------
Date: October 25-26, 1979
SUMMARY OF VISIBLE EMISSIONS
Table 2? (contd)
Type of Plant: Copper mine
Type oT DTTcnotge; ITrizzley chute Location of Discharge; East qrizzley
Height of Point of Discharge: 10-20' above fit-Description of Sky; N/A
Wind Direction: N/A Wind Velocity: N/A
Detached Plume:
Color of Plume: N/A
Observer No.; N/A
Distance from'Observer to Discharge Point:
Direction of Observer from Discharge Point: ^__
Height of Observation Point; 10' above discharge potnt
Description of'Background: Grey metal walls
N/A
Duration of Observation: 5-1/4 hours
10'
East
Set
Number
1
2
3
k
5
6
7
8
9
10
11
12
13
U
15
16
17
18
19
20
SUMMARY OFAVERAGE OPACITY
Tl
Start
0110
0116
0122
0128
0134
0140
0146
0152
0158
0204
0210
0216
0222
me
End
0116
0122
0128
0134
0140
0146
0152
0158
0204
0210
0216
0222
0228
OP
Sum
0
0
30
0
0
0
0
0
0
0
0
0
0
petty
Average
0
0
1.5
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
me
End
Opa
Sum
pity
Average
Sketch Showing How.Opacity Varied with Time:
8
Opacity
)
c-
6
W - __ . _ .
4 •
2
n
1 hr 2 hrs 3 hrs
4 hrs
Time, Hours
-76-
-------
SUMMARY
flfi e: October 25-26,. 1979__
Type oT Dischai ye: Grtzzl'ey chute
OF VISIBLE
Table 28
Type
EMISSIONS
of Plant: Copper mine
|ight of Point of Discharge:
id Direction: N/A
Color of Plume:
No.
N/A
« server No.: N/A
stance from'Observer to Discharge Point:
Direction of Observer from Discharge Point:
Height of Observation Point; 5' above discharge point
Inscription of'Background: Grey metal walls
Location of Discharge; Grizzley west
1Q-2Q1 above fit-Description of Sky:
Wind Velocity:
Detached Plume:
Duration of Observation:
30*
N/A
N/A
4 hours
East
Set
umber
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
SUMMARY OFAVERAGE OPACITY
Tl
Start
1656
1702
1708
1721
1741
1747
1753
1759
1805
1822
1830
2106 .
2112
2118
2124
2130
2136
2142
2148
2154
me
End
1702
1708
1714
1727
1747
1753
1759
1805
1811
1828
1836
2112
. 2118
2124
2130
2136
2142
2148
2154
2200
Op
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
pclty
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
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
T
Start
2200
2206
2212
2218
0040
0046
0052
0058
0104
0115
0121
0127
0139
0153
0159
0205
0211
0217
0223
0229
me
End
2206
2212
2218
2224
0046
0052
0058
0104
0110
0121
0127
0133
0145
0159
0205
0211
0217
0223
0229
0235
Opa
Sum
0
0
0
0
0
0
0
0
0
105
95
45
0
0
0
0
0
0
0
0
pity
Average
0
0
0
0
0
0
0
0
0
4.4
4.5
1.9
0 .
0
0
0
0
0
0
0
•Ketch Showing How Opacity Varied with Time:
Opacity
8
.6
c-
Ihc
2 hr
hr
Time, Hours
4 hr
-77-
-------
SUMMARY
October 25-26, 1979
OF VISIBLE
Table 29
Type
Discharge: Process hood
Grbund level
Brown
Date:
Type oT
Height of Point of Discharge:
Wind Direction:
Color of Plume:
Observer No. : N/A _ _ _
Distance from1 Observer to Discharge Point: _
Direction of Observer from Discharge PointCast
Height of Observation Point; Ground level
Description of 'Background:
EMISSIONS
of Plant: Copper mine
Location of Discharge:
Description of Sky:
Wind Velocity:
Detached Plume:"
Crusher hood
N/A
N/A
Duration of Observation;Approximately 4-1/2 homts
Indoors
Set
Number
1
2
3
k
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
SUMMARY OF- AVER AGE OPACITY
Tl
Start
1645
1651
1657
1703
1709
1720
1726
1745
1751
1757
1803
1809
1821
1827
1833
2050
2056
2102
2108
2114
me . Op
End
1651
1657
1703
1709
1715
1726
1732
1751
1757
1803
1809
1815
1827
1833
1839
2056
2102
2108
2114
2120
Sum
135
10
110
30
55
25
30
40.
4a
5
0
15
65
40
60
15
20
10
10
80
pclty
Average
5.6
0.4
4.6
1.3
2.3
1.0
1.9
1.7
1.7
0.2
0
0.6
2.7
1.7
2.5
0.6
0.8
0.4 .
0.4
3.3
Set
Number
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
T
Start
2120
2126
2132
2138
2144
2150
2156
2202
2208
2214
2220
0036
0042
0048
0054
0111
0147
0153
0159
0205
me
End
2126
2132
2138
2144
2150
2156
2202
2208
2214
,2220
2226
0042
0048
0054
0100
0117
0153
0159
0205
0211
Opa
Sum
45
15
5
20
40
80
25
300
110
55
0
5
45
30
0
195
20
5
40
15
pity
Averagei
1.9
0.6
0.2 !
0.8
1.7
3.3
1.0
12.5 i
4.6
2.3
0
0.2
1.9
1.3
0
8.1
0.8
0.2
1.7
0.6
Sketch Showing How.Opacity Varied with Time:
12
k hrc
Time, Hours
-78-
-------
October 25-26. 1979
Process hood
(Jate: _^
Tvpe oT~Discharge:
• ight of Point of Discharge: Ground level
Wnd Direction: H/A
Color of Plume:
f server No.:
«
SUMMARY OF VISIBLE EMISSIONS
Table 29 (contd)
Type of Plant:
.„•• Location of D
Copper mine
Brown
Description of Sky:_
Wind Velocity: N/A
Detached Plume: M/A
N/A
(stance from'Observer to Discharge Point; 5'
Duration of Observation: Approximately 4-1/2 Knur*
Direction of Observer from Discharge Point: East
tight of Observation Point; Ground level
scrlption of 'Background: Indoors
Set
lumber
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
SUMMARY OFAVERAGE OPACITY
Tt
Start
0211
0217
0223
0229
me
End
0217
0223
0229
0235
Opacity
Sum
0
0
5
45
Average
0
0
0.2
2.3
Set
Number
21
22
23
2k
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
T
Start
me
End
Opa
Sum
pity
Average
j
\
Wcetch Showing How-Opacity Varied with Time:
)pacity
(*)
c-
12
— 9r
6
3
11
hr
2
hrs
3 hrs
4'
hrs
Time, Hours
-79-
-------
-te: October 25, 1979
rype oT Dischar g e:~~5ta,c!c
Sur.MARY OF VISIBLE EMISSIONS
Table 30
Type of Plant:
Copper mine
Height of Point of Discharge: 15* above roof
Wind Direction: S.E.
Color of Plume: Gray
Observer No.:
Location of Discharge: NO. 1-2'baghouse out Tat
Description of Sky; N/A
Wind Velocity: 10-30
Detached Plume:
N/A
fT/A
Distance from'Observer to Discharge Point; 50'
Duration of Observation: 1-1/2 hours
Direction of Observer from Discharge Point: South-west of stack
Height of Observation Point; Level with lip of stack
Description of'Background:
Multicolored mine wall
SUMMARY OF AVERAGE OPACITY
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time . Opacity
Start
1630
1636
1642
1648
1654
1700
1706
1712
1718
1724
1730
1736
1742
1748
1754
End
1636
1642
1648
1654
1700
1706
1712
1718
1724
1730
1736
1742
1748
1754
1800
Sum
0
10
0
10
10
0
15
0
10
0
0
0
10
0
15
Average
0
0.4
0
. 0.4
0.4
Q
0.6
Q
0.4
0
0
0
0.4
o
0.6
Set
Number
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
T
Start
me
End
Opa
Sum
pity
Averagei
j
i
1
Opaci ty
Sketch Showing How Opacity Varied with Time:
0.8.:
0.6_
0.4_
0.2_
1 hr
Time, Hours
-80-
-------
SUMMARY
N/A
White
D~t e : October 26, 19.79
T^pe of Discharge; Open dump pits
Might of Point of Discharge:
Vm>d Direction: N.W.
Color of Plume:
terver No. :
tance from 'Observer to Discharge Point:
Direction of Observer from Discharge Point:
Might of Observation Point: 10' above pits
Inscription of 'Background: Ground
OF VISIBLE
Table 31
Type
EMISSIONS
of Plant: Copper mine
Location of Discharge; Truck dump area
Description of Sky; Partly cloudy
Wind Velocity: 15-30 mph
Detached Plume: No
Duration of Observation:Approximately 3 hours
20'
North-east
SUMMARY OFAVERAGE OPACITY
Set
, lumber
1
2
3
*»
5
6
7
8
9
10
11
12
13
U
15
16
17
18
19
20
• •
Tl
Start
1450
1^56
1502
1508
1514
1520
1526
1532
1538
1615
1621
1627
1633
1639,
1645
1651
1657
1703
1709
1715
rne Op
End
1456
1502
1508
1514
1520
1526
1532
1538
1544
1621
1627
1633
1639.
1645
1651
1657
1703
1709
1715
1721
Sum
25
80
70
55
20
45
30
95
100
0
25
80
30
35
0
25
Q
155
0
55
pclty
Average
1.0
3.3
2.9
- 2.3
0.8
1.9
1.3 -
4.0
4.2
0
1.0
3.3
1.3
1.5
0
1.0
0
6.5 .
0
2.3
Set
Number
21
22
23
2k
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
T
Start
1721
1727
1733
1739
1745
1751
1757
1803
1809
me
End
1727
1733
1739
1745
1751
1757
- 1803
1809
1815
Opa
Sum
15
30
10
80
75
15
25
15
65
pity
Average
0.6
1.3
0.,4
3.3
3.1
0.6
1.0
0.6
2.7
Opaci
Showing How-Opacity Varied with Time:
4
ty
~~~
Time, Hours
-81-
-------
SUMMARY OF VISIBLE EMISSIONS
Date: October 26, 1979
Type oT Discharge: Stack
Table 32
Type of Plant:
Copper mine
Location of Discharge;3?4 baghouse outlet
Description of Sky;Partly cloudy - cloudy
Wind Velocity: 20-~30 mph
Detached Plume:
No
Height of Pojnt of Discharge: 15* above roof
Wind Direction: South
Color of Plume: Gray '
Observer No.: N/A ~ Duration of Observation Approximately 2-1/4 hours
Distance from'Observer to Discharge Point: 100'-150'
Direction of Observer from Discharge Polnt;1^st of stack
Height of Observation Point; Level with Up ot stack
Description of'Background:
colored mine wall
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
SUMMARY OFAVERAGE OPACITY
Tl
Start
1445
1451
J457
1503
1509
1515
1521
1527
1533
1539
1619
1625
1726
1732
1738
1744
1802
1808
!8t4
1820
me . Op
End
1451
1457
1503
1509
1515
1521
•1527
1533
1539
1545
1625
1631
1732
1738
1744
1750
1808
1814
182Q
1826
Sum
0
15
30
0
20
0
65
55
0
80
25
110
20
5
95
10
0
40,
a
95
aclty
Average
0
0.6
1.3
. 0
0.8
0
2.7
2.3
0
3.3
1.0
4.6
0.8
0.2
4.0
0.4
0
1.7 .
0
4.0
Set
Number
21
22
23
2k
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
T
Start
1826
1832
me
End
1832
1838
Opa
Sum
30
10
pity
Average
1.3
0.5
-
Sketch Showing How-Opacity Varied with Time:
Opacity
(*)
, ..
2
1 .
, r
.
— — - - -
n
— -
rr
—
4J
L~T_
•
' — r
L, .
1 hr
hrc
Time, Hours
-82-
-------
SU.",.",ARY
ria"te:
October 26, 1979
OF VISIBLE
Table 33
Type
EMISSIONS
of Plant: Copper mine
** e of Discharge-.'Conveyor dtsrhargp. *n ..^,.1,, Location of Discharge:
ght of Point of Discharge: 80' PrT^ Description of Sky: Q,
I
WTnd Direction:
Color of Plume:
1 server No.
stance
Coarse ore stockpile
QVPrra«;f
S.W.
White-Grey
N/A
from'Observer
to Discharge Point:
Direction of Observer from Discharge Point:
Hjlght of Observation Point; 65'
Inscription of 'Background:
Wind Velocity: 10-15
Detached Plume: N£
Duration of Observation:
150'
3 h.otirs.
West
Nearby mountain
Set
umber
1
2
3
4
6
8
9
10
11
12
13
14
15
16
17
18
19
20
SUMMARY OFAVERAGE OPACITY
Tl
Start
1400
1406
1412
1426
1432
1438
1450
1456
1502
1515
1521
1527
1533
1539.
1545
155T
1557
1603
1609
1630
me Op
End
1406
1412.
1418
1432
1438
1444
1456
1502
1508
1521
1527
1533
1539
1545
1551
1557
1603
1609
1615
1636
Sum
55
145
140
145
125
130
135
280
265
200
165
145
140
150
400
330
305
270
355
160
pcity
Average
2.3
6.0
5.8
6.0
5.2
5.4
5.6
11.7
11.0
8.3 -
6.9
6.0
5.8
6.3
16.7
13.8
12.7
11.3
14.8
6.7
Set
Number
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
T
Start
1636
1642
1648
1654
1700
1706
1712
1718
1724
me
End
1642
1648
1654
1700
1706
1712
1718
1724
1730
Opa
Sum
150
165
145
155
310
350
305
255
250
pity
Average
6.3
6.0
6.5
12.9
14.6
12.7
10.6
10.4
Sketch Showing How-Opacity Varied with Time:
Opacity
20
15"-
2 hrs
3 hrs
Time, Hours
-83-
-------
SUMMARY OF
October 26, 1979 Tal
Date: . .
Type of Discharge: Conveyor belt discharge
Height of Point of Discharge: 85'
Wind Direction: N/A
Color of Plume: N/M
Observer No. : N/rA
Distance from Observer to Discharge Point:
Direction of Observer from Discharge Point:
Height of Observation Point: 85'
VISIBLE EMISSIONS
>le 34
Type of Plant: Copper mine
Location of Discharge: Coarse ore transfer pofn
Description of Sky: N/A
Wind Velocity: N/A
Detached Plume: N/A
Duration of Observation: 3 hours
15'
t
—
Description of Background: Indoors
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
1850
1856
1-902 ~
1908
1914
1920
1926
19.32
3938
J9.44
20QO.
2006
2012
2018
2024
2030
2036
2042
2048
2054
me
End
1856
1902
1908
1914
1920
1926
1932
1938
1944
1950
2006
2012
2018
2024
2030
2036
2042
. 2048
2054
2100
Opacity
Sum
0
0
0
0
0
0
0
0
Q
0
Q
0
0
0
0
0
0
0
0
0
Average
0
0
0
0
0
0
0
Q
0
0
0
0
0 '
0
0
0
0
0
0
0
Set
Number
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
T
Start
2120
2126
2132
2138
2144
2150
2156
2202
2208
2214
me
End
2126
2132
2138
2144
2150
2156
2202
2208
2214
2220
Opa
Sum
0
0
0
a
0
0
0
0
0
0
pity
Average
0
0
0
0
0
0
0
o
0
0
M-
Opaci ty
Sketch Showing How Opacity Varied with Time:
8
6
4
2
0
1 hr
2 hrs
3 hrs
Time, Hours
-8k-
-------
Table 35
Mean Fugitive Emission Values
Mean fugitive emission values (% frequency emission) for three tests
at each location are presented. Values are given for each observer.
Test 1
Test 2
Test 3
Site Mean
Test 1
Test 2
Test 3
Site Mean
Test 1
Test 2
Test 3
Site Mean
Test 1
Test 2
Site Mean
Crusher Grizzley East
Observer 1
0.0
0.0
0,29
0.09
Crusher Grizzley West
Observer 1
0.42
0.0
4.06
1.49
Crusher Hood Area
Observer 1
21.34
31.73
15.59
22.39
Observer 1
0.0
0.0
0.0
Fine Ore Feeder*
Test Mean
0.0
0.0
0.29
0.09
Test Mean
0.42
0.0
4.06
1 .49
Test Mean
21.34
31.73
15.59
22.39
Test Mean
0.0
0.0
0.0
•Illumination = 4 foot-candles. Ten foot-candles is the level con-
sidered necessary for proper application of the method.
-85-
-------
Table 35
(cont inued)
Truck Dumping Area
Test 1
.Test 2
Test 3
Site Mean
Test 1
Test 2
Test 3
Site Mean
Test 1
Test 2
Test 3
Site Mean
Observer 1
15.44
10.75
15.42
16.54
Coarse Ore Stockpile
Observer 1
38.14
100.00
100.00
96.05
Coarse Ore Transfer Point
Observer 1
0.0
0.0
0.0
0.0
Test Mean
13.75
15.42
16.54
Test Mean
83.14
100.00
100.00
.96.05
Test Mean
0.0
0.0
0.0
0.0
-86-
-------
Appendix A
Raw Test Data
-------
TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
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.
tO
M^
SaEMATIC OF SAMPLING LOCATION *? T*
•3
J* • ' 1 I •*•
~»« •' "I . M . .
TRAVERSE
POINT
NUMBER
/
2
3
1 t
^
6
7
FRACTION
OF STACK 1.0.
,0pf
,oyv
.o75
^ / 0 ^F
/ ^J t
.It?
*'2fy(0
^ .331
^ . 6/?
li
13
i ^L
)£
/ *O
17
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• d JF
^Tf X ^^
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2.H
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M^tna.
c,.o>c.
T-S52.
^ M*T2.
yz.-iZH
^%*\1«o
2.2,51*
•Z.H -M-4 8
ZS^SM
x1.3i?
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2.9-6
30.5^3-
38 . 5S2.
3.?
DISTANCE B
3V
/
*
i
so^
' ^.l'
i -
' q ^.
-', -
?«.*
? . ft
/
TRAVERSE POINT LOCA' ION
FROM OUTSIDE OF PORT
(SUM OF COLUMNS 4 & 5)
V
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„• A-1
-------
PRELIMINARY VELOCITY TRAVERSE
PLANT
DATE.
LOCATION
STACK I.D. *2**
BAROMETRIC PRESSURE, in. Hg
STACK GAUGE PRESSURE, in. HT0 *"/
OPERATORS
SCHEMATIC OF TRAVERSE POINT LAYOUT
TRAVERSE
POINT .
NUMBER
6
f
(7
AVERAGE
VELOCITY
HEAD
Ups), in.H20
AS
(.123^
STACK '
TEMPERATURE
(Ts), °F
79
TRAVERSE
POINT
NUMBER
1
-a.
3
^
S
. 6
7
^f
9
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//
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^3
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i5T
M
17
<^
AVERAGE
VELOCITY
HEAD
(Aps), in.H20
.75
J2-
43
M
M
At
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1.1
t.z
1.2$
/**
A^
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f.a36
STACK
TEMPERATURE
(Ts). °F
77'
1C
K
76
76
K
7$
75
TS
75 .
75
-75 .,- •
75
IS
ii
t$
TS
H5
11°
A-2
-------
NOMOGRAPH DATA
PLANT
DATE
SAMPLING LOCATION
CONTROL BOX HO. A/UTgCW **£
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE 1 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
^Hfa
T(navg.
Bwo
Pm
ps
P7
A-3
-------
.°F
DRY GAS METER
TEMPERATURE
INLET
(T«Jn).°F
OUTLET
PUMP
VACUUM.
in. HI
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE,
^57. /
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7.5
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1.5
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1.6
w-
7-5
ifc,
1'£9*0
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.250
IB
.96
'•35
/•35
77
-------
-------
FIELD DATA
PLANT
DATE
PROBE LENGTH
NOZZLE I.D._f
-4t
SAMPLING LOCATION
SAMPLE TVPE
RUN NUMBER
OPERATOR
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE.
FILTER NUMBER Is)
ASSUMED MOISTURE. %
SAMPLE BOX NUMBER.
METER BOX NUMBER.
METER AH~ L
CFACTOR
PI TOT TUIE FACTOR _
REFERENCE Ap l.3>7
MOTE
READ AND RECORD ALL DATA PVEBY 2. >5 MINUTES
TRAVERSE
POINT
NUMBER
GAS KTER READING
VELOCITY
HEAD
(Apsl. in. HjO
ORIFICE PRESSURE
DIFFERENTIAL '
(AH), in. HjO)
DESIRED ACTUAL
STACK
TEMPERATURE
-------
TRAVERSE
POINT
NUMBER
/
-^
^
4
5
(,
7
8
Q
to
ti
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tk
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TIME, mm ^^
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lApsi in HjO
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7.5
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= "4 A/3 \ „
ORIFICE PRESSURE
DIFFERENTIAL
IAH). in H^Oi
DESIRED
1.65
/«fo5
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1*8
2..Q
/*&£
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ACTUAL
1-55
1-ts
(•t
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2.*t>
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3L-I
2-0
/fr
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75~
76
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73
75
05
73
7(3*^^1 •
DRY GAS METER
TEMPERATURE
INLET
'T-",n'-OF
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6f*-{
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0.9975:
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74.2635923
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FIELD DATA
PLANT All/AfQ/dOA CoPPtP-
DATE. •=*-' - ""'-
SAMPLING LOCATION _&i
SAMPLE TYPE.
RUN NUMBER _3 U JL
OPERATOR.
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P,l
FILTER NUMBER Is) -^
PROBE LENGTH MD TV
NOZZLE ID. .//%
ASSUMED MOISTURE. 1
SAMPLE BOX NUMBER
METER BOX NUMBER.
METER AH^_
CFACTOR
l.l£
PI TOT TUBE FACTOR.
REFERENCE A p ' »
NOTE
5*7
±; .010
READ AND RECORD ALL DATA FVFRY
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
' - ^
VELOCITY
HEAD
(Aps). in. H^
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. Hl
DESIRED
ACTUAL
STACK
TEMPERATURE
rr,».°F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM,
in. HI
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
610* $
AC
3-5"
#
7.5"
l-f
-
OO
73
u-s
- 6
2-1
if
)&.
IS
1 .
2*2-
w
26
7.°
7--0
70
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I
2-0
2-0
y-s
0.0
v-v
/O.o
643.4
/.C
. Y
/-V
ic_
--^:
-------
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
'V »
3
VELOCITY
HEAD
626';
24. 04'
- •"•
&*
''s
-
28. 97'
5 Clot
. -J O •.
9o
r.
55
'M.
2-0
'.vv-'-^" '.; -90J:
:/:^;:r-. " -i. 7i
'^X'/4v'' O.'i&Sf
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• 28.90356847:
7: -* 23. 915'
V.-?73-'94204832i
•r24777. 98039s
-^•58.'57169647,
•;••19627. 37549'
! 101.583391
^06.81193461!
:Up-'4599^595;
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FHWT
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;:FHGR
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-------
TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
PLANT STXJ0CWP& LrD / ' **~
DATE /0-2.<4~~lcl
SAMPLING i nr.annN 'C £V-£ ft e*«- At-o^)iS
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 '
4/'/z.
3'/2.
^9e> ii •/
4'
NEAREST DOWNSTREAM DISTURBANCE 4'
CALCULATOR OfJU^**A~
SCHEMATIC OF SAMPLING LOCATION
TRAVERSE
POINT
NUMBER
FRACTION
OF STACK 1.0.
STACK I.D.
PRODUCT OF
COLUMNS 2 AND I
(TO NEAREST 1 8 INCH)
DISTANCE B
TRAVERSE POINT LOCATION
FROM OUTSIDE OF PORT
(SUM OF COLUMNS 4 & 5)
t-
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2 '/*
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7^2.
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if 'A
K
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27 •
If
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/b
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21
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30
31
32.75'
£L
£45.
f*.
-1-1''
A-10
-------
PRELIMINARY VELOCITY TRAVERSE
PLANT
DATE
LOCATION
STACK I.D.
BAROMETRIC PRESSURE, in. Hg
STACK GAUGE PRESSURE, in.
OPERATORS
TRAVERSE
POINT
NUMBER
X- 1
2
3
f
£
7
#
r
/a
//
/^-,
/?
/if
/5
/^
17
1%
n
^>
A
2Z
V
14
AVERAGE
VELOCITY
HEAD
Ups), in.H20
.45
,$(*
,5
. &3 Li
.64
.£4
..64'
, >3
.'TO
.*f
,45
^6
.ffc
' 4b
At)
*L
.«
-------
NOMOGRAPH DATA
PLANT /Xy;
DATE
^4
SAMPLING LOCATION
CONTROL BOX MO. stJ!/)£f<4 >
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
ORIFICE, in. H20
AVERAGE METER TEMPERATURE ( AMBIENT + 20 °F).°F
PERCENT MOISTURE IN GAS STREAM BY VOLUME
BAROMETRIC PRESSURE AT METER, in Hg
STATIC PRESSURE IN STACK, in. Hg
(Pm±0.073 x STACK GAUGE PRESSURE in in. H20)
RATIO OF STATIC PRESSURE TO METER PRESSURE
AVERAGE STACK TEMPERATURE, °F
AVERAGE VELOCITY HEAD. in. H20
MAXIMUM VELOCITY HEAD. in. H20
C FACTOR
CALCULATED NOZZLE DIAMETER, in.
ACTUAL NOZZLE DIAMETER, in.
REFERENCE ^p. in. H20
^Hrg
mavg.
Bwo
PR,
ps
•^
sa»g.
•>Pavg.
APmax.
/•'>
. 3"
.
-------
FIELD DATA
PLANT
SAMPLING LOCATION.
SAMPLE TYPE ^
RUN NUMBER
OPERATOR X7^
PROBE LENGTH AND TYPE
NOZZLE I.D
/?-'•
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE. (Pf( i
FILTER NUMBER (s)
ASSUMED MOISTURE. I
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AH,
C FACTOR
PI TOT TUBE FACTOR
REFERENCE A p L
NOTE
'*-
READ AND RECORD ALL DATA EVERY
MINUTES
TRAVERSE
POINT
NUMBER
i
VjJ
Xcf
CLOCK TIME
sf,
3ej
mi
3tS
-to
GAS METER READING
(Vml. It3
52.
(?(*,&&?>
VELOCITY
HEAD
(AP). in. H0
70
,70
.-70
.10
t-?0
.-70
*
.(oO
ORIFICE PRESSURE
DIFFERENTIAL
(AMI. in H20)
DESIRED
,/*
^^
ACTUAL
A/s
2.
STACK
TEMPERATURE
(T$)."F
7-Z-
7V-
7V
74
Z5L
7
7f
it
DRY GAS METER
TEMPERATURE
INLET
ff.taf.-F
£
OUTLET
PUMP
VACUUM.
in. H|
7
/4
"(<
' \ '
D. softer
2.4265
75.417
95. 23
. 90. 07
, . '24..04:
-2.',
18. .
28. 97
' 96.
-1. 7'
0^238
. :0.9994
0. 846
• ". . 16. ,
28883519'!
, U.75456
%.. 077275021
28;85182293
23. 9.15
28491402'
24234.57817:
.39.'98847273'
'18896. 46861'
36923518
r.i.r i
x..H
TS<
TIT;
. 'VMfl,
!PpflRv
• vwe
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-------
-------
FIELD DATA
PLANT.
OATE_
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER . ?
OPERATOR f':V-/-'--.-v-'
PROBE LENGTH AND TYPE.
NOZZLE I.D. --?*,«
•>=f/£•;.' -V
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE. (P,)_
FILTER NUMBER (s)
74°
ASSUMED MOISTURE. %
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AH*.
C FACTOR_
/. ft
PI TOT TUBE FACTOR
REFERENCE Ap
NOTE
1 A-
READ AND RECORD ALL DATA EVERY
MINUTES
- .01
TRAVERSE
POINT
NUMBER
SAMPLING
TIME, mm
CLOCK TIME
sCLOCKI
GAS METER READING
(Vl. It3
VELOCITY
HEAD
-72.
24,
t<(5
*
73
252)
3fe
3.
71
(GD
t!
9.3W)
70
/OfD
0
10.
ILS
&
76
~3£.
+<>
2
/&>
?.x>
10o
/ffD
w
3F-
ifr
t&o
12,0
/2.0
-------
SAMPLE BOX ~T IMPINGER I
-------
FIELD DATA
PLANT
DATE
SAMPLING LOCATION
SAMPLE TYPE >^
RUN NUMBER
OPERATOR {Tc
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE. (Ps)_
FILTER NUMBER (s) _ _
PROBE LENGTH AND TYPE
NOZZLE I.D. • <5>
ASSUMED MOISTURE. %
SAMPLE BOX NUMBER.
METER BOX NUMBER.
METER AHa *
CFACTOR
s./f
PI TOT TUBE FACTOR
REFERENCE Ap .
NOTE
READ AND RECORD ALL DATA EVERY
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
•- K3
VELOCITY
HEAD
(APS). in. H^O
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20|
DESIRED ACTUAL
STACK
TEMPERATURE
(TS).°F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in. HI
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
.J5o
67
,53"
2^
2<&
(06
. ten
(,1
M
3.50
(07
33-
1^
(s?
31
(ob
(,7
7*5
4ft
j.ft
.0
Ztd
-------
VELOCITY
HEM)
lApsi in HJ)
ORIFICE PRESSURE
DIFFERENTIAL
(AH). 10 HjO)
DRY GAS METER
TEMPERATURE
IMPINGER
TEMPERATURE
DESIRED ACTUAL
0. 81,108
429
64. 29
83.
90.
TS
TM
VMfl
PBflR
VI... 1C
I...ISG
U. 230
0.9994
0. 846
is;-
70.90678619
0.84902
1. 183207388
>9881679261
28.84020215
23.92235294
51.13686068
QflCT j
VSTD i
7. .59559
.92940054
4.6136
- 0.
004093952
5.4821266
FHWT
T WT
FHGR
FHLB
-------
TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
PLANT fynet/VfttOja. ( ^naA&r
DATE . /O
SAMPLING LOCA
INSIDE OF FAR 1
OUTSIDE 0
INSIDE OF NEAR
OUTSIDE 0
STACK I.D.. iDIS
NEAREST UPSTF
NEAREST DOWNS
CALCULATOR
*•— i*y* T^I " v
TION Olr\j^V\pr> la&«*W
IfALL TO
F PORT. (DISTANCE A)
WALL TO
F PORT. (DISTANCE B)
TANCE A • DISTANCE B
!EAM DISTURBANCE
JREAM DISTURBANCE
-"*/ —
_ 3 ^ji j
a*A^^ ^tl^T'
XV" . -rs-J
3 /V " ,
*J f ' r-i ' '
^"""\ V V "^ S*^ ! /
1 5^<^ A / t? ^T-v
f
1
/
/I - 3i^
TRAVERSE
POINT
NUMBER
#-J> |
3_
3
! *%
^t> "^
1 1~ y&
/i ' O
/ 7%
.2 ^/
3% y&
\ s y$
^ 3 7 /?
/o _¥ y %
//
/«5
• V5 7g
,^^^PN f^}
STACK I.D.
f3"
, ...
'
PRODUCT OF
COLUMNS 2 AND 3
(TO NEAREST 1 8 INCH)
•
SCHEI
'•<:/ ^
VIATIC OF SAMPLING LOCATION
DISTANCE B
1%
-------
PRELIMINARY VELOCITY TRAVERSE
PLANT n n^coc^o^ £epp£,r
DATE 1^-3.4-79 ''
LOCATION k<»V- bACjWkJS <2_ T«4
STACK I.D.
BAROMETRIC PRESSURE, in Hg
STACK GAUGE PRESSURE, in. H,0
OPERATORS
<.
TRAVERSE
POINT
NUMBER
fi '
-5
/
s •
6,
7
^
?
i^>
//
il
;
D- /
a
^^
V
£
6»
-)
^
0
/D
1^
/c
AVERAGE
VELOCITY
HEAD
Ups), in.H20
.f<
M^
/^?
5
. 2?
,
.75"
^ 5*
. 7
•7
' 7b
7^>
7^
~>-3
7 'SL.
7^
7
-------
NOMOGRAPH DATA
PLANT
DATE._
n"A
SAMPLING LOCATION
CONTROL BOX MO.
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
^
mavg.
Bwo
Pm
PS
P'P.
savg.
Apavg.
APmax.
A/2
• nt
,i
i.f
1.1
-75-°
&
••' i
1
13°
.ial
'/.?
\
> (tf?
A-21
-------
P.*MT
DATE
SAMPLING LOCATION g
SAMPLE TYPE R.f4.
RUN NUMBER I
OPERATOR
A.xU i> U -> « -
,
* ' *-T
PROBE LENGTH AND TVPf 7 <=3
NOZZLE I.D. .11*?
ft\
l (\c
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P ) _
FILTER NUMBER Is)
y
'
34
A-
ASSUMED MOISTURE. % •
SAMPLE BOX NUMBER ' "
METER BOX NUMBER / 3 Oj>"
METER 4Hfc__L_X_ZZ__
CFACTOR /« I JL-
PITOT TUBE FACTOR
REFERENCE A p_lu
NOTE
READ AND RECORD ALL DATA EVERY
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(VJ.lt3
VELOCITY
HEAD
(Aps). in. H^
ORIFICE PRESSURE
DIFFERENTIAL
(&H). iii. HjO)
DESIRED ACTUAL
STACK
TEMPERATURE
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in. H|
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
O
,5V
73
ro
ro
fr.n./ . s? i D
£
.2.
^4?-
4L
m
/. r^» ^ -CO
. 7 .
7O
S
7O
=?
•70
y
^/j.^Q
A
•
^LQ.
Jb U .
***
-------
TRAVERSE
POINT
NUMBER
J+
i
i
*/
•r
T
TIME mm
GAS METER READING
lVmi. II3
f ^ -^ -^
p
a / .' T ^ o
51 -s , 1 o O
1 0
a .
7.
C* ^ •
VELOCITY
HEAD
i4p$i. in HjO
14-
, 7
-5"
, 35
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in HjOl
DESIRED
LlL
,-?
ACTUAL
STACK
TEMPERATURE
lT,t.°F
7ts
-^3-
l£-
•7
7
7
DRY GAS METER
TEMPERATURE
INLET OUTLET
76
7?
7?
77
74?
PUMP
VACUUM.
in H|
0. 76987
• . 0.7329
75.1
. . . 78. 5
48.59
- - 24/04-
- ' 4.!
.10.7
• 28. 97
' 28.166
'*',".• ' ''96.;
... -2.5
o; 179:
"1.0317
.0.848
14.7
58151615
0,692785
720166409
983359
78129774
:;23. 85617647
,49. 27089325
\83265. 83876
-''38. 09707402
"64382.53121 -
;i-r03« 2147991
7. 1942"
'o.;
80486715
; '1547. 861528 '
* 0.
.
1 TM
V-Mfl'
.pBflR.
. VUC
; I..JSG
' . MWD
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Y
CP
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PS
'VflCT
QflCT
VSTD
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-------
FIELD DATA
PLAMT
DATE t j-> - .3 'S - 'I 9
SAMPLE TYPE *
RUN NUMBER £L
OPERATOR '
PROBE LENGTH AND TYPE "7
NOZZLE I.D.___JL7 "
a°/o
»- 0%c <•> * >
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE. (P )_
FILTER NUMBER Is) 2
ASSUMED MOISTURE. %
SAMPLE BOX NUMBER.
METER BOX NUMBER f 3Q gT
METER AHg l>*f
C FACTOR I, I X
PI TOT TUBE FACTOR
REFERENCE Ap <, S"
NOTE .
kC
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
w.
CLOCK TIME
GAS METER READING
(V.t. II3
VELOCITY
HEAD
vv
.O
to
• "7 f
II
.5
MJ-
5" O (o 5" O
-2
t) v
0
s ~i 0
J_L
k
a
^1
^Oi
,44-
-iD
iO
JXL
4r3~-
-4>-
-------
TRAVERSE
POINT
NUMBER
ro
i
CLOCK TIME
GAS METER READING
lVmi. II3
9 .'
fa 77 t /1
f/S *^». **~n l 1C. J
, - &j.~j'i/ ' in HjO
77
.9
w
O
-/
70
ORIFICE PRESSURE
DIFFERENTIAL
IAH). is HjOi
DESIRED ACTUAL
«, OS'
STACK
TEMPERATURE
(Tsi°F
II
4Z3-
-
7f
7/
'
/
za.
_7_0_
70
^-t-
7JL-
DRY GAS METER
TEMPERATURE
INLET
"-'•*
-J-2-
o
3Q.
'//*
OUTLET
•ro
7/
PUMP
VACUUM
m H|
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE
MA»v—*-^
• p. ss-^c
: 0.8469
. :72. 146;
. 71.25
• 52.123
/'• 24.04
4..
': ,!io.i'
28.97
•. 28. 166
^; ../. 96.
'\ 0.179,
-A 1.0317
^ p. 848
14. 1
05392615-
: .0.664495
/I.519942812
•r. 9848005719
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^23.84147059
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,'88953. 75557
'!40. 98352212
51305
L.3625424
7.3215
TS
TM
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PBflR
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VMUD
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STflT .
TH2D
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vws
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MUS
-------
PLANT
/?/w
FIELD DATA
DATE / £> -~3yr y?
SAMPLING LOCAT
SAMPLE TYPE
IWK NUMBER
.OPERATOR
PROBE LENGTH AND TYPE
NOZZLE 1.0.
ASSUMED MOISTURE. \
SAMPLE BOX NUMBER
METER BOX NUMBE
METER AH*
C FACTOR
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
PI TOT TOiE FACTOR
REFERENCE Ap
NOTE
STATIC PRESSURE. (P )
FILTER NUMBER is) -3
READ AND RECORD ALL DATA EVERY
-------
J>
I
N>
••J
f ,:-. P • ,
.-:-. H
f s •
TM
- VMfl ,
RBflR.",
VbJC
MUD
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TT
STflT
DH
CP
TH2D
VMS
VWS
VlRpT
QflCT
VSTD
QSTD
FHI.JT
T-UTj
FHGR l|
FHLB *
-------
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 1.0.. (DISTANCE A - DISTANCE B)
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
CALCULATOR
TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
Cu, -
,
c
- »
SCHEMATIC OF SAMPLING LOCATION
TRAVERSE
POINT
NUMBER
t '
2_
3
4
5
If
7
$
9
I
FRACTION
OF STACK 1.0.
,0/(.
,OH?
,0%Z~
.12.5-
1 1 VI
i 2L2.C?
,2S3
,37r
.fezr
\o ,7/7
n
• • . ' J 2-
13.
m
i^
it*
.1£0
,tf^ /
,97s-
,9/s*
.^Cl
ag>ty
STACK 1.0.
7/u
/zk-'
It* ty
3L\
jj7 2/^
Via ''H
53
57 Vg
(<> l^i.
6M 3/M
/ ™) 2 AJ
7^3/5,
72 5^
DISTANCE B
3V
t
t
i
1
i
\
i
J/
TRAVERSE POINT LOCATION
FROM OUTSIDE OF PORT
(SUM OF COLUMNS 4 & 5)
44$-
7~£
_J?%
/Z3/4 -
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/?%
itf'/**
Zi '/j
W%
30'sks
b//4
t>3~
t>8~$
~ y/ty
73%
7£'A
A-28
-------
PRELIMINARY VELOCITY TRAVERSE
- £.f A
7V"
LOCATION
STACK I.D..
BAROMETRIC PRESSURE, in. Hg
STACK GAUGE PRESSURE, in. H20 T.
OPERATORS
SCHEMATIC OF TRAVERSE POINT LAYOUT
TRAVERSE
POINT
NUMBER
A- /
z_
3
• 4
S
6
7
€
9
/o
//
/2.
/3
W
/r
/£
AVERAGE
VELOCITY
HEAD
Ups),in.H20
• S*0
•r<
,6^
,7/
,7o '
,*?/
•7°
,^7
• 70
•7^
.y?
,?r
,?/
,-79
. ?r
• 7'
!\.^
•11
STACK
TEMPERATURE
(Ts), 8F
W
7^
1*
-?v
7f
7#
"7W
7^
7V
7^
-7
-------
PLANT
DATE
NOMOGRAPH DATA
CO- -
SAMPLING LOCATION
CONTROL BOX NO. .
CALIBRATED PRESSURE DIFFERENTIAL ACROSS
DRIFICEJnJijIU
i
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 OPSTATIC 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
^6
T(navg.
Bwo
Pm
ps
P'Pm
savg.
•^Pavg.
^Prnax.
1C
$
*
//
/,9-?
7o
3
*
*7W
•75*
•7?
>1
fjh
T
/
A-30
-------
FIELD DATA
/0-3.S--79
SAMPLING LOCATION .4,
SAMPLE TYPE. '
OPERATOR /*(&•
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE. (PI.,
FILTER NUMBER Is) i
PROBE LENGTH AND TYPE 7 •^at-Oal/.ga^l,
NOZZLE I.D . /.?7
ASSUMED MOISTURE. * «%
SAMPLE BOX NUMBER.
METER BOX NUMBER.
METER AH(
CFACTOR.
A2 .2 7
/.
/• Ol
PI TOT TUBE FACTOR.
REFERENCE A p_^_L
MOTE^Xr s. • 6l$
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK THE
GAS METER READING
(VJ. It3
2 7 2. £06
VELOCITY
HEAD
IAP$|. in. H^
ORIFICE PRESSURE
DIFFERENTIAL
(AH). i». HjO)
DESIRED ACTUAL
STACK
TEMPERATURE
(TS».°F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in. H|
SAMPLE BOX
TEMPERATURE,
°F
IMPINGER
TEMPERATURE.
°F
fi-l
. r
^35-
/.or
r
^_
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w
73
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A/r
7^.0
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73
33
.84
Co
"76
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39
7
JZ.7O
\4
AZ
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7X.
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Vs'
LC,
fro
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7
76
u*.
Ai
317
J3
-------
VjO
to
CLOCK TIME
i24 hi
ORIFICE PRESSURE
DIFFERENTIAL
(AH), ii HjOl
DRY GAS METER
TEMPERATURE
PUMP
VACUUM.
in H|
GAS METER READING
STACK
TEMPERATURE
SAMPLE BOX
TEMPERATURE
°F
IMPINGER
TEMPERATURE
°F
TRAVERSE
POINT
NUMBER
INLET OUTLET
-'•£' "^ i^J O 03yi-4>.:<3-" v
-------
FIELD DATA
PLANT.
DATE_
-OX"- "TT
SAMftliiG LOCATION
SAMPLE TYPE
RUN NUMBER "
OPERATOR
l
PROBE LENGTH AND TYPE.
NOZZLE I.D. . JV 7
AMBIENT TEMPERATURE Of
BAROMETRIC PRESSURE
STATIC PRESSURE. (P$) ^
FILTER NUMBER Is) _
ASSUMED MOISTURE. %
SAMPLE BOX NUMBER.
METER BOX NUMBER
METER AHg / / ff
C FACTOR ).£>>
PI TOT TUBE FACTOR fc
REFERENCE Ap A /
NOTE CXJ ~ , O
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(Vml. It3
VELOCITY
HEAD
IAP). in. H0
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjO)
DESIRED
ACTUAL
STACK
TEMPERATURE
(TS».°F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in. HI
SAMPLE BOX
TEMPERATURE.
°F
IBPINGER
TEMPERATURE.
"F
JU_
A£L
57_
57
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A/V
7^-
2-C/o
'66
K
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Co
«. i
fo
£
J"/
• 62-
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£7
SI
17
Si,
^\
JT^-
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2-7
62-
25-5"
rz,
10
7.r
4^.
rz.
33
62,
7XS
12.
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13
39
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75"
i£.
37j7.'i.3^
L2£
t?
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0
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1
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2^
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-------
TRAVERSE
POINT
NUMBER
b 'ft
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10
(i
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|LJ
1*
1(0
^N. CLOCK TIME
TIME, mm v^
v\
11
2,0
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GAS METER READING
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VELOCITY
HEAD
ill-
>7^
i <$"3
,53
i S"M
•PI
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t?1
.11
ORIFICE PRESSURE
DIFFERENTIAL
(AMI. in H?0i
DESIRED
\>2.°[
/. Z1?
I'H
l^
/•'/S"
/•-S"
J, U
f'5^
liC>
LP^
s?
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ACTUAL
i /•
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STACK
TEMPERATURE
lTsl°F
3£^-'\<£
*7^
75"
75-
^.^
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7£7-"7£v^/
DRY CAS METER
TEMPERATURE
INLET
•w*
<5t)
S^
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pt?
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^3i*'O
o^
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<£~2,
fco*
OUTLET
(T»oul'°F
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.
31" Lf"''
ro to en •&• to ••£' • en
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H y x
PUMP
VACUUM.
1
I
t
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1
1
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£_
^
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SAMPLE BOX
TEMPERATURE.
°F
7.5-^
^S3 —
'Z S"5~"
Z.S3T"
"Z6><9
2.6>C>
2JT"
^&>O
'?$'£'
IMPINGER
TEMPERATURE
°F
^"3
57?
SV
i"V
sy
J>"5^
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sSPS~
>
CO
4r-
-------
PLANT.
DATE_
\n -
SAMPLING LOCATION.
SAMPLE TYPE
RUN NUMBER ,3
OPERATOR.
r.
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P$)
FILTER NUMBER (s)
FIELD DATA
PROBE LENGTH AND TYPI
NOZZLE I.D
ASSUMED MOISTURE. %
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AH0
C FACTOR
Eftc
PI TOT TUBE FACTOR Y
REFERENCE Ap I. 1
NOTE LCI- -
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
GAS METE^READING
VELOCITY
HEAD
(APSI. in. HjO
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjO)
DESIRED
ACTUAL
STACK
TEMPERATURE
(T$).°F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in. H|
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
"F
^_L
!•£.
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Co
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3.
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3
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2-
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13
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^21.
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-------
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TRAVERSE
POINT
NUMBER
_£
f\
to
II
a
|A
i*f
|6
^N. CLOCK TIME
TIME, mm \^°CKl
— —-__
>j
j»7
3o
13
*•$
42.
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1?
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('} *• "
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lVni. II3
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(-/fc 5" • *•/
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HEAD
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t t *
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- ''•"/ 'V
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ORIFICE PRESSURE
DIFFERENTIAL
(AH), in HjOi
DESIRED
/'3
/• "-' •«"
/ ^
: /
/ ")
, ^)
/, ')
1. "1
^
I»5l5f
/-
*(f
ACTUAL
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STACK
TEMPERATURE
(T$l °F
~7"> '
-7 7
"•'?-
:. / /
) :'"
' t •'
•h
'/,)-
•J V
13^ -^ l-^
DRY GAS METER
TEMPERATURE
INLET
•T.,...«F
•C* '-?
C? t,'
V^:>-
/„ 7
/()
- 6"/-
/ t-*/
OUTLET
^';'?'
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--, -.?
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^
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1
PUMP
VACUUM.
in H|
1
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TEMPERATURE.
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7 £.0
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--
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t' ^
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-------
TRAVERSE POINT LOCATION FOR CIRCULAR DUCTS
PLANT
DATE O-.:)-.'"/?
' "*"
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
u -^ p
-- j
K
V. •-' -
SCHEMATIC OF SAMPLING LOCATION
TRAVERSE
POINT
NUMBER
fi-(?
f\
"2>
V
s
f*
Vv"
FRACTION
OF STACK I.D.
•m ,
•iy5/«/.r
"" pq, L?
"^ "•».•/
• ii'' ?£ t/ ' •
,:-,.:.«,-v *-* /
f-b .L?
.
STACK I.D.
n
(. 13-
"
.-
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i ^
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PRODUCT OF
COLUMNS 2 AND 3
(TO NEAREST 1.8 INCH)
^
l&l
aH
^'0^ . .-
' Gl^'
6€i
DISTANCE B
Vi"
l<
),
1.
I.
i-
TRAVERSE POINT LOCATION
FROM OUTSIDE OF PORT
(SUM OF COLUMNS 4 & S)
Sir
>f
au
^
Ci
72^
I
A-37
-------
PLANT .('r-r-v .^rvJ
DATE * •> .;'.->•
LOCATION 'ify-cK
STACK I.D._
PRELIMINARY VELOCITY TRAVERSE
f»*
BAROMETRIC PRESSURE, in. Hg
STACK GAUGE PRESSURE, in. H;Q
OPERATORS tteJ-S\S* -
(>•> J'lwt.U.c.^
SCHEMATIC OF TRAVERSE POINT LAYOUT
TRAVERSE
POINT
NUMBER
f
f**
.•„"'.
'•'•- -
J
'J
\
\ •
^
*
f
y»
lr
— •
AVERAGE
VELOCITY
HEAD
Ups),in.H20
ri^
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.^3
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» .17 v»-
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STACK
TEMPERATURE
(Ts), °F
^^
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•., ",{
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— ^
ti<
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. -•
f
W.O& //
TRAVERSE
POINT
NUMBER
AVERAGE
VELOCITY
HEAD
Ups), in.H20
STACK
TEMPERATURE
(Ts). °F
A-38
-------
NOMOGRAPH DATA
PLANT.
DATE
SAMPLING LOCATION
CONTROL BOX MO.
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
•>Hr;
T|navg.
Bwo
>«
ps
P°Pm
savg.
•*pavg.
APmax.
I- /
•\ •-.
• *-*i .•*.
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A-39
|
-------
FIELD DATA
PIANT_H£
DATE_UllOj-l-L
PROBE LENGTH AND TYPE.
NOZZLE I.D ?- 3.'
S • <.'%/>'
.e-
o
TRAVERSE
POINT
NUMBER
ft
* f
.1
43
ll
?
&
B
r *
o 3_
••/:
id
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3"
^
SAMPLING L(
SAMPLE TVP
RUN NUMBER
OPERATOR
AMBIENT TEI
BAROMETRIC
STATIC PRE!
FILTER HUM
X. CLOCK TIME
STT'NC XCLOCW
TIME, mm NT
^W^-SL_
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KATION f< -0V V.'« •••«•• O 1'^M'Vi.)
E AlX'\
£ ^
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f. i--. .;
•PERATURE 3 ^ • j f ^
PRESSURE ' <->VvSPV
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RFR |t) * ^ S ^ ,1 ^
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'F "
* . f\
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READ AND RECORD ALL DATA EVERY
GAS METER READING
'V K3
'Jyv! •'> »y
v 5 I /-- ^
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"/ "'. 7 ,"' /(.-'
y/^". '?...^
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STACK
TEMPERATURE
(T$I.°F
•Lf "'•>
'/ J.
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V5
i/ 3
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(45.IL.;//)
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SAMPLE BO)
METER BOX
METER Mt
C FACTOR.
PITOT TU
REFERENCI
NOTE
t NUMBER V
NUMBER : A A ft* |r
{ c, • .. . .
1. '
9E FACTOR
• Ap
. :,^ •: 0, 7:-!?h:.o-:
i. C «_* /tT" ,^O~f ""'I'-'-'r
ES^- ^. /a- .&! ' f'^'-.
DRY GAS METER
TEMPERATURE
INLET
(Tm |n).°F
^f
•' , •.',_'
V.A
i .'
^^
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• *' V '
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''''.'!•
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;' Hc ;pv>7
c 1.0817
' 0. 848
•• 13. 1
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U. 61/345
1. i"Uu699:. 65
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44 Q=:s 1 fi--.^
7625v ft ^ "=;•-'
j •-' i o 8175 ft ' :; ti Q
1 64146. 1R51-P
' 93. 25 509 9:"; 4
$ 0. 3873
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-------
FIELD DATA
PLANT.
DATE_
PROBE LENGTH AND TYPE_H
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER X
OPERATOR Utt
AMBIENT TEMPERATURE .
BAROMETRIC PRESSURE _
STATIC PRESSURE. (P$)_
FILTER NUMBER ($) 2.
READ AND RECORD ALL DATA EVERY.
HOZ71FID . .X3.7
ASSUMED W
SAMPLE BO
1ISTIIHF 1 ^1_
X NUMBER
METER BOX NUMBER / 4i-J *7
METER AH,
C FACTOR.
PI TOT TU
REFERENC
NOTE
i ,'T'
? ' '/
BE FACTOR
E AD
/> ^) ^
. f '•• \ »/ ^
MINUTES "*- -^ '0* .. <>[
K
TURE
F
9
/
^
• ' •
•™^
(.-7s)
DRY GAS METER
TEMPERATURE
INLET
\)
3 7
~)2
~n
<7 Q
$c
£ j
V
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OUTLET
_£ J
(p (•>
{-e U_
G- Q
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6 7
^MF
6> ^
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L-J L>
Q><^>
,(.
bis
.^
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PUMP
VACUUM.
in. H|
v.r
5"
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0. f373i' f,:-.P
1=69 .,,H
: 43= 42 TS
72. 58 TH
45. 272 VMfl
24. 44 PBflR
2. VI.JC
8. 4 WSG
28. 27 HS
f:,0c TT
' X -n. ft5 STHT
0.227 DH
1. 0317 V
n. H48 CP
10.4 ' TH2D
38.01656842 VMS
fi -^j.iTP 'v'lii:-.
. 1. 273022952 °^ri
: „ 9 ft 72ft 97 70^ MD
i 2ft. H30:-;4^38 MWS
i 24. 39220588 PS
: 45.22841569 VRCT
76716. 43869 QflUT
I 38= 18024509 VSTD
647fcl. 3:J1 fZ UbTD
,-, ,-. J J .-, .-, - 1 -j ,-, B .- T
yy. 412 ji ib •-. i
1 n •"••'•• 10 FUhlT
U . o -.:• 4 j r n W 1
fl T I'll
1 o=iqd=i--:-.:'Hq FHGP
- "^ 4ft-"-ft"::::-;fii FHLB
n. T GR
I 0. T LB
-------
FIELD DATA
>
i
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TRAVERSE
POINT
NUMBER
0
A '
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7
i,
•7
/ ,
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1
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DATE /£- *ln-~7?
SAMPLING LI
SAMPLE TYP
RUN NUMBER
OPERATOR .
AMBIENT TEI
BAROMETRIC
STATIC PREJ
FILTER NUM
>sv CLOCK TIME
^L™\s5c»
TIME, mm N^
~~ 'St&^J—^
/
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NATION "^futJi. L^t^P £>4-qkzus>Q-' „
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•PERATURE 4 7 6^
PRFKUHF -2¥.V¥
5URE. IP j ^BE| ~ i ¥ v
RFR 10 -7 5 < V ^
PHOBF LENGTH AMD TYPE "7 V^a>
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METER BOX
METER AHfr
* AJC
i.7
KTUHF I 9v~
(NUMBER
NUMBER / <*• 5"
1- ?
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REFERENCI
NOTE
IE FACTOR
•An
t(od .
1 C o4 lly" ,01 <£
READ AND RECORD ALL DATA EVERY f MINUTES L *^ IO '' ' C °
GAS METER READING
i V ft3
•>67.1ro
<^W7^C
^ V V . 5 7«
4^1 $^'
9-^7. £/s'
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7JP
VELOCITY
HEAD
(APS). in. HjO
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ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjOl
DESIRED
f't
is
/•*>
/•^
«7.6>
2,1
*.v
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/ 7
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f ,— ,,
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ACTUAL
f
STACK
TEMPERATURE
(T$I.°F
*v
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^ (,,5
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vn
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DRY GAS METER
TEMPERATURE
INLET
(Tm,n)."F
/,,6
*76
^
^^
^y
V6
7c^
^(^
^/
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^
^^
'V
(7».*
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OUTLET
.-F
>">"
6>
6
b
(S.17fj
1
1
fto*^ •)••.• , -, .
1
<-"
T! o. rn^p,
^ 1.75
? 37. y2
J 71.54
45. 462
, 24. 44
• Q 4
2R. 97
! -.-• ;-; •"• ~7
' f:. l"l .
. ' -0. 45
0. 227
1. 0317
0. 848
1 ":. . 4
>!o. 2576829
0. 53735
1. 385099998
0. 986149
28. 81805453
f £4. 4U691 176
45. 9n5ft?"^Rp
77865. 21422
39. 15913666
66421= 7276
96. 56084396
0. 2413
0.
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55. 41442:.44
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0.
r,:.. r
,:,H
TS
TM
VMH
PBflR
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MUD
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PRELIMINARY VELOCITY TRAVERSE
PLANT.
DATE.
/"/ U-g.'*yi*MJI.M FJLX'f1/^ 7ar^3'
**- Sj *V ba^.U.oiyX^ o *^t~U«3C
* PRF^IIRF in Ho
LOCATION
STACK I.D. -'it. ---. ^-
BAROMETRIC PRESSURE, in. Hg
STACK GAUGE PRESSURE, in. H;Q — >
OPERATORS ^ -l l L
0
TRAVERSE
POINT
NUMBER
fr'l
?_-
^
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7
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f
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13
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VELOCITY
HEAD
Ups), in.H20
ijb
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1*7
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l.o
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STACK
TEMPERATURE
(Ts), °F
1^
/
SCHEMATIC OF TRAVERSE POINT LAYOUT
TRAVERSE
POINT
NUMBER
/3-(
.2-
3
¥
y~
^
7
5?
?
10
u
tz-
13
/
-------
FIELD DATA
PLANT.
DATE_
SAMPLING LOCATION :VU
SAMPLE TYPE ^&*Jf-
RUN NUMBER ' (
OPERATOR Ni&
PROBE LENGTH AND TYPE.
;yyr
S i /.
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE _
STATIC PRESSURE, .°F
DRY GAS METER
TEMPERATURE
INLET
(To, ...I.-
OUTLET
PUMP
VACUUM.
in. H|
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
«5"3
l
8
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•fa
J23.
-5
JL3S"
235-
52?
1SL
2£
^35"
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f
.n
ft
to
ST?
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1.7,
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to
ro
. 3
To
3,0
M'.O
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32.
63
2-3
^_
n
.,
it
A
^L
1
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1,04
-------
TRAVERSE
POINT
NUMBER
0-*
9
1°
H
I;L
i3-
•4
\4
lie
"^^tLOCK TIME
VTL"C\SL«»'
TIME. mm x^
" _______
\L
P
/L0 4 111
2.2- 5*"-JlW
7^ fOZfH
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2$
30
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si -i o ^
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IW.I. II3
T/9/.5"
ftZ^?
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<^ ^b^. i-z-fr
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C0??. CP
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ro
'.£'
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Dr-t'i
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STACK
TEMPERATURE
• T.I.-F
5a<
5b
5?r
5-5^
5-q
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.srs"
—< i-* cn >.•.< >.-.' >—< '—'
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o o co ••••• o co "..j cn a-, o --J '•••a- cn cn co -
• • co po " !"* ••£' cn cn ~--\ ••& cn co IT> cn r
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53
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1 1
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OUTLET
.T0ou,..«F
y¥
*>¥
^4.
5^
w$?
^
H?
H,^
3.6>^~
2*b(j
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0
M*
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:=Z X- 3 — 1 — 1 5- ?•
O 70 X' 12 CO X ~0
1
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IMPINGER
TEMPERATURE
°F
S'O
5~*>
•ye>
5-v
S7>
5o
ro
6"0
j-o
-
• !
1
I
jr-
VJ1
-------
FIELD DATA
PLANT.
DATE_
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER 1
OPERATOR
rr
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE _..
STATIC PRESSURE, (P ) ~ . 3 !
FILTER NUMBER (s)
PROBE LENGTH AND JYPE.
NOZZLE 1.0
ASSUMED MOISTURE. "I
SAMPLE BOX NUMBER
METER BOX NUMBER.
METER AH~ U
C FACTOR __UG
PI TOT TUBE FACTOR
REFERENCE Ap U
NOTE icn. - .01-7
/,1'VH
ST>
fr?V
T-uU
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
SAMPLING
TIME.min
CLOCK TIME
GAS METER READING
(Vm». It?
VELOCITY
HEAD
(Ap$». in. H^O
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjO)
DESIRED
ACTUAL
STACK
TEMPERATURE
(TS).°F
DRY GAS METER
TEMPERATURE
INLET
ff.iJ.-F
OUTLET
PUMP
VACUUM.
in. H|
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
fl-/
5M-
t
235-
hot
. i
rs
it-
J>'»7.4
i
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yo
rs*
4-7
Mb"
.TV
/O
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I/
zx
&
2710
S'V
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01-
^5_
JTD.
2$
.It
2.7S-
275
_U=_
J£51
^S_
jLi
.2=Z£
.Jto.
-^
re;
^
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10.
/.ol
M-
-£t
J7D
-5-0
-------
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
iWBi. II3
VELOCITY
HEAD
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in HjOl
DESIRED ACTUAL
STACK
TEMPERATURE
(T$l "F
DRY GAS METER
TEMPERATURE
INLET
iT.Mi.«F
OUTLET
PUMP
VACUUM.
in HI
SAMPLE BOX
TEMPERATURE
IMPINGER
TEMPERATURE
°F
57
Iff
.<*to. /
5.41.3
62-.
ID
to
2.65'
J.70
13-
s.ts
i.fl
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2>o
ms~w
*"/
p O
_£> °O
_P -J
i--- or-' co co -fi- ro ro • ° co
o co co ro en -£•• co VD -t^ co
cr- en • ro • • • ••& en
° '•£' ro en co -£•• ••£> en -£•• "-1-
cr-. -P-. •"••j co '.£i i— r-o -P- r-o o -j
co • -P". • en -P>- o en o ° r-o >-*•
o ~-j o PO •—•• ro •"•• ~-j '•£> ^•~l• -f^- o ° o i
• ro co i-* i-* '?•• -\i '.£i ro en co • o • o
• • —. .. n . . ... j ,—, fy-j (^t v...t
a
r-.-i ivi
i",-i co en i-j
.t, -j en -£•• •
i-- ro '-•-' --7 •— •-• • v r;;.f,,...,; .:..j ,-,-, .v. co >-••' cr- . ^J-1
—i r-.'i i.i '.j_i ! -T-1- '-•-''—' -' . . . o r. ,T- . i-i r.-i ji. rn '.j_i
PpppppgsSs§g^2*«^"«*S:titt- :^-jw
'7'. -P- '
ro co en
CO •£•• CO
i TI TI ~-r
IX
. r~ IT.' si
i ro 73 —i
to co ID 5 3 .. < ±; ^- _;
i _i __i i—i —i TJ :=_ 12 .--. •= ' >v Ll .-
, S M -H -H co co a 3 co co a TJ --
CO ~D
—\ 3 SI -C TO -C
ti ID —i X' si co s: ID 3 -H —i;
21 —I —I CO tr! iT' O xO ICi 12 CO
1
-------
FIELD DATA
PLANT.
SAMPLING LOCATION 3,<4
SAMPLE TYPE ^M
RUN NUMBER_
OPERATOR _
PROBE LENGTH AND
NOZZLE I.D 1
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P$) ~
FILTER NUMBER Is)
tt
ASSUMED MOISTURE. * 3
SAMPLE BOX NUMBER
METER BOX NUMBER.
METER AH
C FACTOR
tcST
PITOT TUBE FACTDB
REFERENCE &p (
NOTE UMT --
'. v 01 5
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(Vnl. It3
. / 0 3
VELOCITY
HEAD
6
s-/
Jt)
, J"
2.70
JL
21°
00-
ro
1
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si
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^jm.
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-------
yi fr
TRAVERSE
POINT
NUMBER
l3'?
C[
JO
II
UL
\<4
if
it?
, i
^N. CLOCK TIME
TIME. mm >>^
lw
f*
to
j^
j
a
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2-fr
1)0
ijs
7J (f5"
;
1
f? , on-
" i—1
' en <-*•
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GAS METER READING
(Vrai. II3
V"7 "7 , (a
5 ")S*i G
TT9-§
TV< ^
5"ir2.. 3
5^3 .^f
5^V, *-/
5^fc . 3
^TPH i o ^?*
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4i co ° en ~-j " "
• en en co • •*• o
VELOCITY
HEAD
(Apjl. in H^O
iV*j
^9
, $5^
« 69
1 7 1
1 7^-'
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i '.£i 'I'' CO
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i f n i i --J i 1 1 i --.j i-* i-.j '-a.' •-'
41. rri o pi'i ' if " "T- '"' CO TO CO ' '-£i
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t_i i-' 'T- -P-
I
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• - J i-1- en o. --J co a-. 4
X CO CO X' X" ~
r " L .' i L. .1 ~f '•- *••• i — i '. •' •• •• •-• •-
. rjj TJ m ^o — | — | i— i fi ti — I — I CO C
i ..£. -j ro i^
:i p.': i~i iT, iTi
1 CO --J '_i i-J-
- '.£' CO --J -J
I < ---
"i f 13! CO 0".
ORIFICE PRESSURE
DIFFERENTIAL
(AHl. in H^Ol
DESIRED
M
'77,
1-0^
/, ^<
/«3
/'"?5^
/.-^
i-'7?
LIO^'
'
•-' "_,
CO CO
en -*- ij-.
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—i
X
ro o
n T1 -c
ACTUAL
^T ^
s
O i
• i i
l-.-'. • IT
..£1 ro -P
fl"l
—1
1 — 1 ITl —
STACK
TEMPERATURE
TO
s""Z^
f |
JTD
rt)
TD
5D
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$-/
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h(V-f IV
r-o r-o r
'.£' CO
a it i "
. 1
i. ro '•£' '•£' •£• -.
..£' -J • • -1
-1 "Tl :=~ l'l"l '~ "
3; —1 — 1 CO U L. .''..'.
'
DRY CAS METER
TEMPERATURE
INLET
&O
C?U?
£jt/
/,«^
(p G
/f»4
fro
-70
~1#
5k-
CO
0 CO C
t* • en c
-.J iT. '
IL. 4:1. " '.
^ en CT-' i-
XI
n-c
i' 3i — i -
Tl X1 IS '
OUTLET
5k
5"&>
-TV
S~k
S"V
5^
c*^/
5^^
5"k
/
S^^tl/
PUMP
VACUUM.
~L^
i
<2_
•^
"•*>
3
3
3
3
^
[
_i
a
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-, „ ...j
;- '• IT:
0 r~i '"0
-•• co P.J
H i:- f-
T . .
' , *>•
'
SAMPLE BOX
TEMPERATURE.
°F
z.r?o
2-70
2.6?s~"
"710^
2-£s —
7.3O
2.10
~Z1€)
"Z.~?o
..
IMPINGE R
TEMPERATURE
°F
5~£>
5~O
3D
,r&
1
.„ .. - - 1
i
*-
UD
-------
FIELD DATA
PLANT
DATE /f
PROBE LENGTH AND
NOZZLE 1.0. •
AMBIENT TEMPERATURE .
BAROMETRIC PRESSURE _
STATIC PRESSURE. (Ps)_
FILTER NUMBER Is) _/
ASSUMED MOISTURE, t I
SAMPLE BOX NUMBER
METER BOX NUMBER 3l
METER AHfl ~
iDlf
C FArTOR —
PI TOT TUBE FACTOR.
REFERENCE A p ^_TL.
NOTE <^1T r =•
i :
SX3L6
{• ^3 READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(Vnl. It3
VELOCITY
HEAD
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjO)
DESIRED ACTUAL
STACK
TEMPERATURE
a$i.°F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in. HI
SAMPLE BOX
TEMPERATURE.
IMPINGER
TEMPERATURE.
337
2£
/oo
J_
vn
o
O
2305
' I- I
t '
f <
/OS
•70
//O
0
J+
%
//
-^4
-Ui
2u]
.
X
'
-^5r
-------
TRAVERSE
POINT
NUMBER
>
O
o
CLOCK TIME
GAS METER READING
VELOCITY
HEAD
pj). in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), id. HjO)
0.7
•
STACK
TEMPERATURE
(T.I.-F
DRY GAS METER
TEMPERATURE
OUTLET
PUMP
VACUUM.
in. HI
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE,
°F
FIELD DATA
PLANT.
DATE_
SAMPLING LOCATH
SAMPLE TYPE
RUN NUMBER £.
OPERATOR _
io-cC_
PROBE LENGTH AND TY
NOZZLE I.D. C>-
/.-
AMBIENT TEMPERATURE _
BAROMETRIC PRESSURE _
STATIC PRESSURE. (P$l
FILTER NUMBER Is) f
. 04
ASSUMED MOISTURE, %
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AHa :
C FACTOR i
PI TOT TUBE FACTOR ...^
REFERENCE &p —
MOTE L~C T-
Tb
- .°i87
3 =>e."t 3. 6 READ AND RECORD ALL DATA EVERY.
MINUTES
/oy
-------
FIELD DATA
PLANT.
DATE_
\ o~
PROBE LENGTH AND TYPE.
NOZZLE I.D . *"»
SAMPLING
SAMPLE TYPE
RUN NUMBER.
OPERATOR _
_L
-a^ci
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P )
FILTER NUMBER Is) L. £*T
ASSUMED MOISTURE. % _
SAMPLE BOX NUMBER
METER BOX NUMBER
METER AH~
CFACTOR
PI TOT TUBE FACTOR
REFERENCE Ap
NOTE L-
vn
r-o
-------
FIELD DATA
[ ~
1
*••• ' ,*'
<> 0«
TRAVERSE
POINT
NUMBER
(> - I
/\- 6>
V
/.&3&\
PLANT ^ ? K. - &Vvx>C<.^A >
OATE « fc -T_r - "?«=»
SAMPLING L
SAMPLE TYF
RUN NUMBEI
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FIELD DATA
vn
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SUMMARY
RECORD OF VISiSLE EMISSIONS
Type of Plant
Company Name
Plant Address
Date
~*?-S-
Type of Discharge STACK
Discharge Location
OTHER
Hours of Observation
Observer
~&/t
Height of Point of Discharge
Observer's Location:
Distance to Discharge Point
Height of Observation Point
/o
Direction from Discharge Point
Background Description
Heather: Clear Overcast Partly Cloudy Other
Wind Direction V/ind Velocity
Plume Description:
Detached: Yes No
Color: Black V'hite Other
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mi/hr
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Lofting
Estimated Distance Pluns Visible
Coning Fanning
Fumigating Other
A-56
-------
0 . 0
IT,
^ - o
T
-l?oo
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Company Name _^
Plant Address
Stack Location
RECORD OK VISIBLE EMISSIONS
Date
Observer
Observer's
Weather Conditions
MIfl
TIME
)0
30
31
32
sa
34
35
36
37
38
39'
40
41
42
43
44
45
46
47
48
51
52
53
54
55'
J>6_
57
58
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15^ 30
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COMMENTS
XV
Otet
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.
-------
RECORD OF VISIBLE EMISSIONS
11
n
8
o ^
Company flamt
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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
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A-58
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4-- 6
Company Name _^
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3
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COMMENTS'
A-59
-------
ty
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\\
Company flame _
Plant Address
RECORD OF VISIBLE EMISSIONS
Date
Observer
Stack Location
Weather Conditions
Observer's
Location
TIME
FR
MfN
05
06
07
08
09
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
Z9
SECCriDS
00 15 30
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0
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COMMENTS
£7&£
A-60
-------
Company Name
Plant Address
Stack Location
Weather Conditions
RECORD OK VISIBLE EMISSIONS
Date
Observer
0_
51
52^
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54
55
56
57
53
59
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15
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COMMENTS
A-61
-------
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Ti/"'0
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Company, flame
RECORD OK VISIBLE EMISSIONS
Date
Observer
Stack Location t£^s,e-/ £ysc.-^4s
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SECONDS
15 30
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45
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COMMENTS
A-62
-------
7102-
f
It
2.131-
HR
Company Name _
Plant Address
RECORD OF VISIBLE EMISSIONS
Date
Observer
Stack Location
Weather Conditions
TIME
MIN
03
OH
OS
06
07
08
09
' r
10
11
12
13
14
15
16
17
18
21
22
23
24
25
26
27
28
29
SECONDS
00
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COMMENTS
A-63
-------
RECORD OK VISIBLE EMISSIONS
Company Name
Plant Addres
Stack Locati
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j^y-^^^^^^si, <^>,js**>s- Date /<^ - «=. -s - ^9
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30
31
32
33
34
35
36
37
38
39
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43
44
45
46
47
48
49
50
51
52
53
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55
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A-6A
-------
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Company Name
Plant Address
Stack Location
Weather Conditions
RECORD OF VISIBLE EMISSIONS
Date
ZfT-rttzr^ Observer
TIME
MIN
00
01
02
03
04
OS
06
07
08
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
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SECONDS
00
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Location
COMMEMTS
A-65
-------
£05" £-
HR
Company Name
Plant Address ^
Stack Location
RECORD OK VISIBLE EMISSIONS
Date
Obs erver
Observer's
Location
Heather Conditions
TIME
MIfl
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
00
SECONDS
15
o
o
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30
CD
O
o
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CD
0
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COMMENTS
^
A-66
-------
RECORD OF VISIBLE EMISSIONS
I
Company Name
Plant Addres
Stack Locatl
Weather Cond
s<£rr&-^^*s/*s- <^2^^^^ Date s&-^>-s--?9
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00
01
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06
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10
11
12
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15
16
17
18
19
20
21
22
23
24
25
26
27
28
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-------
RrCORD OK VISIBLE EMISSIONS
0134-0140
Company Name
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MIH
30
31
32
33
34
35
36
37
38
39
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41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
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A-68
-------
Company Name -^
Plant Address
RECORD OF VISIBLE EMISSIONS
^*e*_^ Date
Observer
Stack Location
Weather Conditions
Observer's
Location
J
A-69
-------
Company Name
Plant Address
c
Stack Location
RECORD OK VISIBLE EMISSIONS
Date
Observer
/
Weather Conditions
Observer's
Location f-^a
TIME
COMMENTS
HR
^^.
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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
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56
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15
30
45
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A-70
-------
SUMMARY
RECORD OF VISIBLE EMISSIONS
Date
Type of Plant
Company Name
Plant Address
Type of Discharge STACK
Discharge Location
Height of Point of Discharge
Observer's Location:
Distance to Discharge Point
Hours of Observation
Observer
Height of Observation Point
Direction from Discharge Point
Background Description
VJeather: Clear Overcast Partly Cloudy Other
Wind Direction _ Hind Velocity
Plume Description:
Detached: Yes Ho
Color: Black White Other
, Sky Color
mi/hr
Plune Dispersion Behavior: Looping
Lofting
Estimated Distance Pluns Visible
Coning Fanning
Fumigating Other
A-71
-------
= o
Company Name
Plant Address
Stack Location
RFCORD OK VISIBLE EMISSIONS
Date
¥-
Observer
Observer's
Weather Conditions
TIME
MIfl
30
31
32
33
34
35
36
37
38
39
40
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
50
00
SECONDS
15
CD
<£>
45
O
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COMMENTS
£f
A-72
-------
+
70
Company Name ^/yy^,
Plant Address
RECORD OF VISIBLE EMISSIONS
Date
Observer
Stack Location
Weather Conditions
Observer's
Location
TIME
HR
/?
7oft
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17
MIN
00
01
02
03
04
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*>^MM
06
07
08
09
10
n
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
SECCriDS
00
0
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RECORD OK VISIBLE EMISSIONS
„., ^ /•?, ^^, Date
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Plant Address
Observer
Stack Location
Observer's
Location
Weather Conditions
TIME
30
31
32
33
34
35
36
37
38
39
10
41
42
43
44
45
46
47
48
51
52
53
54
55
56
57
58
59
DO
<£>
<*>
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SECONDS
15
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A-71*
-------
RECORD OF VISIBLE EMISSIONS
Date
1
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Plant Address ^£s-?^~ ~Z?77£-r^£-'"'*- Observer ^^ «^fc^-s>7^ £/^-x^=»x^ Observer's
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/ Location . ^>&xrv^.
TIME
FIR
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00 '
01
02
03
0'4
05
06
07
08
09
10
11
12
13
14
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16
17
18
19
20
21
22
23
24
25
26
27
28
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SECONDS
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O - Q i
•2-4
.
•
Z / -Sib " ^ &• ^ "Z*
^ — O
2V i
•
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-------
Company flame _
Plant Address
RECORD OF VISIBLE EMISSIONS
Stack Location
Weather Conditions
.
/&e/?
ft
n>
0)
0
0
(T)
%
0
0
0
0
(3
0
0
0)
fp
Ib
0
(3
0
0
0
f)
0
0
0
0
0
0
0
0
0
0
0
0
0
0
30
0
0
(9
0
o
()
0
0
0
0
ft
0
0
0
0
c
0
0
0
0
45
0
0
0
0
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$
0
0
0
6
0
0
0
0
0
COMMENTS
j *2*2*o"i — ZZo£>
- -;- -• -£. ~ (^
2-V
•Z2.0S - "227 V •
<=> -n
2-¥
^•- • --
• i
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fj-, / / **f ^^ fc W t. V-'
d J^ 1
1« fl
1
i
.
.
•
•
A-Ul
-------
FUGITIVE EMISSION
INSPECTION
Company
Location '
: .
' U r^
7.?.
Company Rep.
Inspector \Wecuc?nL
Affilitation
Date l£2
Sky Conditions
Precipitation
Wind Direction
Wind Speed
Facility Type
Emission Source
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)
Accumulated
Emission
Time
(Min: Sec)
0 ..
o
0
0
End Observation
tfepi Jwt
w
-------
FUGITIVE EMISSION
INSPECTION
Company EEft- Ao?ce>*ja
Location : \
Company Rep.
Inspector
Affilitatio
Date J
Sky Conditions
Precipitation
Wind Direction
Wind Speed
Jkl
Facility Type Cfflfsp?v?.&•£'.&»£&iVa.^^
Emission Source
GIT.J gt.L
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)_
Accumulated-
Emission
Time
(Min: Sec)
End Observation
-------
FUGITIVE EMISSION
INSPECTION
Company
Location
Company Rep.
Inspector
Affiliation
\o/is
Sky Conditions
Precipitation
Wind Direction
Wind Speed _I
Facility Type Cf>t>(V.r. Of P.J' '<• ubonPo.\ro.\
Emission Source
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)
*f ft NO
J
Accumulated
Emission
Time
{Min: Sec)
16"
0 6.6")
End Observation
-------
FUGITIVE EMISSION
INSPECTION
Company f\r\p cj>>-OGp. . LfthOP*C \&^ n6 "V^O^
-r ' * \ U J'uW J
1 nration ' h/J4&">A i . WVOrf Nf \
«. / ~ —
Company Rpp- • ......
Sky Conditions jL^filPO^^
Prpcipitation
F?cu;tYTVp6 Cra f^per b.rspj.^rVNO^^W^r
-, lnTPPtnr T^(W , R» Kd5^^
Aff5l!tat!nn ^ ^- Uft^fik -1^ "
lh/OC/70,
natP IC/JT/Xn
1 /r l i ' •-
Wind Direction ~~ KU^ *- ^
Wind Speed T^
Emission Source (a r\C,Q)/ r5Q$.V.til
Sketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points.
•Conveyer-
OBSERVATIONS
Begin Observation
Time
Accumulated
Observation
Period
(Min: Sec)
Accumulated
Emission
Time
in: Sec)
TU
o"
0'
o
End Observation
0
-------
FUGITIVE EMISSION
INSPECTION
Location _
Company Rep.
Affil Station.
Sky Conditions
Precipitation
Wind Direction
Wind Speed
KlM 1
Facility Type U^l
Emission Source
Sketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points.
OBSERVATIONS
Begin
_.
"me
Accumulated
Observation
Period-—
(Min:Sec)
7V
Accumulated
Emission
Time
(Min; Sec)
0 .
0
0
End
A-146
-------
FUGITIVE EMISSION
INSPECTION
Company *y "**
\ OC3t'°n M'NCy^Jp'v
Company Rep- •
Sky Conditions A,"
Precipitation
Facility Tvpp ^fif
Aoixp&Ja Capper
A A » 1 * I
0. UsMlf r Cb ^b\V , Mfc^TCs"6
T
> a.cx*>r^
*r (^Sp; U^ce.A^^
in.pp.tor TUao^ IVVsx^..
Affiiitation H&y F- Ud.S"\b^Tr>c
;
Wind Direction — . \\(jf\ -*
Wind Speed — . .. .
Emission Source br»2.Lvy Hftftn K/Pil
/ '
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)
Accumulated
Emission
Time
{Min: Sec)
o—
o
End Observation
-------
FUGITIVE EMISSION
INSPECTION
\Z- Fmisrion Sonrp.i>
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)
Accumulated
Emission
Time
(Min: Sec)
OQlo*
2o loo
End Observation
A-H8
-------
FUGITIVE EMISSION
INSPECTION TE6T
Company
C*.
Location
Company Rep.
Inspector AND&&AJ
Af f ititation
Date
fr^TKl / i
Sky Conditions
Precipitation
Wind Direction
Wind Speed
Facility Type
-------
FUGITIVE EMISSION
INSPECTION
Company
Co-
Location -
Company Rep.
Inspector
Affilitation
Date _
Sky Conditions /frJ.Ooog>S
Precipitation -.-*••
Wind Direction
Wind Speed
Facility Type CO?P0£
Emission Source ^g;/K/»lg ^ .
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: SecV
Accumulated
Emission
Time
(Mint-Sec)
20 (Od
03://
OS!
00-'
4140
End Observation
A-150
-------
FUGITIVE EMISSION
INSPECTION
Cnmnanv ^t >"> >, c fl *^ A.^. — °. i« to-e^u v~o .
1 n^atinn ' c» «^«_"T—vTjLob<' Lo <_aJX>-» ^. J
Prccipi*ation i - • •
Parilitw Tv/np ^•"|5»V»X\\va. JP^ •
Inspector ,_/^' *** ^-a.c^^iv^*-^
l^t ^ 1 " * ^^^^
Affilitfti™ ^"-^ ^^ ^^ * * J "^•NA "
Of»TP J °J-~,"L S"— "7 9
Wind Direction /W «^
Winri SpPPfl r
Fmi«inn SnnrrP Flp* • y. • - -
OBSERVATIONS
Begin Observation 7- \ \ 5
Time
.ipsy/u.i
Observation
Period
(Min: Sec)
I o-'. o o
Q
-t.-z.o5 „
\ o :• o o
\ o -. o
-------
FUGITIVE EMISSION
INSPECTION
Company
Location 1
~#^
v» .
Company Rep.
.AC-a^-Y
Inspector _
Affilitation.
Sky
Conditions Ki/ft- C3lxA
.«or
Wind Dirpp.tinn
Facility
•w
1 V\
mi "r
Sketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points.
OBSERVATIONS
Time
Begin Observation IT- A S"
Accumulated'
Observation
Period
(Min: Sec)
. A o. i o. o
- jQ V .0 5 Vo :,
\P -
- O\
\o c. oo
QVLS"- CM 35
V o -. o
\o:6o
Accumulated
Emission
Time
(Min: Sec) •
ij) o
G : o o
o •„ o o
6 : C
0:00
End Observation
- O
A-152
oo
VG'-OO
\ 0 '.
\ 00 ^
'. o o
O '. 0 O
0 '. O 0
O'.oo
-------
FUGITIVE EMISSION
INSPECTION
Company
Location '
Company Rep.
Inspector
Af filitation
°
/ 02 £
Sky Conditions
Precipitation
Wind Direction
Wind Speed 15~
Facility Type
Emission Source t^> V-
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
(M5n: Sec) :
JCL
Accumulated
Emission
Time.
(Min: Sec)
.33 »
End Observation
VH «
A-153
-------
FUGITIVE EMISSION
INSPECTION
Company
C*
*P.e_r
Location _
Company Rep.
Inspector
Affilitation
Date _Z
.f?
Sky Conditions
Precipitation
O
Wind Direction /I/
Wind Speed ' f'£~ 3o
Facility Type
Emission Source
\J
Sketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points..
OBSERVATIONS
Begin Observation
Time •-•.
O
Accumulated
Observation
Period—
(Min: Sec)
ft>
Accumulated
Emission
Time -
(Min: Sec)
0" &£J
'
End Observation
-------
FUGITIVE EMISSION
INSPECTION
Company
Location 1
Company Rep.
Inspector
Affilitation
Sky Conditions
Precipitation
Wind Direction
Wind Speed /£.'">?*
Facility Type
c M *^
-------
FUGITIVE EMISSION TfST 1
INSPECTION
Company €.?^ AyAt^vv^xrt . ^
\ oration ' falAiCCifitbk . .Cc>P.f>6'/L'y ' (Vic;
Company Rep- • ..-•-.
Sky Conditions oOeVl CAST
Prpripitation ....
Facility Typp Ce>p.fi0L. &Ke* ~!j&&te%Kld~
Inspector . _It)5\Vhh CALS7&AJ
Affilitatinn A?. £. U}(~ST&*>. '*
Oaf I&I Pblff
"•
Wind Direction So^rH UJpfrFstL.*/
Wind Speed /0 - /S~ MpH
Emission Source CoUjtS.^ &/?.(?. Smz.KPft.t--
Sketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points.
__J^ 0— . ._ - ..
OBSERVATIONS
Begin Observation
Time
Accumulated
Observation
Period
(Min: Sec) -
Accumulated.
Emission
Time
(Min: Sec)"
Go.
End Observation
A-156
-------
FUGITIVE EMISSION _
INSPECTION 'C5TJ
•
Company .^ >n p?VACc>/i)&A
Company Rep- •
Sky Conditions d^eA-CA-SI"
Precipitation . , . .
Facility Type (RQuyfr^ fi&Q^- • -^fefc^ZPflUr"
Inspector ,. J^U/'J JtJ*t,'SliOfc+
Oatp . IblfUflVi
Wind Direction Sau-^ CJ^S-nT^Ly
Wind Speed . /0-^o np#
Emission Source fCot//trtT G/ie" ^TZC^P/LtT'
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)~
Accumulated
Emission
Time ;-
(Min: Sec)-
. 60
, co
~
End Observation
A-157
-------
FUGITIVE EMISSION
INSPECTION
Company
.£?A
Location
Company Rep
Inspector _
Affilitation.
Date '—.
Sky Conditions
Precipitation
Wind Direction
Wind Speed
U3
Facility Type
Emission Source
Sketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points.
OBSERVATIONS
Begin Observation __
Time
MAS- --
'JO
Accumulated
Observation
Period
(Min: Sec)
Accumulated
Emission -
Time
(Min: Sec)
} -
End Observation
A-158
-------
FUGITIVE EMISSION
INSPECTION
Tersr /
Company
Location
(/fT
Company Rep.
Inspector _
Affiliation /<-
Date
Sky Conditions
Precipitation
Wind Direction
Wind Speed
Facility Type
Emission Source
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)
Accumulated
Emission
Time
(Min: Sec)
o.-eo
O.
End Observation
A-159
-------
FUGITIVE EMISSION -,
INSPECTION ' eST
rnmpany £PA $*ACO#C>H
i^ati«n vWiawxM G*¥>X.^
it
Precipitation ....
•—•r- X~)' JL
Facility Typp G»MS£ O/IG 'j&wsfe't- ~*>i*/i
TX O ,
Inspector 1 JAU lO /L/VCS.fc'O _
Affilitatinn R> ^ 6J<«r<&/V
'
Wind Direction -L^V OOC/tS
Wind Speed . ^
Emission Source G3U/l$5" ^fefi". Ofac^^/Cf
Sketch emission source, indicate observer position relative to source; indicate potential emission points
and/or actual emission points.
OBSERVATIONS
Begin Observation
End Observation
Time
Accumulated
Observation
Period
{Min: Sec)..-
^O, cst>
Accumulated
Emission
Time
(Min: Sec)
JLC-'fS
O..OO
A-160
-------
FUGITIVE EMISSION ?
INSPECTION TG*r -5
Company ^'n rrrtfiCtoMbfT.. ^
1 nratinn JWtttyVfD/V. CoppCfW)' DU.tt«?", ^T~.
i Comp?ny Rep- •
Sky Conditions J^fifObb/l^
Precipitation f . • •
F?riiityTyPF Cjuflsg. . ®n£\''7Ji&&e/L foV/y-t
Inspprtnr r)iOlCt> . N^STOfO
Affilitatinn S S ^CSTB^
OatP r ^0/^6/7*7
•
WinH pirPCtion . - _/-/!» *>6tf/C T
Wind Speed . . . .
Emission Source Cou/ZS^" \LJR£. oTBCiC^r^
v
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)
Accumulated
Emission
Time
(Min: Sec)
End Observation
A-161
-------
Appendix B
Laboratory Reports•
-------
C3
I
G/^ PARTICULATE SAMPLE ANALYSES Analyst i\tC- Date IVO.O ?
Plant \\{VK( ftr^(i>AJo9^>1^ Sampling Location f~>C»"27V. f-cv^
Run # i
Test Date Vrp^- ~)T Test Period \i-,-^SAQ \t>-J.->~)ci Stack # i
Beaker iVolume
FHA tyv^-^ i-'Hpn
FILTERj it ^fH4(a
FIITFR' ft
FH TCTfcl j
TareO)
qrams
I O<3 T^ay^'
f-S^ ?>
RHU | j
r.HA 1
10TAI
_/' Q rsrns
\ *-V ^^ C) O^r\ f*^
i|£~q3
• i
;
!
|
«H»Ul>
I 02,. /^/^ 9-
nH jj
"Wlfi)
/o^ . 'u^5"
7L.l«/5 -
A Wt
o J fao£
.5O4.T
i,
• Process/?
"HOT-
°'0i"2^
Nefawt.
e> , .'^-1.
-*/4^>
Common ts
C Q^
v /v /* ' Xs * V l*^" \ "
Plant VVYvG^fr"1^'— v^KOo>{ Sampling Location (of «TJxV, CC^r Run ft T_
Test Date y^TiSOS Test Period \o -^s \t» Mv^V^^ Stack #
Beaker Volume
ff ml
FHA ^-r-.-^ MD'h
5 FILTER, // ^Hq>
J; FILTER' u
TgFglJ,
jo 4 'i<§>5"'-
,y-5&l
m FH TOTAL
BHW
"- BHA
^ TOTAL i
Tare (2)
grams
lf^ •a.T^,^
. f S^?7 <
Final (1)
g rams
/ D1/. H ~> m? '
5^1 S 5 '•**
Final(2)
a rams
f£J.J.l>7 IJfr
. 51 *?O
Process/?
Awt. iBlk. Cor.
qrams j qrams
O.//fe/ : -OC?/*^
• //^y — -
I
\ ;
j
86 Comments
Plant 'v'^O-f 'Vi-rt i- C'-^A' Sampling Location (of ^'L"L\u CCL*^ Run # 3>
Test Date iQO^-'^^ Test Period xooc^ v>-1\j->1.^-1.-~,c; Stack #
\
Beaker Volume
ff ml
FHA ftcvV) ''itO
FILTER, # 3.W\
FILTER; #
FH TOTAL :
BHW
BHA j
TOTAL j
1BU>
k/Nll fcl^^V) Q
1 U *•!" T^O* el I
./57A
Tare (2)
qrams
io^, ^9.^9'
.VSTi_"
Final(l) 1 F'nal(2)
qrams 1 grams
/6V. ^7V^*| IP-1. '-•'.' c "'•:
.vsa.Co i .i^AS"*
i
i t
I 1
1
1
A Wt.
qrams
„ ^t°l~f
H& t" LJ t"
I1C U W 1. .
> // ^«*
•f/^S
•2i3V
Process^
Blk. Cor.
qrams
-oo/y
* O3S/ •— '
Net wt.
qrams
» G&^l X
+ \J+^'^
: j
i
:
; . - -«**-Ti'
Comments
ACETONE BLK
WATER BLK
1
CODE: FHA=Front half acetone wash BHW=Back half water(impinger contents + water wash) BHA=Back half
acetone wash FH TOTAL=Front half catch weight TOTAL"Total train catch weight
-------
N>
^vfr PARTICULATE SAMPLE ANALYSES Analyst
Plant ^ ivlf IM-^VK.. v.ctfo-?f Sampling Location y\ ',{".. A ^ • C*,\- .,'_> <>.( MoxV
RtlL Date \\-,^-'!c'J
Run ^ i
Test Date ^rf^-l^ Test Period lo-3.^ \r^ Vcs-.^->o O Stack # '
Beaker Volume
FHA (W^ |!LlrjO
FILTER! # Jl5»n 1
FIITFR: «
FH TCT£L
RHU ,
Tare(l)
qrams
\cf^ ^ll-^
.tUoCa
Tare(2) 1
qrams'
IO7 •^CTT?
4L>DCr3 x
i
;
P.HA i i
lOTrtl 1
»n»ui>
/ O'i.~?7j.3
~\ . O */3L\ '
Fi8arams2>
/4»9.~77^'i?;
\CtA5
AWt§
.•375^
(?»»*3'5/*^
Process/?
Blkramor'
-CO I ^
Net wt.
qrams
.•^•7^0
(, .5"SV^
i
6 •et%r-A1(V O»(?p(i^ Samplinq LocationTCvt^'V("j> C$ v sY~lK v&C#L Run # ,2_
Test Date . ND-O.^--^ Test Period lo-r^cC Jt> \W-a->~» 1 Stack #
Beaker Volume
f mT
FHA ^-^ HVO
FILTER, rf -DSMTf
FILTER' ^
FH TOTAL
BHW
BHA
TOTAL
1BU>
lp4 i?)")0!*"
. ''5*9-5^ —
1
i ' i ':
j
Net wt.
qrams
-aiafl
£.57$
d.&Oft
Comments
^^ / 0 -o
Plant ^N o dXt.0 -do <•»_ ^-^PCf Samplinq Location\ r >^vv^VI v Cvwslxtr Unxi'Run # ^5>
Test Date \h-a5-TR Test Period »c>-^ \^ Vt>.Vi. n 9 Stack #
Beaker Volume
# 1 mT
FHA 9r\-lO 1 5"b
FILTER, # ^S^5l^i" I
Final(l) 1 F'RSlli)
arams grams
lo4/ . ~)b>t~t 4 iCr!. fa 2 !
f.*-0 TH -"i H. ^C> "j1^
i i
i t
i i
•
!
Process/?
A wt. iBl k. Cor.
qrams qrams
O'3tfot> | ,OOlCi
Y- 3VgU
Net wt.
qrams
-3*£ S1
¥/^¥fl
I
i
:
! " .
i ty-biS
Comments
ACETONE BLK
WAItR BLK
CODE: FHA=Front half acetone wash ,BHW=Back half water(impinger contents + water wash) BHA-Back half
acMBla • ••^TP" *^™" -°^—^ '—^e-^~«->.i^ .^^t^u.. -TA-rAi._a^».i ^^^ catfik wej
-------
LU
UJ
e- 3^ — l«J Test Period ir\-^< 4-^ \r\?3~i-~i1 Stack # r Process//
Beaker [Volume
FHA Qp- | I^MD
FIITFR, # 4WH
FIITFR' ft
FH TCTfcl i
BHU | i
Tare(l)
grams'
\\O SM^I
.ItaOH
P.HA j '
10TAI !
grams
IIC? ' ^ C»i2 I
c/.l^>oH- ""
i
j
!
i
Fi8?lms) J FiSrUl)
ll< 4V(o6>^ //5.V46-U
A. Olf/^' ^.^^O*? —
A wt . Blk. Cor. Net wt.
grams grams grams
^eefv «QO/O ^5^7
— Sl.SIO*
i ^-iR^"
Commanls
Plant Arv^fno&a C Olfte f Sampling Location^-^Q "jV./jVuisp iVklei' Run # Zt
Test Date \p^5-~jcj" Test Period it^-nc ^ »/tv-:i_-v->
2? FILTER. // ^S*W7
t, FILTER' u
^ FH TOTAL
BHW
^ BHA
T§F|ti,
mn ^0^,^
.V-S^o
?; TOTAL !
Tare (2)
grams
IftT. tff??
t+S'So "
Fina'il) Final(2)
grams a rams7
\\o ^^
Awt. |Blk. Cor. Net wt.
grams i grams grams
•3,O5^T : ,OOJ3 2>£>5\^-
f.aioi - if,yiQ\
! ;
* Comments "7 «"?>^l
#? v r *-, ^ a -r, .
Plant V\f\
ibT . ^.S^O
.4. ^84
Tare (2)
g rams
/D~7 . ^5 ?>5
y { % i
•
Final (1) 1 Final (2)
grams' grams
\lO. vCWn i/fl 4J?c3O
5.*IOtol ; 3.£\0j
i
I :
I
!
|
, ;
Awt. iBlk. Cor. iNet wt.
grams grams grams
X . k^^M- ' ^ O(0 1 "2i \ 3..lo3Llte
^ Ak4^ i O i 1 ^ r^*5T 1 0
tfC .1^^ 1 r> *^ *^ iO w I f\
j
H-. b^O(
i
Comments
ACETONE BLK|\-A-H 3.^0
WATER BLK ' ' ' a '
.-^.^^^oil I^^T l^^-/
1 1
/b£. 2yt>> J (>S. Jtffr\ ft,00/O 0.000004 ft <3/«?>J(L
1 «-/
CODE: FHA=Front half acetone wash BHW=Back half water (impinger contents + water wash) BHA=Back half
acetone wash FH TOTAL=Front half catch weight TOTAL"Total train catch weight
-------
CO
-t-
U* . PARTICULATE SAMPLE ANALYSES Analvstj
Plant \-. "(Vs ' ^r- • <\ <• ••^••^( Sampling Location *~ \ l!- ^ ^.-'/iVvin.-p Ar.'f
Ku. Date ll-^~~)c^
," Run # <
Test Date \f>3L '^ l Test Period 1 ">-?<< \ •., \>v v . . •/"/ Stack/? '' Process^
Beaker i Volume
ff i m i
FHA (\A-6 \C\T:
FILTERj H JDSM10
FIITFR' ft
FH TCT£l i
Tare(l)
g rams
>o3. 78*^5^
A(oA"^
RHU , j
RHA i '
IOTA! !
w
\ 03. .7 5*9 5"
.4U>S.ol
j
f
!
1
»ii»Ul>
/os • .TOG/'
lfL><4'2>
»wu»)
/ 03 . S Cw/
X Q>'/ '-0
^r-wi* B1kf.=,£or- IN§£=WI-
grams grams grams
O-^»7o .Ooo^i UO/fct>
,OO3L|
,OO"^]
i
• Olt?V
Comments
Plant Hro,£pY*^{V Cj^O^ef Sampling Location I 3 cucV>.Mit 'DiAlO' Run # "^
Test Date ir?^"^^^ % Test Period \O-ciS i>,\^-n-i. -in Stack # Process/?
Beaker Volume
ff m'
FHA nrv^ '5t>
Z FILTER, rf .afiH^
fe FILTER' )?
inU>
VpM-JTlCsl
,4fcoo
^ FH TOTAL
BHW
"• BHA
% TOTAL !
Tare (2)
g rams
io'f qiol *~
.''KpOO-'
Final (1)
^rams
1 (j1-/ . °> ^>->j
.HV^M
Final (2)
a rams
/ ^ . '' S" i1"' *
*•: '*-* -*'O *^^
Awt. |Blk. Cor.
grams grams
- .Ol'Sf .Oool
.(^OA6! — •
' i •
•
Net wt.
grams
,0137
.cost's
»O/*a fc
06 Comments
Plant Wr,(Tv c>>^ tj. C^g<.'< Sampling Location l^ I^"IA|,M^I» riLtrl?iJRun # _j
Test Date \0-^CS--T51 Test Period VD-a.'S AD M^AI-^ Stack # Process/?
Beaker Volume
ff ml
FHA AvN-H 3lfiO
FILTER, i? A5^*/
FILTER; #
FH TOTAL
BHW
BHA i
TOTAL j
Tjnjj)
» OLI f^lO^*
yfjS'CL
Tare (2)
^rams
(04 i 'hJD'S'
.•/^5"3k "
f
Final(l)
grams
;0v. Jf5(.-^/^
,¥$%>
Final (2)
grams
• O ^'. N' "?' v>
y $"??<<
\
i i
i /^
/
'
Awt. jBlk. Cor.
grams grams
.026,1 ! .00/3
fooscj -
1
Net wt.
qrams
' Vr^T^ *CI
*CJ ^/ " *^
t
\ .O3.1
Comments
ACETONE BLK
WATER BLK
CODE: FHA=Front half acetone wash BHW=Back half water(impinger contents + water wash) BHA=Back half
.ne H^k
-------
PARTICIPATE SAMPLE ANALYSES Analyst |v' (L
Plant \-TNQA/)r$/A_ v-^QC^-f Sampling Location "i M ^ \ >.~ -\.«* '.cc.f-'r Run # ; t
Test Date ND-^VT^ Test Periodic- 25 k^Wy;.?;-' •'* Stack #
Beaker (Volume
FHA (W^ 3°<5
FIITFR, # 3&Z3 \
FIITFR' # \
FH IT-rfcl
TareO)
grams
io4. £^"7
.«/s"3S
T8Flii>
ID'S .^^l *
vS"3 S ^
j
RHU , i
HHA 1 • 1
TOTAI !
i
Fi nal (1 )
grams
/O^.
/of. 3 •»
^
• C>2?2.'3
-^G^^/
Process^
Blk^or.
xOo/y
_^
M,^,.
^o<5C^
•SO6>f^
X*^" ^*«
I • i O /-^
Comments ^*^ — *
Plant v^flCVrV) V- ^>.;:cn( Sampling Location "3,*A v.:W-MYJ 1 - r-\c4-' Run # 0
Test Date \o~c^^ a<; -K \r> ^.~i^ ? •"• Stack #
Beaker Volume
FHA IW~\C. ^D
^ FILTER, rf 43?3aS
«jf fT FILTER' #
^ m FH TOTAL
BHW
^ BHA
1BU) 1
1 Of ^ 3 3 5" x
.vsv?
% TOTAL !
Tare (2)
grams
1Of .3?>^S
. V5"V7x-
Final (1)
cLrams
/0V. VV?7
.L.7^73i *
"»U»
;y.l . i/ -V-;^
.k-7 ^^
i
i
Process^
Awt. iBlk. Cor.
grams grams
•* ,//5"7 ^Oo/'?
,C^^oS —
) >
06 Comments
iffi rV
Plant ^,of\Cbr.W^ GM>?PO- Sampling Location 3. U ?v>n\v.vM» l.rxler' Run # ^?
Test Date \v2-lr.--tq Test Period \n>-^s Vr> \c^- r/ ;? Stack #
Beaker Volume
ff i mi
FHA tH-Avp l(uO
FILTER, # 41J5I7
FILTER2 # !
FH TOTAL
BHW
BHA i
TOTAL i
inll)
\o6, 4O&9 **
, v5"to V -
Tare (2)
qrams
lr)x^ .«-io^9
y^«/ '
Final(l)
crams
,'D?,. W7 5'?
Final (2)
grams
/y< • '•'••i»i:»**
/pO^O .(okS^ "
J 1
i
i t
t
*
A wt.
qrams
»Ofe»97
- )•? 2V
Net wt.
grams
^//*/-y
^2"io s
x
/ ! - 33 f"*"/
V__ *^ ' ^
Process^
Blk. Cor. (Net wt.
grams | qrams
/•OQoJ?
i
'Ofe^S
./73L*/-
i
**^~ ~~^\
! ; i\ --l-'//3
Comments "**- — < ^
ACETONE BLK
WATER BLK
CODE: FHA=Front half acetone wash BHW=Back half water(impinger contents + water wash) BHA-Back half
acetone wash FH TOTAL=Front half catch weight TOTAL-Total train catch weight
-------
CD
I
^>v p PARTICULATE SAMPLE ANALYSES Analyst
Plant \V (^"f -y N, v.TCOi?( Sampling Location *"3 LL| ^ i-V.-jOU duJ/'?^/
iV^v Date 11-3- 17
Run /? / t-
Test Date \rv3LVrr-~) c\ *" Test Period IVA.'VV-, \fv , -, ->' Stack/? Process/?
Beaker i Volume
FHA kW-Vj 2.^
FILTFR1 ? ^S^a'
FIITFB' #
FH TCTfj
Tare(l)
grams
loA. ''/a.TT''
.453;
T§FI^
10 3 ."73.T7
.if-g^l *
1
i
j
RHU ,
HHA j ' i
IflTAI !
I
Fi nal (\ )
qrams
OjL. 7t t-CL*
if ££3
• ^5"^^?'
A wt. Blk. Cor. Net wt.
qramS qrams qrams
.O385" -OOI^ .O.T75
-fx>*^K — ,Oo5<£
1 r-^
! r.£><+3i
1 V
Comments
Plant " vVrf. f ^^CvtCr-Alr>~lQ Test Period ih-^1^ V.N Vivv'-j -1^1 Stack/? Process/?
Beaker
FHA ?\o.-^
5 FILTER, rf 3£fiLt
fc FILTER' «
^ FH TOTAL
BHW
"• BHA
% TOTAL
Volume
mT
^5*0
1»U)
l^>5 "5U4-'7*'
y^V^ *
i
Tare (2)
g rams
lo'S'.<5u5"o
MSt^
'
Final (1)
grams
/os. '^167
<«»^8
Final(2)
a rams
/ OS. "> ^'-2
. Vt5^3 ""
A wt. jBlk. Cor. Net wt.
qrams j qrams qrams
"\O3lS : ^OO/*? rC)^.*!^
*o/o*/ ~~ -Q/dxS'*
i :
i
j
K»o*/c>3
* Comments ^
^ ^ f , -^L a , 4,-f
Plant virr> f t^rK, Vt>VP'iv: Sampling Location -> v \{Tir?hi-f\f ! CXtP?.T Run /? -^
Test Date ln-A'o-l<^\ Test Period it> - ^
i o3. ^0^9 •*
.Vi"AT
Tare (2)
grams
10 'i .^OH*1?
,¥-ti^T •*
i
Final (1) '
qrarfis
1 03 . »3§o
i5(o~l
Final (2)
grams
*" /OT3- $ ^.?r">
. t/£6>3- *•
i
i t
i
1
,
:
Awt. iBlk. Cor. |Net wt.
qrams qrams qrams
-0.2.S/! ,000*1 .na~7S
-OQ3*T — ,OO35
'. i
i
/T.O3O"
VL
Comments
ACETONE BLK
WATER BLK
\
CODE: FHA=Front half acetone wash BHW=Back half water(impinger contents + water wash) BHA-Back half
-------
ANALYTICAL DATA
PLANT
OATE_
c-e/vtiA
SAMPLING LOCATION G &[Z?uj
SAMPLE TYPE
RUN NUMBER
P/1&T'lciA£-Al=&
SAMPLE BOX NUMBER
CLEAN UP
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTtR NUMBER
CONTAINER 00 00 3
CONTAINER ^OP/
LABORATORY RESULTS
lp me
FRONT HALF SUBTOTAL
."I
.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 _/2L.
INITIAL VOLUME
NET VOLUME
.ml
ml
ml
SILICA GEL
FINAL WEIGHT *?;<,.<, t
INITIAL WEIGHT _2^^— g
NET WEIGHT ^L- I
CONTAINER ______
ETHER-CHLORCFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
.mg
.mg
mg
TOTAL WEIGHT
LJf f O
/"^v • _> mj
TOTAL MOISTURE
/y.6
SUBTOTAL
B-7
-------
ANALYTICAL DATA
PLANT 'A
OAFE_
SAMPLING LOCATION
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
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 _/f_£_ ml
INITIAL VOLUME '¥%L- ml
ml
COMMENTS:
LABORATORY RESULTS
CONTAINER
CONTAINER
L
FRONT HALF SUBTOTAL
CONTAINER ______
ETHER-CHLOROFORM
EXTRACTION
."I.
BACK HALF SUBTOTAL
.mpfci,
TOTAL WEIGHT
JIM
SILICA GEL
FINAL WFIGHT T!
INITIAL *FJf.HT 2c
NET WFIGHT '
f f
>0 e -j
** , t
SlIBTnTAI 1$' 5
TOTAL MOISTURE
B-8
-------
ANALYTICAL DATA
PLANT y4#/.^\_.f.
DATE_ y?/jL6
SAMPLING LOCATION
SAMPLE TYPE _
RUN NUMBER
SAMPLE BOX NUMBER
CLEAN UP MAN
/
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
CONTAINER 000/7
LABORATORY RESULTS
.•£ mg
CONTAINER
FRONT HALF SUBTOTAL
.fflg
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
OISTURE
CONTAINED
ETHER-CHLOROFORM
EXTRACTION
BACK HALF SUBTOTAL
TOTAL WEIGHT
IMPINGERS
FINAL VOLUME .
INITIAL VOLUME .
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
J_^Q...... ml
—-2 m|
,'J/t) 8
.2oO t
so f
t
,'g
I
SUBTOTH . tf
.mg
.mg
.mg
TOTAL MOISTURE
B-9
-------
ANALYTICAL DATA
PLANT.
DAFE_ .
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
SAMPLE BOX NUMBER
CLEAN UP MAN _
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS). CONTAINER.
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER J2L2_LL__ "^^^^^ CONTAINER
LABORATORY RESULTS
FRONT HALF SUBTOTAL
-
BACK HALF
. IMPINGER CONTENTS AND WATER WASH OF
IMPINGERS. CONNECTORS. AND BACK
HALF OF FILTER HOLDER
ACETONE WASH OF IMPINGERS. CONNECTORS.
AND BACK HALF OF FILTER HOLDER
CONTAINER _______
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
TOTAL WEIGHT
.Big
ntf
_mfi|
MOISTURE
IMPINGERS
FINAL VOLUME JfL& ml
INITIAL VOLUME _2:'£i_L_ ml
NET VOL I IMF ~7- . ml
SILICA GEL
FINAL WFICiHT 3-1° g
INITIAL WFIGHT GS-Pfi..,,.- R
NET WEIGHT 1$ .. I
, 8
8
|
SUBTnTH
TOTAL MOISTURE
He.
B-JO
-------
ANALYTICAL DATA
•_ Aj±K*
PLANT
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
1*
CONTAINER
O 9
FRONT HALF SUBTOTAL
.mg
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
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
TOTAL WEIGHT
IMPINGERS ^
FINAL VOLUME _r±.-_T_
INITIAL VOLUME -££0
NET VOLUMF P
SILICA GEL -)/.
FINAL WFIGHT ^ ,?•
INITIAL WEIGHT ^***A.
NFT WFIfiHT f(sf
_ml
_ml
? t t •
K .8
SUBTOTAL _
_mg
mg
mg
TOTAL MOISTURE.
-------
ANALYTICAL DATA
PLANT_ _
SAMPLING LOCATION.
SAMPLE TYPE
RUN NUMBER
CfU&)
>
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
N
_mg
.mg
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
CONTAINER _______
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
TOTAL WEIGHT
.mg
.m
^OiSTURE
IMPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
-I "I
ml
ml
222-
t
."8
.g
TOTAL MOISTURE
SUBTOTAL
B-12
-------
ANALYTICAL DATA
PLANT r>e, o-ia«-v >..
DATE Ikl^S-l"
SAMPLING LOCATION
SAMPLE TYPE _
RUN NUMBER L
SAMPLE BOX NUMBER
CLEAN UP MAN jfeJS
COMMENTS:
cj.jft VvVl -..5 Ju- rA
-------
ANALYTICAL DATA
PLANT.
OATE_ . .10-
SAMPLING LOCATION Cr^,, V-^ f ^-.e,
^^^ /
SAMPLE TYPE 7*^- ;
RUN NUMBER
SAMPLE BOX NUMBER
-O
CLEAN UP MAN V-. x
>:XQ
'fV '" .i
COMMENTS:
t »a ** i.
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
( Q o OH ^ ")
CONTAINER
LABORATORY RESULTS
CONTAINER »O £»«*»«-/
FRONT HALF SUBTOTAL
.nig
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 _2j2.'±_ ml
INITIAL VOLUME _^°2_ ml
ml
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT _C
NET WEIGHT
21 v^ . ! e
) 00 . e
'"?!> R
j
g
£
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
TOTAL WEIGHT
.nig
.m(!
.mj
TOTAL MOISTURE "1. i
SUBTOTAL
-------
ANALYTICAL DATA
PLANT_ /•i.'.jLi-.ir'.J.
DATE_ l^\^L.
SAMPLING LOCATION jLj___
SAMPLE TYPE _J±U±__
RUN NUMBER 3
e
SAMPLE BOX NUMBER
CLEAN UP MAN L—
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER ~3 f
COMMENTS:
CONTAINER
CONTAINER
LABORATORY RESULTS
a,
a.og/,8
mg
FRONT HALF SUBTOTAL
•V 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
ml
g
:i
.t
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
.mg
BACK HALF SUBTOTAL
me
TOTAL WEIGHT
TOTAL MOISTURE [3 «
SUBTOTAL
B-15
-------
ANALYTICAL DATA
PLANT _
DATE
SAMPLING LOCATION hZ
SAMPLE TYPE
RUN NUMBER _
SAMPLE BOX NUMBER
CLEAN UP MAN T>
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
CONTAINER.
CONTAINER
LABORATORY RESULTS
S>. I
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 _£OOO_3
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
TOTAL WEIGHT
_J9K
_Wig
nfc
IflR
MOISTURE
IMPINGERS
FINAL VOLUME
INITIAL VOLUME JLc<2
NET VOLUME - £
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
ml
ml
ml
' ''
1*9°
I
.8
.8
TOTAL MOISTURE / 4?
SUBTOTAL
-------
ANALYTICAL DATA
PLANT.HMi^
DATE, 10-7-5"-1*7
SAMPLING LOCATION L'<
SAMPLE TYPE _
RUN NUMBER 2r.
SAMPLE BOX NUMBER
CLEAN UP MAfTTT
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
CONTAINER.
CONTAINER
LABORATORY RESULTS
» i me
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
O O
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
TOTAL WEIGHT
.mi
jng
MOISTURE
IMPINGERS
FINAL VOLUME JL£2JL_ ml
INITIAL VOLUME ^&Q— ml
NET VOLUME - J— ml
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT 200
NET WEIGHT
8
g
t
.1
• I
SUBTOTAL
TOTAL MOISTURE
- 7
B-17
-------
ANALYTICAL DATA
PLANT JTlS^&f:
DATE _ ip-.ar
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
SAMPLE BOX NUMBER
CLEAN UP MAN 1NJ& '
- 6PF)
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 ^£O_l£
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
jug
J»g
TOTAL WEIGHT
^•7 . 5" JK
MOISTURE
IMPINGERS
FINAJ , wm.iiMP ^'->,.
INITIAL VOLUME _2^>.^
NFT VOI IIMF , ? 3
SILICA GEL -, . ,
P1NAL aif ir.HT *-!'•
INITIAL ffFIRHT ,2^),^,,.
NFT WFIdHT '-3,,,
ml
ml
ml
f
t
f
t
"I
g
SUBTOTAL .
TOTAL MOISTURE
I
B-18
-------
ANALYTICAL DATA
PLANT_
OATE_
SAMPLING LOCATION-
SAMPLE TYPE
RUN NUMBER ___y_
SAMPLE BOX NUMBER
CLEAN UP MAN '
_
Bg.
.CL
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
^87/3
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
rnMTAiMFa
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
BACK HALF SUBTOTAL
.nig
.nig
mg
TOTAL WEIGHT
2)87,3
mj
MOISTURE
IMPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
"•
ml
ml
° . /
TOTAL MOISTURE
f ? . [
SUBTOTAL
B-19
-------
ANALYTICAL DATA
PLANT
SAMPLING LOCATION TX Is D'L» *»./•> 3
-------
ANALYTICAL DATA
PLANT _,
DATE-./p'v^::
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER.
3
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
S14I.3
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 WFIGHT
Riff
ing
me
2V/.3 mt
MOISTURE
IMPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
ml
ml
ml
TOTAL MOISTURE
SUBTOTAL
B-21
-------
ANALYTICAL DATA
PLANT, rr.
OATE_
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER L
SAMPLE BOX NUMBER
CLEAN UP MAN '.
-19
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
CONTAINER
Q
CONTAINER O
LABORATORY RESULTS
^ "7
FRONT HALF SUBTOTAL
' Q mt
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
-J«
IM
TOTAL WEIGHT
¥3 r /
MOISTURE
IMPINGERS
FINAL VOLUME _Jr.2-2_ ml
INITIAL VOLUME 2<3«2__ ml
NET VOLUME £— ml
2.0?
SILICA GEL
FINAL WEIGHT ^T I
INITIAL WEIGHT Lo° I
NET WEIGHT 2- I
SUBTOTAL
TOTAL MOISTURE
B-22
-------
ANALYTICAL DATA
PLANT. rOUy
DATE.. (0- .2.0-75
SAMPLING LOCATION _JLi
SAMPLE TYPE
RUN NUMBER _
- \C,Pfl
SAMPLE BOX NUMBER
CLEAN UP MAN
COMMENTS:
FRONT HALF
ACETONE WASH OF NOZZLE. PROBE. CYCLONE (BYPASS).
FLASK. FRONT HALF OF FILTER HOLDER
FILTER NUMBER
I
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
MMfaiMPR 1
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
JH8
BACK HALF SUBTOTAL
me
TOTAL WEIGHT
MOISTURE
IMPINGERS
FINAL VOLUME
INITIAL VOLUME
NET VOLUME
SILICA GEL
FINAL WEIGHT
INITIAL WEIGHT
NET WEIGHT
ml
ml
e
,"8
.8
SUBTOTAL
TOTAL MOISTURE
B-23
-------
ANALYTICAL DATA
PLANT _F~tV
DATE _ . 'C
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER _
TPti
3 Q
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 RESULT^il
« &*
me
3.S
FRONT HALF SUBTOTAL
.•rt
BACK HALF
. IMPING ER 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
201
SUBTOTAL
CONTAINER
ETHER-CHLOROFORM
EXTRACTION
CONTAINER.
.mg.
BACK HALF SUBTOTAL
me
TOTAL WEIGHT
TOTAL MOISTURE
-------
ITLE
Project No.
Book No.
* 2
-------
Witnessed 8 Understood by me.
Date
Invented by
Recorded by
Date
-------
ITLE
Project No.
_ Book No.
Page No.
r\ \*ef
^5.
fabU
ML
|V3ft
_aia
i
/£?/
Jb
15U3i
V
yfer;
is zc>
0^3
.c
0C5T
/76
.n
,0^^
fl
£&
inoS
opg?
re
03 r
loV
n
ikaisu
•J5_2
O
,1
J
.'i»5ft
1SL5
Of
__A
^
• S1
__a
LJL
a.
3
0|
T
L
t
'f
_^_if.
7
(r'Ti
iSao,
I9P_1
15-
JilLfe
o
To Page No.
Witnessed & Understood by me.
Date
Invented by
Recorded by
B-Zy
Date
-------
WMn
n,;ed & Undcrstoo.-.! by nu\
Date
Invented by
Recorded by
B-28
Date
-------
Wiifi'-.sed 8. Understood by me.
-------
York Services 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 P. Weston, Inc.
Weston Way
West Chester, PA 19380
Reference: TRACE ELEMENT ANALYSIS OF PARTICULATE 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:
#37695 - Anaconda - #1 & #2 - Crusher Baghouse Inlet, Run 1,
10/25/79 WESTON #00006
#37696 - Anaconda - Primary Crusher Hoop, Run 1, 10/25/79
WESTON #00008
#37701 - Anaconda - Front Half Acetone Grizzly Crusher, Run 1,
10/25/79
#37703 - Anaconda - Front Half Aceton #3 & #4 Baghouse Inlet,
Run 1, 10/26/79
Please contact Mr. Robert Bradley, if you have any questions.
Sincerely,
MD/mdf
cc: Dennis Holzschuh
Roger Kniskern
Robert Bradley
Maria Denaro
Project Scientist
B -30
A Subsidiary of York Research Corporation
-------
et
BS
CASLC ADDRESS "LEDOUX TEANECK"
TELEX 134340
£j,.*\ 359 Alfred Avenue. Teaneck. New Jersey 07'J66 • Telephones: 2t->g47
I INDEPENDENT CONTROL. AND RESEARCH CHEMISTRY. INSTI1UMENTAL AND CHEMICAL ANALYSIS • SAM?LINC.
WEIGHING. SHIPPEilS' REPRESENTATION. BENEf ICIATIDN. AND STORAGE OF ORES A.'iO METALS
REPORT OF ANALYSIS
Ootobcr 31f 1980
Our analysis of the sample of DUST SAMPLES
From York Research Corporation
Marked: 15 Samples as below P.O. #3-5830
and
... .-..,: •-.•• > ••; PARTS. PER. MILLION
-.".'•'•'."»" -v • "' :. .37695
URANIUM
THORIUM
: BISMUTH- —
LEAD r
;. THALLIUM
MERCURY
GOLD
PLATINUM
IRIDIUM
OSMIUM
RHENIUM
TUNGSTEN
TANTALUM
HAFNIUM
LUTETIUM
YTTERBIUM
THULIUM
ERBIUM
HOLMIUM
DYSPROSIUM —
TERBIUM
GADOLINIUM —
EUROPIUM ~—
SAMARIUM
NEODYMIUM
PRASEODYMIUM
'5v
50 ..
<0.2
<1.
<0.2
<1.
<0.2
<1.
2.
<1.
<1.
<1.
20.
submitted to us, shows:
37696
10.
•200.
500.
<1.
<2.
<0.2
<1.
<0.2
<1.
<0.2
<1.
<0.2
2.
<1.
2.
5.
5.
To York Research Corporation
PAGE 4 of 12 PAGES
B-31
LEDOUX & COMPANY
NO WARRANTY IS EXTENDED IN RESPECT TO SERVICES PROVIDED BY L2DOUX & COMPANY
-------
CAHLE ."..'•l.Kv
BS
SS ••UEr.'O"X Tr.--.NECK"
TF.UEX 134340
359 Alfrr..! Avenue. Teaneck, New Jersey 07666 • Telephones:
t INDm NOENf CON1SOI. AM) Ber.EftRCH HME'.tiSTRY. INSTRUMErUAl AfJfc CHEMICAL ANALYSIS • S^^i'LINC.
I WEIGHING SlllfPEHV REPREStNTATIUM BENEFIC1/.TION. AND CTOKACE OF ORES AN3 MHALS
REPORT OF ANALYSIS
No.
1 QfiD
Our analysis of the sample of DUST SAMPLES
From York Research Corporation
Marked: 15 samples as below P.O.#3-5830
and submitted to us, shows:
PARTS PER MILLION .
:j 37695 37696
CERIUM • 10. 20.
LANTHANUM 1- 10. 20.
BARIUM - 500. 200.
CESIUM '• 2. 2.
IODINE 1. 1.
TELLURIUM — ' ' <1. <1. .
ANTIMONY • 20. 50. '
TIN • <1. <1.
INDIUM = <2. <2.
CADMIUM <2. <2. • .
SILVER 5. 10. •
PALLADIUM : <2. <2.
RHODIUM <1. <1.
RUTHENIUM ~ • <2. <2.
MOLYBDENUM <2. <2.
NIOBIUM — 10. 5.
ZIRCONIUM . 2. 200.
YTTRIUM 10. 5.
STRONTIUM — 100. 50.
RUBIDIUM 10. 20.
BROMINE , 10. <0.5
SELENIUM <0.5 <0.5
ARSENIC 500. 500.
GERMANIUM <2. <2.
GALLIUM 5. "5.
ZINC 200. 1000.
*0
•r
To
York Research Corporation
PAGE 5 of 12 PAGES
B-32
LEDOUX & COMPANY
WO WARRANTY IS EXTENDED IN RESPECT TO SERVICES PROVIDED BY LEDOUX 8t COMPANY
(PJ.EASE SEfJ REVERSE SIDE)
-------
No. 1014_2_1_5.
BS
CABLE ADDRESS "t-EDOUX TEANECK"
TELEX 134340
359 Alfred Avenue, Tcaneck, New Jersey 07666 • Telephones: *
lv '
I ISOEPENOENrCDNTHOl. AND RESEARCH CHEMISTRY. INSTRUMENTAL AND CHEMICAL ANALYSIS • SAMPLING.
I WEIGHING. SHIPPERS REPRESENTATION, BEhEFICIATION. AND STORAGE OF ORES AND METALS
REPORT OF ANALYSIS
October'?!. 1Q80
Our analysis of the sample of DUST SAMPLES
From York Research Corporation
Marked: 15 Samples as below P.0.# 3-5830
"•
COPPER
NICKEL
COBALT . —
IRON
MANGANESE
CHROMIUM
VANADIUM
TITANIUM
SCANDIUM
CALCIUM
POTASSIUM
CHLORINE
SULFUR
PHOSPHORUS
SILICON
ALUMINUM
MAGNESIUM
SODIUM
FLUORINE
CARBON
BORON
BERYLLIUM —
LITHIUM
and
" PARTS PER MILLION
.= •... ' 37695
M-
•• 50.
.5..
.. _— . M
— — M
50.
100.
M
10.
500.
M
2 .
. . M
500.
M
M
A
M .
— 10 .
100.
A
i n
submitted to
1. .37696 , .
- M . . .
" 50.
: 2. ' - •
M ' '
200. :
10.
100.
M
5.
1000.
M
2.
M
200.
M
M
A
1.
5. .
50.
A .
us, shows:
5.
To
A. Matrix Interference
M. Signifies Major Constituent of Sample
»
York Research Corporation.
PAGE 6 of 12 PAGES
B-33
LEDOUX & COMPANY
MO WARRANTY IS EXTENDED IN RESPECT TO SERVICES PROVIDED BY LEDOUX & COMPANY
tot
-------
CAULE AUDREYS "LKSOOX TEANECK"
TELEX 134340
No.__1Q14215
35V Alfred Avenue, Teaneck, New Jersey 07666 • Telephones:
INDEPENDENT CONTROL. AND RESEARCH CHEMISTRY.IHSTRUMENTAL AND CHEMICAL ANALYSIS • UMPLI1C.
WEIGHING. SHIPPERS1 REPRESENTATION. BENEFICIATION. AND STORAGE OF OR£S ANO METALS
REPORT OF ANALYSIS
October 31, 1980
Our analysis of the sample of ous^ Samp les
From York Research Corporation
Marked: 15 Lots as Below P.O.#3-5830
-URANIUM •—
THORIUM
.BISMUTH'----
LEAD
, THALLIUM •
.MERCURY------
GOLD —
PLATINUM
IRIDIUM
OSMIUM
RHENIUM
TUNGSTEN
TANTALUM
HAFNIUM
LUTETIUM
YTTERBIUM
THULIUM
ERBIUM
HOLMIUM
DYSPROSIUM —
TERBIUM
GADOLINIUM —
EUROPIUM
SAMARIUM
NEODYMIUM
PRASEODYMIUM
•-- PARTS PER MILLION
submitted to us,shows:
#37703, -.-..::"
•iooo.-':-:V:;:^ • •••;': .>.;;\;;'
106., '.,.-.. \, .: . -
<0.2
<1.
<0.2
<1.
<0.2
<1.
<0.2
20.
5.
To
Page 7 of 12 Pages
York Research Corporation
LEDOUX & COMPANY
NO WARRANTY IS EXTENDED IN RESPECT TO SERVICES PROVIDED BY LEDOUX & COMPANY
toi c f. r-c rcc r>c\/cor-c .nnei. ---
-------
t. ./ S-J •- ' '*-
C^.UL". An
.
i - •' \;
Jo w
••e.iooux T^/
TELF.X 1
LM
A-j / >•• '« 359 AlfreJ A vemie,.Tc,weck, New Jersey 07666 . Telephones:
u«f\*^** »
2°
CONTiTOL. AT;0 RtSEARCll CHEMISTRY, INSTRUMENTAL AMU CHEMICAL ftffACYSIS *
WEICHIUU. 5HI?P£R,r RCPilCSENTATION. BEfJEFICIATlOn. A.M) STORAGE OF GAES A^O
REPORT OF ANALYSIS
NO. _!°JA2ll
October 317 1980
Our analysis of the sample of Oust Samples
From York Research Corporation
Marked:
15 Lots As Below
CERIUM
LANTHAMUM
BARIUM
CESIUM
IODINE
TELLURIUM
ANTIMONY
TIN
INDIUM
CADMIUM
SILVER
PALLADIUM
RHODIUM
RUTHENIUM
MOLYBDENUM
NIOBIUM
ZIRCONIUM
YTTRIUM
STRONTIUM
RUBIDIUM
BROMINE
SELENIUM
ARSENIC
GERMANIUM
GALLIUM
ZINC
P.O.* 3-5830
and submitted to
PARTS PER MILLION •
•--•' #37703
us, shows:
20.
20.
1000.
20.
20.
50.
10.
200.
100.
<0.5
<0.5
100.
100.
Page 8 of 12 Pages
To York Research Corporation
LEDOUX & COMPANY
B-35
NO WARRANTY IS EXTENDED I?J RESPECT TO SERVICES PROVIDED 3Y LEDOUX & COMPANY
(PLEASE SEE RCVZRSZ SIDE)
-------
CABLE ADDRESS "LEDOUX TEANECK'
TELEX 134340
S 3SV Alfred Avenue, Teaneck. New Jersey 07666 . Telephones:
I INdfPENDENT CONTROL. AMD RESEARCH CHEMISTRY. INSTRUMENTAL ANO CHEMICAL ANALYSIS • SAMPLING.
I AEIGHING. SHIPPERS' REPRESENTATION. BENEFICIATION. MO STORAGE OF ORES AND METALS
REPORT OF ANALYSIS
No..
1014215
October 31, 1980
Our analysis of the sample of . . _ ,
^ Dust Samples
I-rom York Research Corporation
Marked: 15 Lots Ag Be|>QW p.0.#3-5830
and submitted to
us, shows:
PARTS PER MILLION
#37703
COPPER : M
NICKEL -, 20.
COBALT 20.
IRON — M
MANGANESE 500.
, CHROMIUM " 200.
VANADIUM 100.
TITANIUM M
SCANDIUM '• 5..
CALCIUM M
POTASSIUM M
CHLORINE 20.
SULFUR . 1000.
PHOSPHORUS 200.
SILICON M
ALUMINUM M
MAGNESIUM A
SODIUM 1000.
FLUORINE , ' 10.
CARBON
BORON 200.
BERYLLIUM • A
LITHIUM 50.
* * #
A = Matrix Interference
M.Signifies Major Constituent of Sample
Page 9 of 12 Pages ,
York Research Corporation
LEDOUX & COMPANY
B-36
NO WARRANTY IS EXTENDED IN RESPECT TO SERVICES PROVIDED BY LEDOUX 3t COMPANY
/nr c A or? r-~tr
-------
BS
CASLE ADDRESS "LEOOUX TEANECK"
TELEX 134340
TJ y
-------
BS
CAC'_S AODREOS "LEDGUX TEANcCK"
TELEX 134340
I?W>-S 359 Alfred Avenue: Teaneck, New Jersey 07666 • Telephones: *^
I INDEPENDENT CONTROL. AND RESEARCH CHEMISTRY. INSTRUMENTAL AND CHEMICAL ANALYSIS • SAMPLING.
I WEIGHING. SHIPPERS- REPRESENTATION. BE»EFICIATIOM, AND STORAGE OF ORES AND METALS
REPORT OF ANALYSIS
No.
' October 31. 1980
Our analysis of the sample of DUST SAMPLES
From York Research Corporation
Marked: 15 Samples as below P.O. #3-5830
CERIUM
LANTHANUM -
BARIUM.
CESIUM
IODINE
TELLURIUM -
ANTIMONY —
TIN
INDIUM
CADMIUM
SILVER
PALLADIUM -
RHODIUM
RUTHENIUM -
MOLYBDENUM
NIOBIUM
ZIRCONIUM -
YTTRIUM
STRONTIUM -
RUBIDIUM —
BROMINE
SELENIUM —
ARSENIC
GERMANIUM -
GALLIUM
ZINC
and submitted to
PARTS PER MILLION
us, shows:
^
37701
50.
20.
1000.
2.
10.
<1.
2.
<2.
20.
10.
5.
20.
20.
200.
<0.5
10.
<0.5
500.
<2.
5.
20.
To
York Research Corporation
PAGE 11 of 12 PAGES
B-38
LEDOUX & COMPANY
,•<•/ .
(,•! ///. ' /.:*,"#•••
NO WARRANTY IS EXTENDED IN RESPECT TO SERVICES PROVIDED BY LEDOUX & COMPANY
iai c/i oc cere. OO/CDCC
-------
TELEX 134340
j ^ 359 Alfred Avenue. Teancck. New Jenev 07666 • Telephones:
•,-:J ' *'
f
I INDEPENDENT'CONTHOL. AND RESEARCH CHEMISTRV. INSTRUMENTAL AND CHSMICAL ANALYSIS • SAMPLING.
I Vr'UGHINC. SHIPPERS1 REPRESENTATION. BENEFICIATION. AND STORAGE OF ORES AhO METALS
REPORT OF ANALYSIS
October 31,-1980
Our analysis of the sample of DUST SAMPLES
From York Research Corporation
Marked: 15 Samples as below P.O. #3-5830
and
• ' •'•'•• • "• '••*••• "••••:••••••• -PARTS PER MILLION : "' :
'•"-'••'''•'•-•'COPPER"---------i—--•'• -•••-••-:
NICKEL •
• •-'vV.'v .COBALT .————— .:.;,.:;-,
• • • • • .-• • IRON.. — •—:—-—--— '-;..•": • '.'• . •". -'."-
'• ' ' •••"':-' -'MANGANESE- -----; ;•;••* . — - • -'. / /
•"" "" ' 'CHROMIUM—^ : ~—' " *
VANADIUM -'
TITANIUM
SCANDIUM
. CALCIUM
POTASSIUM
CHLORINE —-
SULFUR
PHOSPHORUS
SILICON
ALUMINUM
MAGNESIUM
SODIUM
FLUORINE
CARBON
BORON
BERYLLIUM
LITHIUM
*
A. Matrix Interference
M. Signifies Major Constituent of Sample
submitted to
us, shows:
. .37101
100.
M
10.
1000.
M
10.
M
500.
M
M
A
M
10.
200.
A
10.
^° York Research Corporation
PAGE 12 of 12 PAGES
B-39
LEDOUX & COMPANY
NO WARRANTY IS EXTENDED IN RESPECT TO SERVICES PROVIDED BY LEDOUX & COMPANY
{PLEASE SEE REVERSE SIDE)
-------
Appendix C
Sample Calculations
-------
SAMPLE CALCULATIONS
Test Run 3 Crusher Baghouse No. 1-2 Outlet Stack
1. Volume of dry gas sampled at standard conditions (68°F, 29.92
in. Hg) , dscf.
17.647 x Y x Vm x ( P, + -AH_ \
vm(std) = --
17.647 x 1.0362 x 69.108 x ! 24.04 ., 116 =59'65
V , v»
vm(std) =
(52 + 460
Where:
^m(std) = Volume of gas sample measured by the dry gas meter,
corrected to standard conditions, dscf.
i
V = Volume of gas sample measured by the dry gas meter at
meter conditions, dcf.
PL = Barometric pressure, in. Hg. .
i^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).°R/in. Hg.
Y = Dry gas meter calibration factor.
2. Volume of water vapor in the gas sample corrected to standard conditions, scf.
V , ., = (:D. 04707 x V ) + 0.04715 x W .
w(std) v we' wsg
= (0.04707 x 13.0) + (0.04715 x 13.0 ) = 1.22
Where:
V / .v = Volume of water vapor in the gas sample corrected to
standard conditions, scf.
V = Volume of liquid condensed in impingers, ml.
C-1
-------
w
wsg
0.04707
Weight of water vapor collected In silica gel, g.
Factor which includes the density of water
(0.002201 '.b/ml), the molecular weight of water
(18.0 Ib/lb-mole), the ideal gas constant
121.85 On. HgJ (ft3)/0b-mole) (°R)] ; absolute
temperature at standard conditions (528°R), absolute
pressure at standard conditions (29-92 in. Hg) , ffYml
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)j. absolute
temperature at standard conditions (528°R), absolute
pressure at standard conditions (29-92 in. Hg), and
453-6 g/lb, ft3/g.
3- Moisture content.
ws
w
(std)
w(std)
V
m(std)
Bws
Where:
Bws
1.22
1.22 +59.65
= .020
Proportion of water vapor, by volume, in the gas
stream, dimension less.
4. Mole fraction of dry gas.
M
1 - B
ws
M
1 - .020
0.980
Where:
Md
= Mole fraction of dry gas, dimensionless
5. Dry molecular weight of gas stream, Ib/lb-mole.
MWd = 0.440(%C02) + 0.320 (%02) + 0.280
+ % CO)
C-2
-------
MWd = (0.440 x 0.0 ) + (0.320 x 20.9) +[0.280 (0.0 + 79.1 )]
28.97
Where:
MW. = Dry molecular weight, Ib/lb-mole.
%CO« = 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 o (MW. x MA + [l8 (1 - Mj]
s ' d a I u d J
MWs = (28,97 x ,980) + [18 (1 - t980 )]
28.75
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.
s (avg) j
C-3
-------
-/•s • 85-*9 x .848 x .923 x —^~
,01 x
58.8
Where:
,- = Average gas stream velocity, ft/sec.
85.49 = Pitot tube constant, ft/sec X
"(lb/1b-mole)(in.Hg)"j
~(°R) (in. H20) _ "
C = Pitot tube coefficient, dimensionless.
Jip = Velocity head of stack gas, in H20.
T = Absolute gas stream temperature, R.
P = Absolute gas stack pressure, in. Hg.
8. Average gas stream'dry volumetric flow rates, dscf/min.
n 1058.8 x v x A x M. x P
Qs(std) ' 5 _J d s
0 1058.8 x 58.8x29.87 x .980 x 24.01
Mstd) ~ ( 73. + 460)
82,128
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. Hg)(min)
9- Isokinetic variation calculated from intermediate values, percent.
C-k
-------
17'316
V
m(std)
Vs x ' 9 x PS x
x (Dn)'
Where:
I
e
Dn
17-316
= 17.316 x 72,9 x 59.65
x .980 x ( ,197 )2
106,8
Percent of isokinetic sampling.
Total sampling time, minutes.
Diameter of nozzle, inches.
Factor which includes standard temperature (528°R),
standard pressure (29-92 in. Hg), the formula for
calculating area of circle
, conversion of
square feet to square inches ( 1M), conversion of
seconds to minutes (60), and conversion to
percent (100), (in. Hg) (in2) (mln) .
(°R) (ft2) (sec)
10. Particulate concentration, gr/dscf.
C. = 0.015432 x M.
V
1
Where:
Cl
Mt
0.015432
0.015432 x
m(std)
27.5
= .007
= Particulate concentration, gr/dscf.
= Total weight of particulate caught by train, mg.
= Conversion factor of gr/mg.
11. Particulate mass emission rate, Ib/hr.
PMR^
0.0085714 x C, x Qs(std)
0.0085714 x ,,007 x 82,128 = 5,01
C-5
-------
Where:
PMR = Participate mass emission rate, Ib/hr.
0.0085714 = Conversion factor relating minutes to hours (60), and
grains to pounds (7,000),(lb) (min)/(gr) (hr).
C-6
-------
Appendix D
Equipment Calibration Records
-------
Date fri. /! " /?'/*?
Barometric pressure, Pj, = Z2nin. Hg
Box No.
Dry gas meter Ho.
Orifice
manometer
setting,
AH,
in. H20
0.5
1.0
iJS
&.o
6.0
8.0
Gas volume
wet test
meter
»w»
ft3
5
5
W5~
10
10
10
Gas volume
dry gas
meter
vd«
ft3
J-JJ-. Ltl3
jvo - r/ ?
fio.rii
sv"3
fo.7ri
Temperature
Wet test
Meter
tw,
°F
65*
• / i *
fr*
W
fr^ °
Dry gas meter
Inlet
tdi.
°F
Outlet
tdo.
°F
Average
td.
°F
6/w' »'
*tf *
%• ^
^ ^
Time
e.
min
W.V3
?.'5,'>
7.?r
/3.?2
Average
Y
/.o/S
!.t>l^
1.0/7?
' •>!«/''
Wo1!
AH0
/.6fer/
/ .s-iwP
r?.c:^
r?.6^ f &
».M»/
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 Pfa (td + 460)
Vd(Pb + TT~fi7 (tw + 4601
AH9
0.0317 AH f(tw + 460) el2
— . 1 ~~ ~~~~~^-^~~ \
Pb (td * 460) L Vw J
Y = Ratio of accuracy of wet test meter to dry test meter. Tolerance = * 0.01
AH@ = 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-]
-------
Date
- /m
BOX No.
Barometric pres;
Orifice
manometer
setting,
AH,
in. H20
0.5
1.0
.^J^i B»
JM n^
6.0
8.0
Gas volume
wet test
meter
Vy/,
ft3
5
5
tar
10
10
10
sure, P|j = _.!in. Hg
Gas volume
dry gas
meter
ft3
r??;asa
$39. A3 A
£v?. 313
W3. 275
9cl'£jo
Dry gas meter
Temperature
Wet test
Meter
°F
Q
£f*
Ls ^f
6>tc
Dry gas meter
Inlet
°F
V/R
7^"
Jo,'^
"i/r"
Outlet
°F
tf^
a* 72.
vd
"/^
-------
Date
rvcr. n rrrr
Barometric pres;
Orifice
manometer
setting,
AH,
in. H20
0.5
1.0
2.S
&0
6.0
8.0
Gas volume
wet test
meter
5
5
S&JT
10
10
10
iff. 10
;ure, PL » ....in. Hg
Gas volume
dry gas
meter
V
l?Kqs$
C1I. 1ft
5"Tt» . 1
JT*'^ , U U
^J* ' 5 I/'W
Box
Dry gas meter
Temperature
Wet test
Meter
°F
6?^'
fc>V*
^y*
(fi°
Dry gas meter
Inlet
°F
10
V
^r?f
V»vfclf
Outlet
°F
10 +
^K1S
7S7? "'
*L ?7
Average
°F
^7'
T7"
95'°
Cjy*
No. /<3\<90
no.
Time
e.
min
W.99
^ 0 ^
A rt ^^
/g.«73
Average
Y
|.»W
W3S
f-wn1
* * Qf^-ft
,011',
AHp
/.*/>ff.r
;.^A7
. /,fy?f
i i.9r«/f
i.??Z7
Calculations
AH
0.5
1.0
2.0
4.0
6.0
8.0
All
AM
13.6
0.0368
0.0737
0.147
0.294
0.431
0.588
Y
Vw Pb (td + 460)
/ * 1 1 \ / \
I/ /r. . AH A ft. . ,,^ft\
vdlpb + n c) (tw + 4601
\ 1 J. O/ \ /
AH0
0.0317 AH f(tw + 460) e]2
1 1
Pb ltd + 460) L Vw J
Y s 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
D-3
-------
Barometric pressure, Pj, =•; _ in. Hg
Box No.
Dry gas meter Mo.
Orifice
manometer
setting,
AH,
in. )<20
0.5
1.0
*.f
$.0
6.0
8.0
Gas volume
wet test
meter
vw.
5
5
V&5"
10.
10
10
Gas volume
dry gas
meter
MM
$tn.'rf&
*••' v • w ^v™
jjjgjj "Aw
a&'3%
Temperature
Wet test
Meter
°F
(02*
W
tt£f
(of
Dry gas meter
Inlet
°F
Outlet
°F
Average
td.
°F
•' '" ?
7«^e7i' ^''
75Jj' ^
&z'rf
Time
e.
min
1330
?.v?
120
/3,5$
Average
Y
/.OOYJ
'.o&l
.flft
,93$
WT
AHp
/. P ?5"<2
;.^ //
-------
Date
.
Barometric pressure, Pj, « _ in. Hg
Box No.
Dry gas meter Mo.
Orifice-
manometer
setting,
AH.
in. H20
0.5
1.0
t.&
2<4>
6.0
8.0
- .
Gas volume
wet test
meter
Vw,
5
5
mr
10
10
10
Gas volume
dry gas
meter
ft3
SJ.P77
'•/2k • f 7?
•J?t^ 10 I
yiu-%'
!/&.'J7s!
— _ .
Temperature
Wet test
Meter
tw.
°F
W"
b2°
if?"
b>Jg
Dry gas meter
Inlet
°F
Outlet
°F
Average
°F
&' . '
7&
Time
e.
min
/2.ifO
1.1?
7,!f?
13.4$
Average
f.0012
Wl
fl?f
•W
,WJ
\.W13
I.V3 o3
i.qoss^
1,1 /?6"
;.«^1
Calculations
AH
0.5
1.0
2.0
4.0
6.0
8.0
All
13.6
0.0368
0.0737
0.147
0.294
0.431
0.588
Y
Vw Pjj (trf + 460)
vd(pb * TTT) (tw + 46°)
-
AH9
0.0317 AH Rtw + 460) el2
Pb (td + 460) L Vw J
•" ' .: .Vr .'7_ .:.. '.'
Y = Ratio of accuracy§of wet test meter to dry test meter. Tolerance » * 0.01
AH@ = 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-5
-------
Box No.
Barometric pressure,
in. Hg Dry gas meter No.
Orifice
manometer
setting,
AH,
in. l<20
Gas volume
wet test
meter
V"w»
ft3
Gas volume
dry gas
meter
Wet test
Meter
tw.
°F
Temperature
Inlet
_Dry_^as meter
Outlet
Average
td
°F
Time
e.
min
0.5
1.0 fO>
1.0
63
10
AT? - «.
.6177
6.0
10
8.0
10
Average
Calculations
&H
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 (td + 460)
\i 1 n i_ AH \ /^ , >i /-rt i
VdVb 13.6/ V w )
•
AH(J
0.0317 AH Rtw + 460)
Pb (td * 460) [ Vw
•r
j
Y = 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. H20. Tolerance - ± 0.15
D-6
-------
BY.
PROJECT.
SUBJECT.
DATE
1
L - O. 118
6 - O-/20
- (j,
•=• O. 235
^^^
.-<^~
D z 0,306
F - 0,3 (3
D-7
SHEET
W.O. NO.
/ne, /
ii
r 0375
o
6 r O - 5*00
- 0*55* f
.OF.
2ZT
- O-
-------
PITOTTUBE IDENTIFICATION NUMBER: T_
#UTC. / £
CALIBRATED BY:
DATE:
RUN NO.
1
2
3
"A" SIDE CALIBRATION
APstd
cm H20
(in. H20)
/.***
0-*r
0,^2-
A P(s)
cm H?0
(in. H£fl)
MS"
O.?o
o.^/4/
AVERAGE
Cp(S)
.f3f
.Pro
.fra
DEV.
. OlC.
H .ofb .o£l .?T3
DEV. = C|,(S) Cp(S)(avg.) (MUST BE £0.01)
Cp DIFFERENCE: Aavg - Bavg =
RUN' NO.
1
2
3
"B" SIDE CALIBRATION"
APstd
cm H20
(in. H20)
/,23
^•^r
<9.3»-
AP{s)
cm H20
(in. H20)
A74
0.
-------
PITOTTUBE IDENTIFICATION NUMBER: £_
CALIBRATED BY:
DATE:
RUN IMG.
1
2
3
"A" SIDE CALIBRATION
Afstd
cm H20
(in. H20)
{•**-
0'K
o/*i-
A l»(s)
cm H?Q
(in. H20)
/.If
•>1
0.^
AVERAGE
CH(S)
fS"*~
. tef
.s-ri
DEV.
. Of
RUN NO.
1
2
3
"B"SIDE CALIBRATION"
^Pstcl
cm H20
(in. H20)
A*3-D
-
-------
PITOTTUBE IDENTIFICATION NUMBER:
t-. fcnU? f JCt .
DATE:
CALIBRATED BY:
RUN NO.
1
2
3
"A" SIDE CALIBRATION
APstd
cm H20
(in. H20)
/•«
o. U"
o.S*.
<+ „,/.
AP(s)
cm H2fl
(in. H20)
/7?
.£f
.^/3
AVERAGE
Cp(S)
^P3Z
.K7
.KS
DEV.
RUN NO.
1
2
3
"B" SIDE CALIBRATION"
cm H20
(in. H20)
_/.?J
0.&C"
O."ST-
_ . *
cm Ii20
(in. H20)
/— ji?>
' * 0
. &9
• V*f
AVERAGE
Cp(S)
.^31
. pjTi"
.^r3
DEV.
0
DEV.» C,,(S) •_Cp(S)(avo.) (MUST BE £0.01} /
Cp DIFFERENCE: Aavg • Bavg s (MUST BE £ 0701)
Pitot tube calibration data.
D-JO
-------
PITOTTUBE IDENTIFICATION NUMBER: _L
CALIBRATED BY:
DATE:
'.(if/
7
RUN NO.
1
2
3
"A" SIDE CALIBRATION
APstd
cm H20
(in. HzO)
/ 3®.
A.<*<
0,3^
AP(s)
cm H?0
(in. H20)
/.Ft-
.^f/
O.V4/
AVERAGE
CP(S)
PS2.
.
-------
\oo
4-.H
-v-
2-
Cdlibranon Check: Nprnographg
Ixilioratory
V
l-t1 T.X T> 8 ^ •'., o <-. ,•--*
4,
-~79
<5 A^. *'. H-.
. V.
\ w,» .
(1) (* I:aclor Adjustment
Probe 1
Probe 2
Probc 3
C3dj = C-
(0.85)2
(2)
(0.85)2
= C( ).
Accuracy (+ \ 0 °/
(a) A'-faclor line. A// and Ap scales
Set
. 3
(0.8S)2
(0.85)2
= C
(0.85)2
( £
(0.85)2
^- )
Aline
A// Reading
i = 0.01 \-07_
, = 0.1 \0.0
Nomograph 1_ -7, Nomograph if
LOO
VA w
6.1
Ap
C
2.0
1.5
1.0
0.7
0.5
= 10.0:A//= 10.0
= 0.1: A// =1.0
(b) C. /j and A? scales
/>„ ', (°F)
0.5 2500
0.4 1 500
0.3 1000
0.25 500
0.2 200
4
\-X /"* T"v
"^L ^""Cii ^* ^x i^ /v r™
Ap=l.O -\-o-z. l.0*z. \.O(, 0.95 x-c
Ap = 0.1 O-\O"i O.\°^ o-v°S Q.\OO 0.
Ap=1.0 <5.o> 3.A ^ ^ Q _ .
Ap = 0.01 0.-lol OJoA Q^ot Q'^OI_ o
A// Readings
Ap i Nomograph 1_ -z, Nomograph -3^- l
0.02 0.^1 0.^^ Q^g\ o.Ag o.^
0.8 8-1 "S-t. S.b 1. o -g.i
0.1 0.31 O .TZ- O.^i o.^l o I
3-° ^-o ^-1 ^,S «
0.9 0.6^ 0.4.S o'. tC, ^L' , -> ^'1
VJ-V"« o.feT. o|
' \\7l-, ^ OVC
I
t
1
D-12
-------
Balances
Mettler Analytical Balances
Performance Data, Contd.
o
•
0
th=l
0 » ]
H51AM
HS4AR
HI*
H7IIAH
o
o
v.
<
it
;E=
C=
_-/
=a
1=
*
HJ11
K31S
HS42
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 signifi- - -
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.
-.' .'. rf^r -„*!
,'. ;.•»»'. '4? ^aSv.Ha j----'. _J[
Serviced by
INSTRUMENT CORPORATION
609-448-3000
DATE SCRIM. NO,
SERVICE*
TECHNICIAN J»
c/0<£" Ao^w^/t-Z i
Special Features
Alt Release System
Automatic Preweighlng
Optical Range Taring
Full Range Taring
Capacity
Weighing Range (g)
Taring in Optical Range (g)
Additional Tare Weight (g)
Total (g)
Precision. .
Standard Deviation (mg)
Readability -
Analog Scale- Est. (mg) • - •
Digital Reading Device-Direct (mg)
Optical Seal*
Range (mg)
1 Scale Div (mg)
1 Digital Step (mg)
Filling Guide
1 Scale Div (mg) . -•-
Built-in Weight* .
Set ot Wts (g)
Additional Tare Wt (g)
Accuracy Ea Wt Comb (mg)_ .
1 Digital Step (g)
Taring System * ~
Max Tare (g)
By Setting Optical Scale to Zero.(g)
By Use of Built-in Wts (g) -
Pan Dia x Bow H (cm)
Housing
UW(cm)- ••• -
" H (cm)
Chamber
LxW (cm)
H(cm)
Shp Wt (kg/n>)
Net Wt (kg)
Cat. No.
Ea
H7SAR
Economical student
model. Same as H72
ancept with ar release
system. Protective fea-
tures enable 2-year
warranty even in
school lab use.
^ir'l'*.feiii4rfji '^>;
*.'* ''£•• .V^;;&£:- > { - -(
0-160
160
±0.05
0.1
0-1000 _
10
0.1
100 ...
.159 . .
±0.25
1
159
159
8.9x18 -
. . 46x24 ^.-.:
41 --
17x20
20
18/40
11
1-909-78 AR
1195.00
1 -909-78 AR
D-13
-------
THE PENNSYLVANIA STATE UNIVERSITY
226 FENSKE LABORATORY
UNIVERSITY PARK. PENNSYLVANIA 16802
Center for Air Environment Studies - Area Code 814
865-1415
June 15, 1979
Mr. James W. Davison
Air Sampling Supervisor
Roy F. Weston, Incorporated
Weston Way
West Chester, Pennsylvania 19380
Dear Mr. Davison:
Five persons from your corporation attended the Visible
Emissions Evaluation Seminar at The Pennsylvania State University
on May 22-23, 1979. Following is a list of the attendees and
their performance:
Name Certified
C. Dobroski Yes
B. Jackson Yes
N. Kaufman No
T. Moxon Yes
J. O'Neill Yes
Certificates and letters will be mailed to each participant.
Sincerely,
sincerely, i
<5^oi^
Robert Jennings Heinsohn
Professor, Mechanical Engineering
and Project Director
RJH/mg
cc: Vern Irwin
D-l/j
-------
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
Jeffery D. O'Neill
Project Scientist
Gregory A. Celiano
Assistant Project Scientist
Charles Dobroski
Assistant Project Scientist
Theodore Moxon
.Senior Laboratory Technician
Andrew Watkins
Assistant Project Scientist
Nancy Goldberg
Chemist
Nancy Robertson
Laboratory Technician
David Ralston
Laboratory Technician
Robert Newton
Laboratory Technician
Vi rginia McGlincy
Laboratory Technician
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
econENVIRONoraics Division
econENVIRONomics Division
-------
Scott Stanley
Laboratory Technician
Thomas Fee ley
Laboratory Technician
Emily Zinser
Laboratory Technician
econENVIRONomics Division
econENVIRONomics Division
econENVIRONomics Division
E-2
-------
|