United States
Environmental Protection
Agency
Office of Air Quality
Planning and Standards
Research Triangle Park NC 27711
EMB Report79-MET-2
December
Air
Metallic Minerals
Emission Test Report
Climax
Henderson, Colorado
-------
Environmental Consultants
UNITED STATES ENVIRONMENTAL PROTECTION AGENCY
EMISSIONS MEASUREMENT BRANCH
MAIL DROP 13
RESEARCH TRIANGLE PARK, NORTH CAROLINA 27711
FINAL REPORT
EMISSION TEST PROGRAM: MOLYBDENUM ORE PROCESSING PLANT
CONDUCTED AT
CLIMAX MOLYBDENUM COMPANY
HENDERSON MILL
SILVERTHORNE, COLORADO
CONTRACT NO. 68-02-2819
TASK ASSIGNMENT 17
EPA PROJECT NO. 79-MET-2
YRC PROJECT NO. 01-9517-17
JANUARY 15, 1981
York Research Corporation
One Research Drive, Stamford, Connecticut 06906 • Telephone: (2033 325-1371 -TWX: 710-474-3947
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TABLE OF CONTENTS
LIST OF FIGURES iii
LIST OF TABLES vi
PREFACE xi
1.0 INTRODUCTION 1
2.0 SUMMARY AND DISCUSSION OF TEST RESULTS 9
2.1 Molybdenum Dryer
2.2 Primary Crusher/Rail Car Unloading
2.3 Pebble Screening and Milling
2.4 Coarse Ore Stockpiling, Tailings Disposal,
Truck Loading
2.5 Ore Samples
3.0 PROCESS DESCRIPTION 107
3.1 Process Description
3.2 Process Operation During Test
4.0 SAMPLING METHODS 116
4.1 Test Port Location and Sampling Point
Determination
4.2 Preliminary Measurements
4.3 Gas Composition
4.4 Particulate
4.5 Particle Size Distribution
V4.6 Opacity Measurement
4.7 Fugitive Emissions Frequency
4.8 Ore Samples
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TABLE OF CONTENTS (Con't)
5.0 ANALYTICAL METHODS 139
5.1 Particulate Samples
5.2 Particle Size Distribution Samples
5.3 Ore Samples
6.0 APPENDICES
6.1 Complete Computer Data Printouts
6.2 Field Data Sheets
6.3 Laboratory Data
6.4 Calibration Data
6.5 Sample Calculations
6.6 Method 22 - Visual Determination of Fugitive
Emissions from Material Processing Sources
6.7 Project Participants
6.8 Work Assignment
-11-
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LIST OF FIGURES
Figure 1-1
Figure 1-2
Figure 1-3
Figure 1-4
Figure 1-5
Molybdenum Dryer
Primary Crusher/Rail Car Unloading
Pebble Screening and Milling
Course Ore Stockpiling
Tailings Disposal Area
Page
2
3
4
5
6
Figure 2-0
Figure 2-1
Figure 2-2
Figure 2-3
Figure 2-4
Figure 2-5
Figure 2-6
Figure 2-7
Figure 2-8
Figure 2-9
Figure 2-10
Climax Molybdenum Product Dryer TP-1
Scrubber Inlet Particle Size Distribu-
tion - Test 2
Climax Molybdenum Product Dryer TP-1
Scrubber Inlet Particle Size Distribu-
tion - Test 3
Climax Molybdenum Product Dryer TP-2
Scrubber Outlet Particle Size Distri-
bution - Test 1
Sampling in Cyclonic Flow
Climax Molybdenum Primary Crusher TP-1
Transfer Point Exhaust Particle Size
Distribution - Test 1 - Sprays On
Climax Molybdenum Primary Crusher TP-1
Transfer Point Exhaust Particle Size
Distribution - Test 2 - Sprays On
Climax Molybdenum Primary Crusher TP-1
Transfer Point Exhaust Particle Size
Distribution - Test 3 - Sprays On
Climax Molybdenum Primary Crusher TP-2
Crusher Pit Exhaust Particle Size Dis-
tribution - Test 1 - Sprays On
Climax Molybdenum Primary Crusher TP-2
Crusher Pit Exhaust Particle Size Dis-
tribution - Test 2 - Sprays On
Climax Molybdenum Primary Crusher TP-2
Crusher Pit Exhaust Particle Size Dis-
tribution - Test 3 - Sprays On
Climax Molybdenum Primary Crusher TP-3
Scrubber Outlet Particle Size Distribu-
tion - Test 1 - Sprays On
19
20
23
28
32
33
34
37
38
39
42
-------
Figure 2-11
Figure 2-12
Figure 2-13
Figure 2-14
Figure 2-15
Figure 2-16
Figure 2-17
Figure 2-18
Figure 2-19
Figure 2-20
Figure 2-21
Figure 2-22
Figure 2-23
Climax Molybdenum Primary Crusher TP-1
Transfer Point Exhaust Particle Size
Distribution - Test 4 - Sprays Off
Climax Molybdenum Primary Crusher TP-1
Transfer Point Exhaust Particle Size
Distribution - Test 5 - Sprays Off
Climax Molybdenum Primary Crusher TP-1
Transfer Point Exhaust Particle Size
Distribution - Test 6 - Sprays Off
Climax Molybdenum Primary Crusher TP-2
Crusher Pit Exhaust Particle Size
Distribution - Test 4 - Sprays Off
Climax Molybdenum Primary Crusher TP-2
Crusher Pit Exhaust Particle Size
Distribution - Test 5 - Sprays Off
Climax Molybdenum Primary Crusher TP-2
Crusher Pit Exhaust Particle Size
Distribution - Test 6 - Sprays Off
Climax Molybdenum Primary Crusher TP-3
Scrubber Outlet Particle Size Distribu-
tion - Test 2 - Sprays Off
Climax Molybdenum Pebble Screening and
Milling TP-1 Screen Exhaust Particle
Size Distribution - Test 1
Climax Molybdenum Pebble Screening and
Milling TP-1 Screen Exhaust Particle
Size Distribution - Test 2
Climax Molybdenum Pebble Screening and
Milling TP-1 Screen Exhaust Particle
Size Distribution - Test 3
Climax Molybdenum Pebble Screening and
Milling TP-2 Bucket Elevator Exhaust
Particle Size Distribution - Test 1
Climax Molybdenum Pebble Screening and
Milling TP-2 Bucket Elevator Exhaust
Particle Size Distribution - Test 2
Climax Molybdenum Pebble Screening and
Milling TP-2 Bucket Elevator Exhaust
Particle Size Distribution - Test 3
54
55
58
59
60
63
75
76
77
80
81
82
-iv-
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Figure 2-24
Figure 2-25
Figure 2-26
Figure 2-27
Climax Molybdenum Pebble Screening and
Milling TP-2A Total Scrubber Inlet
Particle Size Distribution - Test 1
Climax Molybdenum Pebble Screening and
Milling TP-2A Total Scrubber Inlet
Particle Size Distribution - Test 2
Climax Molybdenum Pebble Screening and
Milling TP-2A Total Scrubber Inlet
Particle Size Distribution - Test 3
Climax Molybdenum Pebble Screening and
Milling TP-3 Scrubber Outlet Particle
Size Distribution - Test 1
Page
85
86
87
90
Figure 3-1
Flow Sheet - Henderson Mill
108
Figure 4-1
Figure 4-2
Figure 4-3
Figure 4-4
Figure 4-5
Figure 4-6
Figure 4-7
Figure 4-8
Figure 4-9
Figure 4-10
Figure 4-11
Figure 4-12
Molybdenum Dryer - TP-1 Sampling Point
Locations
Molybdenum Dryer - TP-2 Sampling Point
Locations
Primary Crusher - TP-1 Sampling Point
Locations
Primary Crusher - TP-2 Sampling Point
Locations
Primary Crusher - TP-3 Sampling Point
Locations
Pebble Screening and Milling - TP-1
Sampling Point Locations
Pebble Screening and Milling - TP-2
Sampling Point Locations
Pebble Screening and Milling - TP-2A
Sampling Point Locations
Pebble Screening and Milling - TP-3
Sampling Point Locations
Modified Particulate Sampling Train
Andersen Stack Sampler
Andersen Sampling Train
117
118
120
121
123
124
126
127
128
131
135
136
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LIST OF TABLES
Table 2-0
Table 2-1
Summary of Scrubber Removal Efficiency
Molybdenum Dryer - Adjustment of
Scrubber Removal Efficiency
Page
15
16
Table 2-2
Table 2-3
Table 2-4
Table 2-5
Table 2-6
Table 2-7
Table 2-8
Table 2-9
Summary of Emission Test Results -
Molybdenum Dryer TP-1 Combined Scrubber
Inlet, - English
Summary of Emission Test Results -
Molybdenum Dryer TP-1 Combined Scrubber
Inlet - Metric
Summary of Emission Test Results -
Molybdenum Dryer TP-2 Scrubber
Outlet - English
Summary of Emission Test Results -
Molybdenum Dryer TP-2 Scrubber
Outlet - Metric
Summary of Opacity Measurements -
Molybdenum Dryer - TP-2 - Scrubber
Outlet
Summary of Opacity Measurements -
Molybdenum Dryer - TP-3 - Dryer Area
Summary of Fugitive Emission Observa-
tions - Molybdenum Dryer TP-3 Dryer
Area
Particulate Radioactivity Analysis -
Molybdenum Dryer
17
18
21
22
24
25
26
27
Table 2-10
Table 2-11
Table 2-12
Table 2-13
Primary Crusher - TP-1 - Transfer Points
Exhaust Duct - Sequence of Train Processing
During Sampling - Sprays On 29
Summary of Emission Test Results -
Primary Crusher TP-1 Transfer Points
Exhaust Duct - Sprays On - English 30
Summary of Emission Test Results -
Primary Crusher TP-1 Transfer Points
Exhaust Duct - Sprays On - Metric 31
Summary of Emission Test Results -
Primary Crusher TP-2 Crusher Pit
Exhaust Duct - Sprays On - English 35
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Page
Table 2-14
Table 2-15
Table 2-16
Table 2-17
Table 2-18
Table 2-19
Table 2-20
Table 2-21
Table 2-22
Table 2-23
Summary of Emission Test Results -
Primary Crusher TP-2 Crusher Pit
Exhaust Duct - Sprays On - Metric
Summary of Emission Test Results -
Primary Crusher TP-3 Scrubber
Outlet - Sprays On - English
Summary of Emission Test Results -
Primary Crusher TP-3 Scrubber
Outlet - Sprays On - Metric
Summary of Opacity Measurements -
Primary Crusher - TP-3 - Scrubber
Outlet - Sprays On
Summary of Opacity Measurements -
Primary Crusher - TP-4 - Transfer
Point Hoods - Sprays On
Summary of Fugitive Emission Observa-
tions - Primary Crusher TP-4 Transfer
Point Hoods - Sprays On
Summary of Opacity Measurements -
Primary Crusher - TP-5 - Rail Car
Unloading - Sprays On
Summary of Fugitive Emission Observa-
tions - Primary Crusher TP-5 Rail Car
Unloading - Sprays On
Summary of Opacity Measurements -
Primary Crusher - TP-6 - Crusher
Building - Sprays On
Summary of Fugitive Emission Observa-
tions - Primary Crusher TP-6 Crusher
Building - Sprays On
36
40
41
43
44
45
46
47
48
49
Table 2-24
Table 2-25
Table 2-26
Primary Crusher - TP-1 - Transfer Points
Exhaust Duct - Sequence of Train
Processing - Sprays Off 50
Summary of Emission Test Results -
Primary Crusher TP-1 Transfer Points
Exhaust Duct - Sprays Off - English 51
Summary of Emission Test Results -
Primary Crusher TP-1 Transfer Points
Exhaust Duct - Sprays Off - Metric 52
-vii-
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Page
Table 2-27
Table 2-28
Table 2-29
Table 2-30
Table 2-31
Table 2-32
Table 2-33
Table 2-34
Table 2-35
Table 2-36
Table 2-37
Table 2-38
Summary of Emission Test Results -
Primary Crusher TP-2 Crusher Pit
Exhaust Duct - Sprays Off - English
Summary of Emission Test Results -
Primary Crusher TP-2 Crusher Pit
Exhaust Duct - Sprays Off - Metric
Summary of Emission Test Results -
Primary Crusher TP-3 Scrubber Outlet -
Sprays Off - English
Summary of Emission Test Results -
Primary Crusher TP-3 Scrubber Outlet -
Sprays Off - Metric
Summary of Opacity Measurements -
Primary Crusher - TP-3 - Scrubber
Outlet - Sprays Off
Summary of Opacity Measurements -
Primary Crusher - TP-4 - Transfer
Point Hoods - Sprays Off
Summary of Fugitive Emission Observa-
tions - Primary Crusher TP-4 Transfer
Point Hood - Sprays Off
Summary of Opacity Measurements -
Primary Crusher - TP-5 - Rail Car
Unloading - Sprays Off
Summary of Fugitive Emission Observa-
tions - Primary Crusher TP-5 Rail Car
Unloading - Sprays Off
Summary of Opacity Measurements -
TP-6 - Crusher Building - Sprays Off
Summary of Fugitive Emission Observa-
tions - Primary Crusher TP-6 Crusher
Building - Sprays Off
Trace Element Analysis - Primary
Crusher - Sprays Off
56
57
61
62
64
65
66
67
68
69
70
71
Table 2-39
Summary of Emission Test Results -
Pebble Screening and Milling TP-1
Screen Exhaust Duct - English
73
-VJ.il-
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Paqe
Table 2-40
Table 2-41
Table 2-42
Table 2-43
Table 2-44
Table 2-45
Table 2-46
Table 2-47
Table 2-48
Table 2-49
Table 2-50
Table 2-51
Summary of Emission Test Results -
Pebble Screening and Milling TP-1
Screen Exhaust Duct - Metric
Summary of Emission Test Results -
Pebble Screening and Milling TP-2
Bucket Elevator Exhaust Duct - English
Summary of Emission Test Results -
Pebble Screening and Milling TP-2
Bucket Elevator Exhaust Duct - Metric
Summary of Emission Test Results -
Pebble Screening and Milling TP-2A
Total Scrubber Inlet - English
Summary of Emission Test Results -
Pebble Screening and Milling TP-2A
Total Scrubber Inlet - Metric
Summary of Emission Test Results -
Pebble Screening and Milling TP-3
Scrubber Outlet - English
Summary of Emission Test Results -
Pebble Screening and Milling TP-3
Scrubber Outlet - Metric
Summary of Opacity Measurements -
Pebble Screening and Milling -
TP-3 - Scrubber Outlet
Summary of Opacity Measurements -
Pebble Screening and Milling -
TP-4 - Bucket Elevator Hood
Summary of Fugitive Emission Observa-
tions - Pebble Screening and Milling
TP-4 Bucket Elevator Hood
Summary of Opacity Measurements -
Pebble Screening and Milling -
TP-5 Screen Hood
Summary of Fugitive Emission Observa-
tions - Pebble Screening and Milling
TP-5 Screen Hood
74
78
79
83
84
88
89
91
92
93
94
95
Table 2-52
Summary of Opacity Measurements -
Coarse Ore Stockpile - TP-1 -
West of Stockpile
96
-ix-
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Paqe
Table 2-53
Table 2-54
Table 2-55
Summary of Fugitive Emission Observa-
tions - Coarse Ore Stockpile TP-1 West
of Stockpile
Summary of Opacity Measurements -
Coarse Ore Stockpile - TP-2 - East
of Stockpile
Summary of Fugitive Emission Observa-
tions - Coarse Ore Stockpile TP-2 East
of Stockpile
97
98
99
Table 2-56
Table 2-57"
Table 2-58
Table 2-59
Summary of Opacity Measurements -
Tailings Disposal - TP1 - West
of Pond
Summary of Fugitive Emission Observa-
tions - Tailings Disposal TP-1 West
of Pond
Summary of Opacity Measurements -
Tailings Disposal - TP-2 - East
of Pond
Summary of Fugitive Emission Observa-
tions - Tailings Disposal TP-2 East
of Pond
100
101
102
103
Table 2-60
Table 2-61
Summary of Opacity Measurements -
Truck Loading
Summary of Fugitive Emission Observa-
tions - Truck Loading
104
105
Table 2-62
Table 3-1
Table 3-2
Table 3-3
Summary of Ore Sample Analyses
*****
Summary of Visual Test Results -
Primary Crusher/Rail Car Unloading
Summary of Visual Test Results -
Pebble Screening and Milling
Summary of Visual Test Results -
Molybdenum Dryers
106
112
113
115
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PREFACE
The work reported herein was conducted by personnel from the
York Research Corporation (YRC), the GCA/Technology Division
(GCA) and the U.S. Environmental Protection Agency (USEPA).
The scope of work, issued under EPA Contract No. 68-02-2819,
Work Assignment No. 17, was under the supervision of the YRC
Project Director, Mr. James W. Davison. Mr. Roger A. Kniskern
of YRC served as Project Manager and was responsible for sum-
marizing the test and analytical data in this report. Analyses
of the samples were performed at the YRC Laboratory in
Stamford, Connecticut under the direction of Mr. Robert Q.
Bradley and at the YRC Laboratory in Denver, Colorado. Radio-
activity analysis was performed by Albuquerque Laboratory,
Albuquerque, New Mexico; trace element analysis was performed
by Ledoux and Company, Teaneck, New Jersey. Hardness analysis
was performed by Bridgeport Testing Laboratory, Inc.,
Bridgeport, CT.
Personnel from GCA were responsible for monitoring the test
process operations and collecting process samples during the
testing program.
The cooperation and guidance of Mr. Kenneth Kloska, of the
Henderson Mill, Climix Molybdenum Company, contributed greatly
to the success of the test program.
Mr. Dennis Holzschuh, of the Office of Air Quality Planning and
Standards, Emission Measurement Branch, EPA, served as Tech-
nical Manager and was reponsible for coordinating the emission
test program. Mr. William Neuffer, of the Industrial Studies
Branch, EPA, provided the process information for this project.
-xi-
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1.0 INTRODUCTION
York Research Corporation (YRC), under Contract No. 68-02-
2819, was requested by the United States Environmental
Protection Agency (EPA) to perform an emission test pro-
gram at a molybdenum processing plant. The test program
was conducted at the Henderson Mill of the Climax Moly-
bdenum Company located near Silverthorne, Colorado. Samp-
ling was performed from August 22, 1979 to August 30,
1979. The following processes/operations were tested:
• Molybdenum Dryer
• Primary Crusher/Rail Car Unloading
• Pebble Screening and Milling
• Coarse Ore Stockpiling
• Tailings Disposal
• Truck Loading
The sampling locations for each process are shown schem-
atically in Figures 1-1 through 1-5 (Section 4.1 describes
each location in detail). The scrubber inlet(s) and out-
let of the first three processes were sampled simultane-
ously. Visual testing corresponded to the sampling. The
test points were as follows:
• Molybdenum Dryer
•• TP-1 Combined Scrubber Inlet
• TP-2 Scrubber Outlet
• TP-3 Dryer Area
• Primary Crusher/Rail Car Unloading
• TP-1 Transfer Points Exhaust Duct
• TP-2 Crusher Pit Exhaust Duct
-1-
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o
PART1CULATE and PARTICLE
SIZE DISTRIBUTION
OPACITY and FUGITIVE
EMISSION FREQUENCY
PARTICULATE, PARTICLE SIZE
DISTRIBUTION and OPACITY
HOLOFLITE DRYERS
GRADE B
DRYER
MOLYBDENUM DRYER
figure 1-1
-------
CRUSHER BUILDING
CUD
O
PARTICULATE and PARTICLE
SIZE DISTRIBUTION
OPACITY and FUGITIVE
EMISSION FREQUENCY
PARTICULATE. PARTICLE SIZE
DISTRIBUTION and OPACITY
PIT
CRUSHER
ground level
APRON FEEDER
CONVEYOR to STOCKPILE
PRIMARY CRUSHER/RAIL CAR UNLOADING
figure 1-2
-------
PARTICULATE and PARTICLE
SIZE DISTRIBUTION
o
OPACITY and FUGITIVE
EMISSION FREQUENCY
•
PARTICULATE. PARTICLE SIZE
DISTRIBUTION and OPACITY
/1.
A
CONVEYO
PEBBLE
SCREEN
undersize
to wet mill
oversize
PEBBLE
MILL
BUCKET
ELEVATOR
PEBBLE SCREENING and MILLING
figure 1-3
-4-
-------
o
OPACITY and FUGITIVE
EMISSION FREQUENCY
CONVEYOR from CRUSHER
T
to reclaim
COARSE ORE STOCKPILING
figure 1-4
-------
MILL BUILDING
TAILINGS PIPELIN
CYCLONE
SEPARATORS
DAM
o
OPACITY and FUGITIVE
EMISSION FREQUENCY
TAILINGS DISPOSAL AREA
-------
• TP-3 Scrubber Outlet
• TP-4 Transfer Point Hoods
• TP-5 Rail Car Unloading
• TP-6 Crusher Building
Samples were collected at the Primary Crusher during two
separate operational modes — wet suppression sprays on and
wet suppression sprays off.
• Pebble Screening and Milling
• TP-1 Screen Exhaust Duct
• TP-2 Bucket Elevator Exhaust Duct
• TP-2A Total Scrubber Inlet
• TP-3 Scrubber Outlet
• TP-4 Bucket Elevator Hood
• TP-5 Screen Hood
• Coarse Ore Stockpiling
• TP-1 West of Stockpile
• TP-2 East of Stockpile
• Tailings Disposal
• TP-1 West of Pond
• TP-2 East of Pond
• Truck Loading
• TP-1 Truck Loading Area
The objective of the test program was to determine emis-
sion levels from controlled metallic mineral (molybdenum)
-7-
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processing facilities to support planned new source per-
formance standards (NSPS) in the Metallic Mineral
Industry.
Samples and data were collected to determine particulate
concentration and emission rate; scrubber efficiency;
particulate radioactivity (Po210) and trace element con-
centration; and particle size distribution. In addition,
visual determination of opacity and fugitive emission
frequency was conducted. Ore samples were analyzed for
moisture content and hardness.
-8-
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2.0 SUMMARY AND DISCUSSION OF TEST RESULTS
Tables 2-0 and 2-1 summarize the scrubber removal efficiencies
for the various operations. The efficiencies are based on the
difference of inlet and outlet particulate concentration mea-
sured during the concurrent testing.
The sections below discuss the testing and results at the sep-
arate processes. All testing was performed in accordance with
USEPA Reference Methods (see Section 4.0, Sampling Methods).1
2.1 Molybdenum Dryer
The test program was started at the molybdenum dryer.
Sampling was conducted concurrently at the scrubber inlet
and outlet. Particulate test and particle size distri-
bution test results are presented in Tables 2-2 through
2-5, and Figures 2-0 through 2-2. Results of visual test-
ing are presented in Tables 2-6 through 2-8.
The inlet sampling location (TP-1) measured the combined
emissions from the north and south dryers, however, this
location does not include the entire gas stream entering
the scrubber. A Grade-B dryer exhaust duct entered the
scrubber inlet duct between the actual sampling location
and the scrubber. This dryer processes approximately 10
percent of the total product. Assuming that the test
results for TP-1 account for 90 percent of the total input
to the scrubber, an adjusted scrubber removal efficiency
was calculated (Table 2-1). The efficiency, however,
only increases by about 0.5 percent.
Some sampling problems were encountered at the inlet
location, TP1. During each test run, when the bottom port
1 Reference Methods are contained 40 CFR 60, "Standards of
Performance for New Stationary Sources, Appendix A".
-9-
-------
was removed, a large amount of water drained from the
duct. This water contained a large amount of molybdenum
as determined by its dark black color.
During the first test, this draining water caused the
heaters to short and fuses to blow in the meter box.
Also, the actual inlet moisture was twice of that measured
in the preliminary moisture test and the measured inlet
duct temperature was inaccurate. At the outlet, TP2, the
flow rate changed enough so that the nozzle had to be
changed. The first tests were finally voided because the
isokinetic ratio for TP1 was calculated to be greater than
the maximum allowable limit of 110 percent. A fourth test
was run to replace the first test.
The particulate samples (filters and front-half-acetone
residues) were also analyzed for polonium-210 concent-
ration. The results, reported in picocuries per sample,
are presented in Table 2-9.
2.2 Primary Crusher/Rail Car Unloading
Sampling at the crusher building was conducted during two
operational modes; suppression sprays on and supression
sprays off. The results for the "sprays on" mode are pre-
sented in Tables 2-11 through 2-23, and Figures 2-4
through 2-10. The "sprays off" test results are presented
in Tables 2-25 through 2-37, and Figures 2-11 through
2-17.
The crushing process involved the dumping of a 22-car
train of ore into the gyratory crusher. A car was pro-
cessed in a span of about one and one-half to five minutes
at the rate of about four trains per hour. Originally,
the testing was to be conducted only during the processing
-10-
-------
of a train, however, this was not feasible due to the
short duration of the processing cycle and the requirement
of at least a two-hour particulate test. The actual test
started at the same time as a train was being processed
and ran continuously until the test period of 144 minutes
was completed. A member of the test team was responsible
for recording the times the ore was dumped from the
trains. The schedules are summarized in Tables 2-10 and
2-24.
Preliminary observations of the scrubber outlet indicated
the flow was cyclonic. Measurements were made according
to Method 1, Section 2.4, which confirmed that the flow
was extremely cyclonic. Sampling in the cyclonic flow was
achieved by rotating the probe to the position of maximum
velocity pressure (determined by 90° - the angle where
/\p = 0, see Figure 2-3) . The nozzle is therefore directed
into the maximum flow and the particulate concentration c,
is accurately determined. However, the particulate emis-
sion rate, E, and flow, Q, are determined using the velo-
city of gas, vvertical, travelling vertically through the
cross-sectional area, A, of the stack:
E - ^vertical HC)
where:
Qvertical = (vvertical)(A)
Tables 2-15, 2-16, 2-29, and 2-30, present the maximum
velocities and flows, but the emission rate, E, is calcul-
ated using Qvertical' which is assumed to be equal to the
sum of the inlet flows from TP-1 and TP-2.
The first three tests were conducted with the suppression
sprays on. During the first test only two trains were
-11-
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processed due to a full stockpile and conveyor mainten-
ance. The second test was started when a train first
started to approach the crusher dump point. Eight trains
were processed during each of the remaining tests con-
ducted. Since it was felt that the second and third tests
with eight trains each were representative of the oper-
ation, the first test was not rerun. The results of Test
1 are not included in the average values.
The second series of tests were conducted with the wet
suppression sprays off. Due to full stockpiles and track
maintenance, seven trains were processed during each of
the three tests. The particulate emissions did not sig-
nificantly differ from those measured with the sprays on,
however, the ore did appear to contain more moisture dur-
ing the sprays off test period.
The particle size distribution tests at the scrubber inlet
location were run only when a train was being processed to
give a more accurate representation of the actual size
distribution during train processing. This was possible
since the sampling time was only several minutes. How-
ever, the outlet particle size testing required a few
hours, so the sampling was conducted while several trains
were processed.
The filter from TP1, Run 3, Sprays Off, was analyzed for
various trace elements using spark source mass spectro-
scopy (SSMS). The results are presented in Table 2-38.
2.3 Pebble Screening and Milling -
The Pebble Screening and Milling operation is not normally
used and was run only for the purpose of the test program.
-1 2-
-------
The results are presented in Tables 2-39 through 2-51, and
Figures 2-18 through 2-27.
During the first test the power was lost due to an over-
loaded circuit. The testing was stopped and the probes
were pulled from the ducts. When the power was restored,
the test was continued until completion. The test was
considered representative and the results valid. At sev-
eral times during the remaining tests, sampling had to be
halted due to blockages in the apron feeder. During these
times, the sampling was stopped and not resumed until ore
was being processed in the unit once again.
2.4 Coarse Ore Stockpiling, Tailings Disposal,
Truck Loading
Testing at these operations only entailed opacity measure-
ment and visual determination of emission frequency.
Three hours of each test were completed at the test
points. Testing was simultaneous at the test points for
Coarse Ore Stockpiling and for Tailings Disposal. The
results are summarized in Tables 2-52 through 2-61.
2.5 Ore Samples
Grab ore samples were taken from various locations during
emission testing to ascertain if a correlation between ore
moisture content and inlet emissions may be developed.
Two samples were also tested for degree of hardness
(i.e., crushing strength) to determine whether there is a
relationship between hardness and potential emissions.
The results from these analyses are presented in Table
2-62*. For the hardness tests, higher numerical values
indicate greater hardness and "C" refers to the highest
(i.e., hardest) Rockwell® scale.
* Crushing strength results were reported from more than one
test program. The results for this test program are circled
on the report, see Appendix 6.3.
-13-
-------
TABLE 2-0
SUMMARY OF SCRUBBER REMOVAL EFFICIENCY
Measured
Removal
Location Test No. Efficiency (%)a
Molybdenum
Dryer
Primary Crusher
Sprays On^
Primary Crusher
Sprays Off
Pebble Screening
and Milling
2
3
4b
AVE
2
3
AVE
1
2
3
AVE
1
2
3
AVE
94.08C
96.52C
97.49C
96.03C
97.98
97.42
97.70
98.62
97.69
95.39
97.23
73.66
91.32
93.27
86.08
a Based on particulate concentration.
b Test 1 was voided, a fourth test was run.
c These values are artificially low because the inlet location
only measured approximately 90% of the gas stream into the
scrubber. See Section 2.1.
d Only two trains were processed during Test 1 so the removal
efficiency is not included. See Section 2.2.
-15-
-------
TABLE 2-1
MOLYBDENUM DRYER
ADJUSTMENT OF SCRUBBER REMOVAL EFFICIENCY
Test
2
3
4
AVE
Measured
Concentration
at Combined
Inlet (gr/dscf)
0.21161
0.16763
0.29319
0.22414
Adjusted
Concentration
for Total
Input (gr/dscf)
0.23512
0.18625
0.32577
0.24905
Concentration
at
Outlet (gr/dscf)
0.01252
0.00584
0.00735
0.02609
Adjusted
Removal
Efficiency (%)
94.68
96.86
97.74
96.43
-------
TABLE 2-2
SUMMARY OF EMISSION TEST RESULTS
MOLYBDENUM DRYER TP-1 COMBINED SCRUBBER INLET*
English Units
Test No.
General Data
Date
Time
Isokinetic Ratio (%)
Gas Data
Velocity (fps)
Flow (scfmd)
Temperature (°F)
Moisture (%)
Particulate Emissions
Gr./scfd
Lbs./Hr.
2
8/23
1312-1448
107.4
26.1
2611
151.8
18.7
0.21161
4.73
3
8/23
1550-1722
103.7
30.2
3106
150.0
16.7
0.16763
4.46
4
8/24
0805-0940
96.6
27.5
3061
150.4
9.8
0.29319
7.69
Average
-
102.6
27.9
2926
105.7
15.1
0.22415
5.63
a The combined gas stream from only two dryers, contributing approxi-
mately 90% of the total scrubber inlet, was sampled.
-17-
-------
TABLE 2-3
SUMMARY OF EMISSION TEST RESULTS
MOLYBDENUM DRYER TP-1 COMBINED SCRUBBER INLET*
Metric Units
Test No.
General Data
Date
Time
Isokinetic Ratio (%)
Gas Data
Velocity (mps)
Flow (dnm-Vmin. )
Temperature (°C)
Moisture (%)
Particulate Emissions
Mg/nm^
Kg/Hr.
2
8/23
1312-1448
107.4
7.96
74
66.5
18.7
484.25
2.15
3
8/23
1550-1722
103.7
9.22
88
65.6
16.7
383.61
2.02
4
8/24
0805-0940
96.6
8.37
87
65.8
9.8
670.94
3.49
Average
102.6
8.52
83
66.0
15.1
512.93
2.55
a The combined gas stream from only two dryers, contributing approxi-
mately 90% of the total scrubber inlet, was sampled.
-18-
-------
PARTICLE SIZE DISTRIBUTION
100.0
99.99
99.9 99.8
99 98
95
90
80 70 60
0.05 0.01
100.0
CLIMAX MOLYBDENUM
PRODUCT DRYER
TP-1 SCRUBBER INLET
PARTICLE SIZE DISTRIBUTION
.:. TEST 2
FIGURE 2-0
0.2
ai
0.01 0.05 0.1 0.2 0.5 1
95
98 99
99.8 99.9 99.99
O.I
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
-19-
-------
PARTICLE SIZE DISTRIBUTION
100.0
99.99 99.999.8
99 98
6O.O
401
SOD
ZOO
10.0
9.0
8.0
T.O
80
3.0
2.0
05
0.2
0.1
!1
CLIMAX MOLYBDENUM
PRODUCT DRYER
TP-1 SCRUBBER INLET
PARTICLE SIZE DISTRIBUTION
TEST 3
FIGURE 2-1
0.01 0.05 0.1 0.2 0.5 1
10
20 30 40 SO 60 70 80
90 95
98 99
11
100.0
8 OX)
70.O
600
000
400
300
200
IOO
9.0
8.0
7.0
8.0
5.0
4.0
3.0
i
V)
I
i
N
2.0
1.0
0.9
0.8
0.7
o.e
0.9
0.4
0.9
0.2
99.8 99.9 99.99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
-20-
-------
TABLE 2-4
SUMMARY OF EMISSION TEST RESULTS
MOLYBDENUM DRYER TP-2 SCRUBBER OUTLET
English Units
Iest No.
General Data
I Date
Time
Isokinetic Ratio (%)
Vas Data
1 Velocity (fps)
Flow (scftnd)
Temperature (°F)
! Moisture (%)
articulate Emissions
IGr./scfd
Lbs./Hr.
2
8/23
1322-1501
96.1
35.9
3056
109.5
15.6
0.01252
0.33
3
8/23
1545-1723
98.6
38.4
3171
103.8
18.8
0.00584
0.16
4
8/24
0815-0954
93.5
31.3
2988
92.8
8.3
0.00735
0.19
Average
96.1
35.2
3072
102.0
14.2
0.00857
0.22
-21-
-------
TABLE 2-5
SUMMARY OF EMISSION TEST RESULTS
MOLYBDENUM DRYER TP-2 SCRUBBER OUTLET
Metric Units
Test No.
Average
General Data
Date 8/23 8/23
Time 1322-1501 1545-1723
Isokinetic Ratio (%) 96.1 98.6
Gas Data
Velocity (mps) 10.95 11.69
Flow (dnm3/min.) 87 90
Temperature (°C) 43.1 39.9
Moisture (%) 15.6 18.8
Particulate Emissions
Mg/nm3 28.64 13.36
Kg/Hr. 0.15 0.07
8/24
0815-0954
93.5
9.54
85
33.8
8.3
16.82
0.09
96.1
10.73
87
38.9
14.2
19.61
0.10
-22-
-------
PARTICLE SIZE DISTRIBUTION
IOO4
99.99 99.9 99.8 99
SCO
ZOO
10X3
9.0
8.0
7.0
60
30
4.0
3.0
2 JO
1.0
0.9
0.8
0.7
OJB
as
0.4
05
0.2
ai
CLIMAX MOLYBDENUM
PRODUCT DRYER
TP-Z SCRUBBER OUTLET
PARTICLE SIZE DISTRIBUTION
TEST 1
FIGURE 2-2
005 .01 ,nnn
800
70.O
600
30.0
4OO
30O
20.0
too
9.0 "JJ
ao Q
7.0 W
6.0 O
or
5.0 o
3.0 UJ
N
0)
2.0
O
i.o
0.9
o.e
0.7
0.6
0.9
0.4
0.3
0.2
0.01 0.05 0.1 0.2 0.5 1
10
20 30 40 50 60 70 80
99.8 99.9 99.99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
-23-
-------
TABLE 2-6
SUMMARY OF OPACITY MEASUREMENTS
MOLYBDENUM DRYER TP-2 SCRUBBER OUTLET
Test No.
Date
Time
Six Minute
Interval
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
2
8/23/79
1320-1459
16
18
19
18
18
15
20
20
17
17
20
16
17
16
15
14
16*
3
8/23/79
1543-1717
- AVERAGE OPACITY (%) -
16
12
15
20
20
18
17
19
19
15
15
18
21
19
22
24
4
a/24/79
0812-0950
16
16
15
4
12
12
10
9
9
7
5
5
5
5
9
10
10a
a Three Minute Interval
-24-
-------
TABLE 2-7
SUMMARY OP OPACITY MEASUREMENTS
MOLYBDENUM DRYER TP-3 DRYER AREA
Test No. 2 34
Date 8/23/79 8/23/79 8/24/79
Time 1352-1.452 1613-1713 0806-0906
Six Minute
Interval - AVERAGE OPACITY (%) -
1 0 0 0
20 00
3
4
5
0
0
0
0
0
0
0
0
0
6
7
8
0
0
0
0
0
0
0
0
0
90 00
10 0 00
-25-
-------
TABLE 2-8
SUMMARY OF FUGITIVE EMISSION OBSERVATIONS
MOLYBDENUM DRYER TP-3 DRYER AREA
Test No. 1 2 3 Average
Date- 8/23 8/23 8/24
Test Period 1352-1452 1613-1713 0806-0906
Test Duration (sec.) 3600 3600 3600 3600
Duration of Fugitive
Emissions (sec.) 000 0
Fugitive Emission
Frequency (%) 0 0 0 0
-26-
-------
TABLE 2-9
PARTICULATE RADIOACTIVITY ANALYSIS
MOLYBDENUM DRYER
Concentration Polonium^10 (pCi/sample)
Location Test Filter Front Half Acetone
TP-1
Combined
Scrubber
Inlet
TP-2
Scrubber
Outlet
2
3
4
2
3
4
ND*
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
* Not detectable, experimental error = ± 1.0 pCi.
-27-
-------
Pjtot tubes and nozzle
In vertical position
Probe rotated from vertical
position until AP aO. PMot tubes
and nozzle are perpendicular
to th? flow.
Probe rotated so that pltot
fubes and nozzle are In the
maximum flow
I
to
00
I
PITOT TUBES!
direction o'f
cyclonic flo
NOZZLE
SAMPLING IN CYCLONIC FLOW
figure 2-3
-------
TABLE 2-10
PRIMARY CRUSHER - TP1 - TRANSFER POINTS EXHAUST DUCT
SEQUENCE OF TRAIN PROCESSING DURING SAMPLING
Train No.
Start
Stop
Total
Time (Min.)
Comments
to
vo
1
2
1
2
3
4
5
6
7
8
1
2
3
4
5
6
7
8
9:19:50
10:20:20
12:55:45
13:07:10
13:17:15
14:04:50
14:12:50
14:32:45
14:41:15
15:07:00
16:23:15
16:52:30
17:04:10
17:17:45
17:29:05
17:40:05
17:55:00
18:26:25
Test 1 Sprays On 0918-1153
9:22:30
10;24:30
2.67
4.17
Test 2 Sprays On 1255-1520
12:59:00
13:10:15
13:20:25
14:09:00
14:17:00
14:35:15
14:50:40
15:09:40
Test 3 Sprays On
16:27:00
16:56:35
17:08:50
17:21:40
17:31:50
17:43:00
18:12:15
18:31:05
3.25
3.08
3.17
4.17
4.17
2.50
3.42
2.67
1623-1848
3.75
4.08
4.67
3.92
2.75
2.92
17.25
4.67
Stopped During Dumping
Stopped For 1.00 Minute
Stopped For 0.33 Minutes
Stopped For 0.08 Minutes
Stopped for 13.00 Minutes
-------
TABLE 2-11
SUMMARY OF EMISSION TEST RESULTS
PRIMARY CRUSHER TP-1 TRANSFER POINTS EXHAUST DUCT
SPRAYS ON
English Units
Test No.
General Data
Date
Time
Isokinetic Ratio (%)
Trains Processed
Gas Data
Velocity (fps)
Flow (scfmd)
Temperature (°F)
Moisture (%)
Particulate Emissions
Gr./scfd
Lbs./Hr.
1
8/27
0913-1117
105.2
2
67.1
16054
63.8
1.5
0.10072
13.86
2
8/27
1253-1457
103.5
8
66.9
15869
65.4
2.0
0.25651
34.89
3
8/27
1621-1823
104.4
8
67.3
16064
63.1
1.9
0.16538
22.77
Average3
—
104.0
—
67.1
15966
64.2
2.0
0.21094
28.83
a Test 1 not included in average.
-30-
-------
TABLE 2-12
SUMMARY OP EMISSION TEST RESULTS
PRIMARY CRUSHER1 TP-1 TRANSFER POINTS' EXHAUST DUCT
SPRAYS ON
Metric: Units
Test
Averagea
General Data
Date
Time
Isokinetic Ratio (%)
Trains, Processed
B/ 27
105.2;
2>
8/27
1253-1457
103.5:
8
8/2-7
1621-1823
104.4
&
104.0
Gas Data
Velocity (mps)
Flow (dnm3/min., )
Temperature (°C)
Moisture (%)
Particulate Emissions-^
20.4
455
17.6
1.5-
20.4
449
18.6
2.0
a Test 1 not included in, average.
20.5
455
1.7 .3
1.9
20-4
452!
18 ..0
2.0
Mg/nm3:
Kg/Hr.
^^S ^Y /t'Qf C Q'^T" rt'rti
• • siS(J +,*ty DO / . UU
6;. 29- L5.83
378.44
10.33
482.72
13.08
-31-
-------
PARTICLE SIZE DISTRIBUTION
IOO.O
99.99 99.999.8
99 98 95 90
80 70 60 SO 40
30JD
ZOO
IOO
9.0
8.O
7.05
60
3JO
4.0
3.0
0.8
0.7
OA
OS
0.1
CLIMAX MOLYBDENUM-
PRIMARY CRUSHER
TP-1 TRANSFER POINT EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST' 1; SPRAYS ON
FIGURE 2-4
0.01 0.05 0.1 0.2 OS 1
10
20 30 40 50 60 70 80
90 95
_L
100.0
8OJO
70.O
600
SOO
40JO
300
20.0
I OX)
9.0
ao
7.0
8.0
5.0.
4.0
3.0
2.0
CO
i
1.0
0.9
0.8
0.7
0.6
0.5
0.4
0.3
0.2
98 99
99.8 99.9
99.99
O.I
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
-32-
-------
PARTICLE SIZE DISTRIBUTION
100.0
99.99
99.999.8
99 98
008 -01 100.0
CLIMAX MOLYBDENUM
PRIMARY CRUSHER
TP-1 TRANSFER POINT EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 2 SPRAYS ON
FIGURE 2-5
0.2
0.01 0.05 0.1 0.2 0.5 1
20 30 40 50 60 70 80
90 95
98 99
99.8 99.9 99.99
O.I
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Op)
-33-
-------
PARTICLE; SIZE DISTRIBUTION*
99.99 99.999.8 99 98 95 90 80 70 60 50 40 30 20 10 5
1 03 02 0.1 0.05 0.01
CLIMAX MOLYBDENUM
PRIMARY CRUSHER
TP-1 TRANSFER POINT EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 3 SPRAYS ON
FIGURE. 2-6
0.01 0.05 0.1 0.2 0.5 1
10
20 30 40 SO 60 70 80
100,0
0.4-
0.3
0.2
90 95
98 99
99.8 99.9 99.99
O.I
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
-34-
-------
TABLE 2-13
SUMMARY OF EMISSION TEST RESULTS
PRIMARY CRUSHER TP-2 CRUSHER PIT EXHAUST DUCT
SPRAYS ON
English Units
Test No.
General Data
Date
Time
Isokinetic Ratio (%)
Trains Processed
Gas Data
Velocity (fps)
Flow (scfmd)
Temperature (°F)
Moisture (%)
Particulate Emissions
Gr./scfd
Lbs./Hr.
1
8/27
0917-1136
100.5
2
86.8
23701
60.0
2.4
0.10938
22.22
2
8/27
1252-1505
99.5
8
85.9
23603
60.0
1.7
0.11049
22.35
3
8/27
1624-1838
100.9
8
86.8
23038
63.2
1.8
0.09078
17.93
Average3
-
100.2
—
86.4
23320
61.6
1.8
0.10064
20.14
a Test 1 not included in average.
-35-
-------
TABLE 2-14
SUMMARY OF EMISSION TEST RESULTS
PRIMARY CRUSHER TP-2 CRUSHER PIT EXHAUST DUCT
SPRAYS ON
Metric Units
Test No.
Average*
General Data
Date 8/27 8/27
Time 0917-1136 1252-1505
Isokinetic Ratio (%) 100.5 99.5
Trains Processed 2 8
8/27
1624-1838
100.9
8
100.2
Gas Data
Velocity (mps) 26.5
Flow (dnm^/min.) 671
Temperature (°C) 15.6
Moisture (%) 2.4
Particulate Emissions
Mg/nm3 250.29
Kg/Hr 10.08
26.2
668
15.6
1.7
252.84
10.14
26.5
652
17.3
1.8
207.73
8.13
26.4
660
16.4
1.8
230.28
9.12
a Test 1 not included in average.
-36-
-------
PARTICLE SIZE DISTRIBUTION
99.99 99.999.8
99 98 95
90
4QC
300
ZOO
3.0
2X>
as
0.4
as
O.Z
ai
0.05 0.01
CLIMAX MOLYBDENUM
PRIMARY CRUSHER
TP-2 CRUSHER PIT EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 1 SPRAYS ON
FIGURE 2-7 -
0.01 O.OS 0.1 0.2 05 1
10
20 30 40 50 60 70 80
90 95
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
S.O
= 4:0
100.0
BOO
7O.O
eao
500
40O
30O
20.0
100.
9.0
8.0
7.0
3.0
2.0
O
or
o
£v
Z
UJ
N
l&J
_1
O
H
(E
<
0.
1.0
0.9
0.8
O.T
0.6
0.5
O.4
0.3
0.2
99.8 99.9 99.99
O.I
-37-
-------
PARTICLE SIZE DISTRIBUTION
100.0
99.99
99.9 99.8
99 98 95 90
80
70 60 50 40
O.S
0.4
03
0.2
100.0
CLIMAX MOLYBDENUM
PRIMARY CRUSHER
TP-2 CRUSHER PIT EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 2 SPRAYS ON
FIGURE 2-8
0.1
0.01 0.05 0.1 0.2 0.5 1 2 5 10 20 30 40 50 60 70 80 90 95 98 99 99.8 99.9
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
99.99
-38-
-------
PARTICLE SIZE DISTRIBUTION
IOO.O
90.0
99.99 99.9 99.8 99
95 90 80
70 60 SO 40 30
20
10
0.5 0.2 0.1 0.03 0.01
as
as
ae
ai
CLIMAX MOLYBDENUM
PRIMARY CRUSHER
TP-2 CRUSHER PIT EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 3 SPRAYS ON
FIGURE 2-9
toao
0.01 0.05 0.1 0.2
10
20 30 40 50 60 70 80
90 95
98 99
99.8 99.9 99.99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
-39-
-------
TABLE 2-15
SUMMARY OF EMISSION TEST RESULTS
PRIMARY CRUSHER TP-3 SCRUBBER OUTLET
SPRAYS ON
English Units
Test No.
Average5
General Data
Date 8/27 8/27
Time 0918-1153 1255-1520
Isokinetic Ratio (%) 92.6 95.7
Trains Processed 2 8
Gas Data
Velocitymax (fps) 73.3 74.1
Flowmax (scfmd) 105617 106705
Flowvertical (scfmd)b 39755 39472
Temperature (°F) 55.0 55.1
Moisture (%) 2.5 2.5
Particulate Emissions
a Test 1 not included in average.
b Flowvertical equals sum of inlet flows.
8/27
1623-1848
94.6
8
75.5
108102
39102
55.7
3.0
95.2
74.8
107404
39287
55.4
2.8
Gr. /scfd
Lbs/Hr
0.00857
2.92
0.00370
1.25
0.00331
1.11
0.00350
1.18
-40-
-------
TABLE 2-16
SUMMARY OF EMISSION TEST RESULTS
PRIMARY CRUSHER TP-3 SCRUBBER OUTLET
SPRAYS ON
Metric Units
Test No.
Average5
4neral Data
• Date
Time
Isokinetic Ratio (%)
Trains Processed
9ks Data
|Velocitymax (mps)
Flowmax (dnm3/min)
Flowvertical (dnm3/mii
• Temperature (°C)
Moisture (%)
trticulate Emissions
Mg/nm3
Kg/Hr
•
8/27
0918-1153
92.6
2
22.3
2991
i)b 1126
55.0
2.5
19.62
1.32
8/27
1255-1520
95.7
8
22.6
3022
1117
55.1
2.5
8.46
0.567
8/27
1625-1848
94. '6^
8
23.0
3061
1107
55.7
3.0
7.56
0.503
_
-
95.2
_
22.8
3042
1112
55.4
2.8
8.01
0.535
a Test 1 not included in average.
equals sum of inlet flows.
-41-
-------
PARTICLE. SIZE DISTRIBUTION
100.0
99.99
99.9 99.8
99 98
95 90
40X
300
ZOO
0.1
80 70 60 50 40 30 20 10 5 2 1 0.5 0.2 0.1 0.05 0.01
CLIMAX MOLYBDENUM
PRIMARY CRUSHER
TP-3 SCRUBBER OUTLET
PARTICLE SIZE DISTRIBUTION
TEST 1 SPRAYS ON
FIGURE 2-10
100.0
8O.O
70.O
60.0
3QO
400
300
20.0
0.01 0.05 0.1 0.2 0.5 1 2 5 10 20 30 40 50 60 70 80 90 95 98 99 99.8 99.9 99.99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
O.I
-42-
-------
TABLE 2-17
SUMMARY OF OPACITY MEASUREMENTS
PRIMARY CRUSHER - TP-3 - SCRUBBER OUTLET
SPRAYS ON
Test No.
Date
Time
Six Minute
Interval
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
1
8/27/79
0913-1136
5
5
7
5
5
5
5
5
5
5
5
5
10
5
5
5
5
5
5
5
5
5
5
5
5
2
8/27/79
. 1253-1518
- AVERAGE OPACITY (%) -
8
9
9
9
9
6
5
5
5
5
5
5
10
7
8
5
6
6
5
8
5
5
9
5a
-
3
8/27/79
1623-1843
9
5
5
5
5
8
5
7
5
6
5
7
5
6
5
8
5
6
6
5
5
5
5
5^
-
a Seven Minute Interval
b Two Minute Interval
-43-
-------
TABLE 2-18
SUMMARY OF OPACITY MEASUREMENTS
PRIMARY CRUSHER - TP-4 - TRANSFER POINT HOODS
SPRAYS ON
Test No.
Date
Time
Six Minute
Interval
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
1
8/27/79
0915-1115
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
2
8/27/79
1300-1500
- AVERAGE OPACITY (%) -
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
3
8/27/79
1600-1800
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
-44-
-------
TABLE 2-19
SUMMARY OF FUGITIVE EMISSION OBSERVATIONS
PRIMARY CRUSHER TP-4 TRANSFER POINT HOOD
SPRAYS ON
Test No.
Average
Date
Test Period
Test Duration (sec.)
Duration of Fugitive
Emissions (sec.)
Fugitive Emissions
Frequency (%)
8/27 8/27 8/27
0915-1115 1300-1500 1600-1800
7200 7200 7200
0
0.0
30
0.4
0
0.0
7200
10
0.1
-45-
-------
TABLE 2-20
SUMMARY OF OPACITY MEASUREMENTS
PRIMARY CRUSHER - TP-5 - RAIL CAR UNLOADING
SPRAYS ON
Test No.
Date
Time
Six Minute
Interval
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
1
8/27/79
0915-1140
1
0
0
0
0
0
0
0
0
0
0
1
0
0
0
0
0
0
0
0
0
0
0
0
0^
2
8/27/79
1258-1458
- AVERAGE OPACITY (%) -
0
0
0
0
0
0
0
0
0
0
0
0
0
1
0
0
1
0
0
0*
—
_.
-
—
—
3
8/27/79
1621-1821
1
0
0
0
0
1
0
0
0
0
0
0
0
1
0
0
0
0
0
0
-
^^
—
—
-
a Two Minute Interval
k Three Minute Interval
-46-
-------
TABLE 2-21
SUMMARY OF FUGITIVE EMISSION OBSERVATIONS
PRIMARY CRUSHER TP-5 RAIL CAR UNLOADING
SPRAYS ON
Test No. 1 2 3 Average
Date 8/27 8/27 8/27
Test Period 0915-1140 1258-1458 1621-1821
Test Duration (sec.) 8700 7200 7200 7700
Duration of Fugitive
Emissions (sec.) 135 87 170 131
Fugitive Emissions 1.6 1.2 2.4 1.7
Frequency (%)
-47-
-------
TABLE 2-22
SUMMARY OF OPACITY MEASUREMENTS
PRIMARY CRUSHER - TP-6 - CRUSHER BUILDING
SPRAYS ON
Test No.
Date
Time
Six Minute
Interval
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
1
8/27/79
0915-1152
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
2
8/27/79
1253-1519
- AVERAGE OPACITY (%) -
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Oa
-
3
8/27/79
1623-1844
"
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Ob
—
-
a One Minute Interval
k Four Minute Interval
-48-
-------
TABLE 2-23
SUMMARY OF FUGITIVE EMISSION OBSERVATIONS
PRIMARY CRUSHER TP-6 CRUSHER BUILDING
SPRAYS ON
Test No. 1 2 3 Average
Date 8/27 8/27 8/27
Test Period 0915-1152 1253-1519 1623-1844
Test Duration (sec.) 9420 8760 8460 8880
Duration of Fugitive
Emissions (sec.) 000 0
Fugitive Emissions 0.0 0.0 0.0 0.0
Frequency (%)
-49-
-------
TABLE 2-24
PRIMARY CRUSHER - TP-1 - TRANSFER POINTS EXHAUST DUCT
SEQUENCE OF TRAIN PROCESSING DURING SAMPLING
SPRAYS OFF
Train No.
1
2
3
4
5
6
7
I
ui
o
I
1
2
3
4
5
6
7
1
2
3
4
5
6
7
Start
08:35:00
08:46:05
09:35:20
09:49:10
10:14:05
10:29:20
10:55:05
12:22:35
12:48:05
13:10:10
13:21:55
13:42:00
14:06:30
14:41:30
15:28:00
16:04:25
16:22:30
16:38:45
16:55:15
17:22:55
17:36:20
Stop
Total
Time (Min.)
Comments
Test 4 Sprays Off
08:37:35
08:48:55
09:38:50
09:52:50
10:18:00
10:42:15
10:58:50
Test 5 Sprays Off
12:26:05
12:53:10
13:13:00
13:25:10
13:44:50
14:08:25
14:44:50
Test 6 Sprays Off
15:30:20
16:08:00
16:25:05
16:42:25
17:08:10
17:26:00
17:39:40
0835-1100
2.58
2.83
3.50
2.67
3.92
12.92
3.75
1222-1450
3.50
5.08
2.83
3.75
2.83
1.92
3.33
1528-1752
2.33
3.58
2.58
3.67
12.92
3.08
3.33
Stopped For 1.50 Minutes
Stopped for 9.42 Minutes
Stopped For 0.50 Minutes
Stopped For 1.83 Minutes
Stopped For 9.50 Minutes
-------
TABLE 2-25
SUMMARY OF EMISSION TEST RESULTS
PRIMARY CRUSHER TP-1 TRANSFER POINTS EXHAUST DUCT
SPRAYS OFF
English Units
Test No.
Average
General Data
Date 8/28 8/28 8/28
Time 0831-1035 1219-1420 1524-1724
Isokinetic Ratio (%) 103.8 103.6 104.0 103.8
Trains Processed 777-
Gas Data
Velocity (fps) 68.9
Flow (scfmd) 16347
Temperature (°F) 64.8
Moisture (%) 1.7
Particulate Emissions
Gr./scfd 0.16224
Lbs/Hr 22.73
67.7
15995
65.0
2.1
0.18533
25.41
65.5
15429
65.0
2.4
0.15917
21.05
67.
15923
64.9
2.1
0.16892
23.06
-51-
-------
TABLE 2-26
SUMMARY OF EMISSION TEST RESULTS
PRIMARY CRUSHER TP-1 TRANSFER POINTS EXHAUST DUCT
SPRAYS OFF
Metric Units
Test No. 4 ' 5 6 Average
General Data
Date 8/28 8/28 8/28
Time 0831-1035 12.19-1420 1524-1724
Isokinetic Ratio (%) 103.8 103.6 104.0 103.8
Trains Processed 7 7 7 -
Gas Data
Velocity (mps) 21.0 20.6 20.0 20.5
Flow (dnm3/min.) 463 453 437 451
Temperature (°C) 1S..2 18.3 18.3 18.3
Moisture (%) 1.7 2.1 2.4 2.1
Particulate Emissions
Mg/nm3 371.27 424.11 364.25 386.54
Kg/Hr 10.31 11.53 9.55 10.46
-52-
-------
PARTICLE SIZE DISTRIBUTION
IOO.O
99.99
99.9 99.8
99 98 95 90 80 70 60
005 -°' 100.0
CLIMAX MOLYBDENUM
PRIMARY CRUSHER
TP-1 TRANSFER POINT EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 4 SPRAYS OFF
FIGURE 2-11
0.2
0.01 0.05 0.1 0.2 0.5 1 2 5 10 20 30 40 50 60 70 80 90 95 98 99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
99.8 99.9 99.99
-53-
-------
PARTICLE SIZE DISTRIBUTION
100.0
99.99 99.9 99.8
9998 95 90 80706050403020
0.01
CLIMAX MOLYBDENUM
PRIMARY CRUSHER
TP-1 TRANSFER POINT EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 5 SPRAYS OFF
FIGURE 2-12
— 0.2
0.1
0.01 0.05 0.1 0.2 0.5 1 2 5 10 20 30 40 50 60 70 80 90 95 98 99 99.8 99.9 99.99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
O.I
-54-
-------
PARTICLE SIZE DISTRIBUTION
IOO.O
99.99
99.9 99.8
99 98 95 90
100.0
CLIMAX MOLYBDENUM
PRIMARY CRUSHER
TP-1 TRANSFER POINT EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 6 SPRAYS OFF
FIGURE 2-13
= . 0.3
0.2
0.01 0.05 0.1 0.2 0.5 1 2 5 10 20 30 40 50 60 70 80 90 95 98 99 99.8 99.9 99.99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
O.I
-55-
-------
TABLE 2-27
SUMMARY OF EMISSION TEST RESULTS
PRIMARY CRUSHER TP-2 CRUSHER PIT EXHAUST DUCT
SPRAYS OFF
English Units
Test No.
6
Average
General Data
Date 8/28 8/28 8/28
Time 0835-1049 1223-1437 1526-1738
Isokinetic Ratio (%) 101.0 101.1 100.0 100.7
Trains Processed 777-
Gas Data
Velocity (fps) 84.1
Flow (scfmd) 22932
Temperature (°F) 60.0
Moisture (%) 2.0
Particulate Emissions
Gr./scfd 0.07041
Lbs/Hr 13.84
82.3
22511
60.3
1.6
0.06805
13.13
85.9
23211
64.8
2.0
0.06287
12.51
84.1
22884
61.7
1.9
0.06711
13.16
-56-
-------
TABLE 2-28
SUMMARY OF EMISSION TEST RESULTS
PRIMARY CRUSHER TP-2 CRUSHER PIT EXHAUST DUCT
SPRAYS OFF
Metric Units
Test No. 4 5 6 Average
General Data
Date 8/28 8/28 8/28
Time 0835-1049 1223-1437 1526-1738
Isokinetic Ratio (%) 101.0 101.1 100.0 100.7
Trains Processed 777-
Gas Data
Velocity (mps) 25.6 25.1 26.2 25.6
Flow (dnm3/min.) 649 637 657 648
Temperature (°C) 15.6 15.7 18.2 16.5
Moisture (%) 2.0 1.6 2.0 1.9
Particulate Emissions
Mg/nm3 161.12 155.71 143.86 153.57
Kg/Hr 6.28 5.96 5.67 5.97
-57-
-------
PARTICLE SIZE DISTRIBUTION
100.0
99.99
99.999.8 99 98 95 90
80
03
0.2
O.I
CLIMAX MOLYBDENUM
PRIMARY CRUSHER
TP-2 CRUSHER PIT EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 4 SPRAYS OFF
FIGURE 2-14
100.0
0.9
0.4
0.3
0.2
0.01 0.05 0.1 0.2 0.5 1 2 3 10 20 30 40 50 60 70 80 90 95 98 99 99.8 99.9 99.99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
O.I
-58-
-------
PARTICLE SIZE DISTRIBUTION
99.99
99.9 99.8
99 98 95 90
0.1
°-01 100.0
CLIMAX MOLYBDENUM
PRIMARY CRUSHER
TP-2 CRUSHER PIT EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 5 SPRAYS OFF
FIGURE 2-15
0.2
0.01 0.05 0.1 0.2 0.5 1 2 5 10 20 30 40 50 60 70 80 90 95 98 99 99.8 99.9 99.99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
O.I
-59-
-------
PARTICLE SIZE DISTRIBUTION
IOO.O
99.99 99.9 99.8
9998 95 90 80706050403020 10
2 1 0.5 0.2 0.1 O.OS 0.01
CLIMAX MOLYBDENUM
PRIMARY CRUSHER
TP-2 CRUSHER PIT EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 6 SPRAYS OFF
FIGURE 2-16
0.2
0.1
100.0
80.0
70.0
60.0
500
400
30O
20.0
10.0
9.0
ao
T.O V>
8.0
S.O
4.0
1
v>
I
3.0
2.0
N
3
1.0
0.9
0.9
0.7
0.6
= 0.9
= . 0.4
= . 0.3
0.2
0.01 0.05 0.1 0.2 0.5 1 2 5 10 20 30 40 50 60 70 80 90 95 98 99 99.8 99.9 99.99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Op)
O.I
-60-
-------
TABLE 2-29
SUMMARY OF EMISSION TEST RESULTS
PRIMARY CRUSHER TP-3 SCRUBBER OUTLET
SPRAYS OFF
English Units
Test No.
Average
General Data
Date 8/28 8/28 8/28
Time 0835-1100 1223-1450 1528-1752
Isokinetic Ratio (%) 99.5 98.9 99.0 99.1
Trains Processed 777-
Gas Data
Velocitymax (fps) 74.3
Flow max(scfmd) 108690
Flowvertical (scfmd)a 39279
Temperature (°F) 51.1
Moisture (%) 3.2
Particulate Emissions
78.0
111974
38506
54.8
2.5
74.4
106798
38640
55.0
2.5
75.6
109154
38807
53.6
2.7
Gr./scfd
Lb/Hr
,0.00161
0.542
0.00293
0.967
0.00512
1.70
0.00322
1.07
a Flowver.tical equals sum of inlet flows
-61-
-------
TABLE 2-30
SUMMARY OF EMISSION TEST RESULTS
PRIMARY CRUSHER TP-3 SCRUBBER OUTLET
SPRAYS OFF
Metric Units
Test No.
6
Average
General Data
Date
Time
Isokinetic Ratio (%)
Trains Processed
Gas Data
8/28
0835-1100
99.5
7
Velocitymax (mps) 22.7
Flowmax (dmtH/min) 3078
Flowvert^cai (dnm3/min)a 1112
Temperature (°C) 10.6
Moisture (%) 3.2
Particulate Emissions
8/28
1223-1450
98.9
7
23.8
3171
1090
12.7
2.5
8/28
1528-1752
99.0
7
22.7
3024
1094
12.8
2.5
99.1
23.0
3091
1099
12.0
2.7
Mg/nm^
Kg/Hr
3.69
0.246
6.69
0.439
11.72
0.771
7.37
0.485
Flowver-t-ical equals sum of inlet flows.
-62-
-------
PARTICLE SIZE DISTRIBUTION
IOO.O
99.99
99.9 99.8
99 98 95
100.0
CLIMAX MOLYBDENUM
PRIMARY CRUSHER
TP-3 SCRUBBER OUTLET
PARTICLE SIZE DISTRIBUTION
TEST 2 SPRAYS OFF
FIGURE 2-17
0.1
0.01 O.OS 0.1 0.2 0.5 1
10
20 30 40 . SO 60 70 80
90 95
98 99
O.I
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
-63-
-------
TABLE 2-31
SUMMARY OF OPACITY MEASUREMENTS
PRIMARY CRUSHER - TP-3 - SCRUBBER OUTLET
SPRAYS OFF
Test No.
Date
Time
Six Minute
Interval
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
4
8/28/79
0834-1059
9
6
9
5
5
5
7
5
5
5
9
7
7
7
5
5
5
10
5
6
5
8
5
8
8a
5
8/28/79
1223-1448
- AVERAGE OPACITY (%) -
9
5
5
5
6
8
5
5
7
9
8
8
5
7
8
5
5
6
8
5
5
5
5
8
ga
6
8/28/79
1528-1752
8
5
5
5
5
5
8
5
5
9
5
5
9
5
5
6
7
5
5
8
5
7
8
5
-
a Two Minute Interval
-64-
-------
TABLE 2-32
SUMMARY OF OPACITY MEASUREMENTS
PRIMARY CRUSHER - TP-4 - TRANSFER POINT HOODS
SPRAYS OFF
Test No.
Date
Time
Six Minute
Interval
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
4
8/28/79
0830-1030
0
0
3
6
4
4
0
0
0
0
4
5
1
0
2
5
5
5
3
5
5
8/28/79
1230-1430
- AVERAGE OPACITY (%) -
5
0
3
5
5
0
5
1
0
0
0
4
0
0
0
0
0
0
0
0
6
8/28/79
1525-1725
0
0
2
0
0
2
5
5
1
5
5
3
5
1
4
3
5
0
0
5
-65-
-------
TABLE 2-33
SUMMARY OF FUGITIVE EMISSION OBSERVATIONS
PRIMARY CRUSHER TP-4 TRANSFER POINT HOOD
SPRAYS OFF
Test No. 1 2 3 Average
Date 8/28 8/28 8/28
Test Period 0830-1030 1230-1430 1525-1725
Test Duration (sec.) 7200 7200 7200 7200
Duration of Fugitive
Emissions (sec.) 3615 1560 3540 2905
Fugitive Emissions 50.2 21.7 49.2 40.3
Frequency (%)
-66-
-------
TABLE 2-34
SUMMARY OF OPACITY MEASUREMENTS
PRIMARY CRUSHER - TP-5 - RAIL CAR UNLOADING
SPRAYS OFF
Test No.
Date
Time
Six Minute
Interval
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
4
8/28/79
0831-1040
0
0
0
0
0
0
0
0
0
0
1
0
1
1
0
0
1
1
0
0
0
la
5
8/28/79
1219-1419
- AVERAGE OPACITY (%) -
1
0
0
0
1
1
0
0
1
0
2
0
0
2
0
0
0
3
0
0
-
-
6
8/28/79
1524-1724
1
0
0
0
0
0
3
0
0
1
0
0
1
0
0
0
1
0
0
3
-
-
a Three Minute Interval
-67-
-------
TABLE 2-35
SUMMARY OF FUGITIVE EMISSION OBSERVATIONS
PRIMARY CRUSHER TP-5 RAIL CAR UNLOADING
SPRAYS OFF
Test No. 1 2 3 Average
Date 8/28 8/28 8/28
Test Period 0831-1040 1219-1419 1524-1724
Test Duration (sec.) 7740 7200 7200 7380
Duration of Fugitive
Emissions (sec.) 266 724 590 527
Fugitive Emissions 3.4 10.1 8.2 7.1
Frequencey (%)
-68-
-------
TABLE 2-36
SUMMARY OF OPACITY MEASUREMENTS
PRIMARY CRUSHER - TP-6 - CRUSHER BUILDING
SPRAYS OFF
Test No.
Date
Time
Six Minute
Interval
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
4
8/28/79
0833-1100
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0-
0
0
0
0
0
0
Oa
-
5
8/28/79
1222-1452
- AVERAGE OPACITY (%) -
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
ob
6
8/28/79
1528-1752
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
ob
a Four Minute Interval
b One Minute Interval
-69-
-------
TABLE 2-37
SUMMARY OF FUGITIVE EMISSION OBSERVATIONS
PRIMARY CRUSHER TP-6 CRUSHER BUILDING
SPRAYS OFF
Test No. 1 2 3 Average
Date 8/28 8/28 8/28
Test Period 0833-1100 1222-1452 1528-1752
Test Duration (sec.) 8820 9000 8640 8820
Duration of Fugitive
Emissions (sec.) 000 0
Fugitive Emissions 0.0 0.0 0.0 0.0
Frequency (%)
-70-
-------
TABLE 2-38
TRACE ELEMENT ANALYSIS
PRIMARY CRUSHER - SPRAYS OFF
Element
Concentration in
Sample3 (ppm)
COPPER
NICKEL
COBALT
IRON
MANGANESE -
CHROMIUM —
VANADIUM —
TITANIUM —
SCANDIUM —
CALCIUM
POTASSIUM -
CHLORINE —
SULFUR
PHOSPHORUS
SILICON —
ALUMINUM —
MAGNESIUM -
SODIUM
FLUORINE —
CARBON
BORON
BERYLLIUM -
LITHIUM —
CERIUM
LANTHANUM -
BARIUM
CESIUM
IODINE
TELLURIUM -
ANTIMONY —
TIN
INDIUM
CADMIUM —
SILVER
PALLADIUM -
RHODIUM —
RUTHENIUM -
MOLYBDENUM
NIOBIUM —
ZIRCONIUM -
20.
20.
<2.
M
M
<2.
10.
M
1.
M
M
5.
M
5.
M
M
A
M
M
5.
A
20.
10.
20.
50.
50.
M
50.
20.
-71-
-------
TABLE 2-38 (Con't)
Concentration in
Element Sample^ (ppm)
YTTRIUM 20.
STRONTIUM 5.
RUBIDIUM 500.
BROMINE <0.5
SELENIUM <0.5
ARSENIC 10.
GERMANIUM <2.
GALLIUM 5.
ZINC 100.
URANIUM 5.
THORIUM <1.
BISMUTH <1.
LEAD 20.
THALLIUM ' <1.
MERCURY • <2.
GOLD <1.
PLATINUM <2.
IRIDIUM <1.
OSMIUM <2.
RHENIUM <2.
TUNGSTEN 5.
TANTALUM <1.
HAFNIUM <2.
LUTETIUM <0.2
YTTERBIUM <1.
THULIUM <0.2
ERBIUM <1.
HOLMIUM <0.2
DYSPROSIUM <1.
TERBIUM <0.2
GADOLINIUM <1.
EUROPIUM <1.
SAMARIUM <1.
NEODYMIUM —• <1.
PRASEODYMIUM 5.
a Filter, TP1, Transfer Points Exhaust Duct, Run 3
A = Matrix Interference
M = Signifies Major Constituent of Sample
-72-
-------
TABLE 2-39
SUMMARY OF EMISSION TEST RESULTS
PEBBLE SCREENING AND MILLING TP-1 SCREEN EXHAUST DUCT
English Units
Test No.
Average
General Data
Date
Time
Isokinetic Ratio (%)
Gas Data
Velocity (fps)
Flow (scfmd)
Temperature (°F)
Moisture (%)
Particulate Emissions
Gr./scfd
Lbs/Hr
8/29
1223-1450
97.7
8/29
1548-1710
101.1
8/30
0854-1034
106.1
71.9
1435
74.1
0.0
0.00724
0.09
65.5
1278
80.0
1.1
0.00770
0.08
64.2
1273
70.0
1.4
0.00814
0.09
101.6
67.2
1329
74.7
0.8
0.00769
0.09
-73-
-------
TABLE 2-40
SUMMARY OF EMISSION TEST RESULTS
PEBBLE SCREENING AND MILLING TP-1 SCREEN EXHAUST DUCT
Metric Units
Test No.
Average
General Data
Date 8/29 8/29
Time 1223-1450 1548-1710
Isokinetic Ratio (%) 97.7 101.1
Gas Data
Velocity (mps) 21.9 20.0
Flow (dnm^/min.) 41 36
Temperature (°C) 23.4 26.7
Moisture (%) 0.0 1.1
Particulate Emissions
Mg/nm3 16.57 17.61
Kg/Hr 0.04 0.04
8/30
0854-1034
106.1
19.6
36
21.1
1.4
18.63
0.04
101.6
20.5
38
23.7
0.8
17.60
0.04
-74-
-------
PARTICLE SIZE DISTRIBUTION
100.0
99.99
99.9 99.8 99 98 95 90
80706050403020 10 5
2 1 0.5 0.2
""» °'01 100.0
CLIMAX MOLYBDENUM
PEBBLE SCREENING AND MILLING
TP-1 SCREEN EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 1
FIGURE 2-18
0.2
0.1
0.01 O.OS 0.1 0.2 0.5 1
90 95
98 99
99.8 99.9
99.99
O.I
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
-75-
-------
PARTICLE SIZE DISTRIBUTION
IOO.O
99.99 99.9 99.8
99 98 95 90 80 70 60 50 40 30 20
O.OS 0.01
CLIMAX MOLYBDENUM
PEBBLE SCREENING AND MILLING
TP-1 SCREEN EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 2
FIGURE 2-19
100.0
8O.O
70.0
60.0
50.0
40O
30X3
20.0
10.0
9.0
8.0
7.0
6.0 O
9.0
4.0
3.0
2.0
I
O
I
i
(A
i
1.0
0.9
0.8
0.7
0.6
0.5
0.4
= . 0.3
0.2
0.1
0.01 0.05 0.1 0.2 0.5 1 2 5 10 20 30 40 50 60 70 30 90 95 98 99 99.8 99.9 99.99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
O.I
-76-
-------
PARTICLE SIZE DISTRIBUTION
IOO.O
99.99
99.9 99.8
0.2 0.1 O.OS 0.01
10 0.0
CLIMAX MOLYBDENUM
PEBBLE SCREENING AND MILLING
TP-1 SCREEN EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 3
FIGURE 2-20
0.2
0.1
O.I
0.01 O.OS 0.1 0.2 0.5 1
20 30 40 50 60 70 80
90 95
99.8 99.9 99.99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
-77-
-------
TABLE 2-41
SUMMARY OF EMISSION TEST RESULTS
PEBBLE SCREENING AND MILLING TP-2 BUCKET ELEVATOR EXHAUST DUCT
English Units
Test No.
Average
General Data
Date 8/29 8/29
Time 1218-1450 1542-1703
Isokinetic Ratio (%) 102.8 106.0
8/30
0854-1034
109.4
106.1
Gas Data
Velocity (fps) 67.1
Flow (scfmd) 796
Temperature (°F) 65.6
Moisture (%) 0.7
Particulate Emissions
Gr./scfd 0.04492
Lbs/Hr 0.31
64.5
741
69.1
3.1
0.08399
0.53
62.7
738
65.0
1.5
0.06303
0.40
64.7
759
66.6
1.8
0.06398
0.41
-78-
-------
TABLE 2-42
SUMMARY OF EMISSION TEST RESULTS
PEBBLE SCREENING AND MILLING TP-2 BUCKET ELEVATOR EXHAUST DUCT
Metric Units
Test No.
Average
General Data
Date 8/29 8/29
Time . 1218-1450 1542-1703
Isokinetic Ratio (%) 102.8 106.0
Gas Data
Velocity (mps) 20.5 19.7
Flow (dnm3/min.) 23 21
Temperature (°C) 18.7 20.6
Moisture (%) 0.7 3.1
Particulate Emissions
Mg/nm3 102.79 192.20
Kg/Hr 0.14 0.24
8/30
0854-1034
109.4
19.1
21
18.3
1.5
144.23
0.18
106.1
19.7
21
19.2
1.8
146.41
0.19
-79-
-------
100.0
99.99
99.9 99.8
PARTICLE SIZE DISTRIBUTION
99 98 95 90 80 70 60 50 40 30 20 10 5
1 0.5 0.2 0.1 0.05
CLIMAX MOLYBDENUM
PEBBLE SCREENING AND MILLING
TP-2 BUCKET ELEVATOR EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 1
FIGURE 2-21
100.0
O.I
0.01 0.05 0.1 0.2 0.5 1 2 5 10 20 30 40 50 60 70 80 90 95 98 99 99.8 99.9
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
99.99
-80-
-------
PARTICLE SIZE DISTRIBUTION
100.0
99.99 99.9 99.8
99 98 95 90
0.2
0.01
CLIMAX MOLYBDENUM
PEBBLE SCREENING AND MILLING
TP-2 BUCKET ELEVATOR EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 2
FIGURE 2-22
100.0
80.0
70.0
60.0
30.0
400
30O
20.0
10.0
9.0
8.0
7.0
6.0
5.0
4.0
3.0
a
a
Jo
z
o
or
o
2.0
N
in
u
o
P
cc
0.
i.o
0.9
0.8
0.7
0.6
0.9
= 0.4
= . 0.3
~ 0.2
0.1
0.01 0.05 0.1 0.2 0.5 1
10
20 30 40 50 60 70 80
90 95
98 99
99.8 99.9
99.99
O.I
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
-81-
-------
PARTICLE SIZE DISTRIBUTION
100.0
99.99 99.9 99.8
99
02 010.05 0.01 ,000
80.0
70.0
8O.O
£0.0
400
300
20.0
80706050403020 10 5
CLIMAX MOLYBDENUM
PEBBLE SCREENING AND MILLING
TP-2 BUCKET ELEVATOR EXHAUST
PARTICLE SIZE DISTRIBUTION
TEST 3
FIGURE 2-23
O.I
10.0
9.0
8.0
7.0
6.0
9.0
4.0
3.0
2.0
I
1.0
0.9
0.8
0.7
0.6
0.5
= . 0.4
= , 0.3
0.2
0.01 0.05 0.1 0.2 0.5 1 2 5 10 20 30 40 50 60 70 80 90 95 98 99 99.8 99.9 99.99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
O.I
-82-
-------
TABLE 2-43
SUMMARY OF EMISSION TEST RESULTS
PEBBLE SCREENING AND MILLING TP-2A TOTAL SCRUBBER INLET
English Units
Test No.
Average
General Data
Date 8/29 8/29
Time 1220-1506 1548-1728
Isokinetic Ratio (%) 104.1 106.5
Gas Data
Velocity (fps) 81.2 76.4
Flow (scfmdj ' 4120 3843
Temperature (°F) 79.6 80.0
Moisture (%) 1.4 2.1
Particulate Emissions
Gr./scfd 0.03629 0.05711
Lbs/Hr 1.28 1.88
8/30
0858-1059
102.0
76.0
5593
74.0
0.9
0.08651
2.90
104.2
77.9
5732
77.8
1.5
0.05997
2.02
-83-
-------
TABLE 2-44
SUMMARY OF EMISSION TEST RESULTS
PEBBLE SCREENING AND MILLING TP-2A TOTAL SCRUBBER INLET
Metric Units
.Test No. 1 2 3 Average?
General Data
Date 8/29 8/29 8/30
Time 1220-1506 1548-1728 0858-1059
Isokinetic Ratio (%) 104.1 106.5 102.0 104.2
Gas Data
Velocity (mps) 24.8 23.3 23.2 23.7
Flow (dnm3/min.) 117 109 111 112
Temperature (°C) 26.4 26.7 23.3 25.5
Moisture (%) 1.4 2.1 0.9 1.5
Particulate Emissions
Mg/nm3 83.05 130.70 197.97 137.24
Kg/Hr 0.58 0.85 1.32 0.92
-84-
-------
PARTICLE SIZE DISTRIBUTION
o oos o.oi ,00.0
90.0
70.0
80.0
50.0
40O
30jO
2O.O
CLIMAX MOLYBDENUM
PEBBLE SCREENING AND MILLING
TP-2A TOTAL SCRUBBER INLET
PARTICLE SIZE DISTRIBUTION
TEST 1
FIGURE 2-24
0.1
10.0
9.0 'g
a.o o
7.0
-------
PARTICLE SIZE DISTRIBUTION
IOO.O
99.99 99.9 99.8
99 98 95 90
80
CLIMAX MOLYBDENUM
PEBBLE SCREENING AND MILLING
TP-2A TOTAL SCRUBBER INLET
PARTICLE SIZE DISTRIBUTION
TEST 2
FIGURE 2-25
0.1
100.0
8O.O
70.O
6QO
3QO
40O
30O
20.0
iao
9.0 ••
8.0 £
7.0 V)
6.0 ^
,ol
4.0
3.0
2.0
I
i
o
i
1.0
0.9
0.8
0.7
0.6
0.5
0.4
0.3
0.2
0.01 0.05 0.1 0.2 0.5 1 2 5 10 20 30 40 SO 60 70 80 90 95 98 99 99.8 99.9 99.99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
O.I
-86-
-------
PARTICLE SIZE DISTRIBUTION
100.0
99.99 99.9 99.8
99 98 95 90 80 70 60 50
O.OS 0.01
100.0
CLIMAX MOLYBDENUM
PEBBLE SCREENING AND MILLING
TP-2A TOTAL SCRUBBER INLET
PARTICLE SIZE DISTRIBUTION
TEST 3
FIGURE 2-26
0.2
0.1
0.01 0.050.1 0.2 0.5 1 2 5 10 20 30 40 50 60 70 80 90 95 98 99 99.899.9 99.99
CUMULATIVE PER CENT BY WEIGHT LESS THAN(Dp)
O.I
-87-
-------
TABLE 2-45
SUMMARY OF EMISSION TEST RESULTS
PEBBLE SCREENING AND MILLING TP-3 SCRUBBER OUTLET
English Units
Test No.
General Data
Date
Time
Isokinetic Ratio (%)
Gas Data
Velocity ( f ps )
Flow (scfmd)
Temperature (°F)
Moisture (%)
Particulate Emissions
Gr./scfd
Lbs/Hr
1
8/29
1220-1446
96.5
40.3
5095
55.0
1.9
0.00956
0.42
2
8/29
1546-1727
96.7
46.2
5868
54.8
2.0
0.00496
0.25
3
8/30
0903-1120
97.6
49.3
6258
51.1
2.9
0.00582
0.31
Average
-
96.9
45.3
5740
53.6
2.3
0.00678
0.33
-88-
-------
TABLE 2-46
SUMMARY OF EMISSION TEST RESULTS
PEBBLE SCREENING AND MILLING TP-3 SCRUBBER OUTLET
Metric Units
Test No. 1 2 3 Average
General Data
Date 8/29 8/29 8/30
Time 1220-1446 1546-1727 0903-1120
Isokinetic Ratio (%) 96.5 96.7 97.6 96.9
Gas Data
Velocity (mps) 12.3 14.1 15.0 13.8
Flow (dnm3/min.) 144 166 177 163
Temperature (°C) 12.8 12.7 10.6 12.0
Moisture (%) 1.9 2.0 2.9 2.3
Particulate Emissions
Mg/nm3 21.88 11.35 13.31 15.51
Kg/Hr 0.19 0.11 0.14 0.15
-89-
-------
PARTICLE SIZE DISTRIBUTION
100.0
99.99 99.9 99.8
98 95 90 80 70 60 50 40 30 20 10 5 2 1 0.5 0.2 0.1 0.05 0.01
CLIMAX MOLYBDENUM
PEBBLE SCREENING AND MILLING
TP-3 SCRUBBER OUTLET
PARTICLE SIZE DISTRIBUTION
TEST 1
FIGURE 2-27
o.z
too.o
80.0
70.0
80.0
30.0
40O
300
20.0
IQ.O
9.0
8.0
7.0
8.0
3.0
4.0
3.0
2.0
1
1
-------
TABLE 2-47
SUMMARY OF OPACITY MEASUREMENTS
PEBBLE SCREENING AND MILLING - TP-3 - SCRUBBER OUTLET
Test No.
Date
Time
Six Minute
Interval
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
1
8/29/79
1215-1405
0
0
0
0
0
0
0
0
0
0
0
5
0
0
0
0
0
0
Oa
2
8/29/79
1643-1726
- AVERAGE OPACITY (%) -
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Ob
-
3
8/30/79
0857-1047
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Oa
a Two Minute Interval
k Four Minute Interval
-91-
-------
TABLE 2-48
SUMMARY OF OPACITY MEASUREMENTS
PEBBLE SCREENING AND MILLING - TP-4 - BUCKET ELEVATOR HOOD
Test No.
Date
Time
Six Minute
Interval
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
1
8/29/79
1215-1415
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
2
8/29/79
1545-1705
- AVERAGE OPACITY (%) -
0
0
0
0
0
0
0
0
0
0
0
0
0
Oa
-
^m
-
-
_
-
3
8/30/79
0900-1043
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Ob
-
-
..
-
a Two Minute Interval
b Four Minute Interval
-92-
-------
TABLE 2-49
SUMMARY OF FUGITIVE EMISSION OBSERVATIONS
PEBBLE SCREENING AND MILLING TP-4 BUCKET ELEVATOR HOOD
Test No. 1 2 3 Average
Date 8/29 8/29 8/30
Test Period 1215-1415 1545-1705 0857-1047
Test Duration (sec.) 7200 4800 6000 6000
Duration of Fugitive
Emissions (sec.) 000 0
Fugitive Emissions 0.0 0.0 0.0 0.0
Frequency (%)
-93-
-------
TABLE 2-50
SUMMARY OF OPACITY MEASUREMENTS
PEBBLE SCREENING AND MILLING - TP-5 - SCREEN HOOD
Test No.
Date
Time
Six Minute
Interval
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
1
8/29/79
1340-1510
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Oa
—
—
.
-
2
8/29/79
1548-1728
- AVERAGE OPACITY (%) -
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Ob
-
.
-
3
8/30/79
0904-1100
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Oc
a One Minute Interval
b Three Minute Interval
c Two Minute Interval
-94-
-------
TABLE 2-51
SUMMARY OF FUGITIVE EMISSION OBSERVATIONS
PEBBLE SCREENING AND MILLING TP-5 SCREEN HOOD
Test No. 1 2 3 Average
Date 8/29 8/29 8/30
Test Period 1340-1510 1548-1728 0900-1100
Test Duration (sec.) 5400 6000 7200 6200
Duration of Fugitive
Emissions (sec.) 000 0
Fugitive Emissions 0.0 0.0 0.0 0.0
Frequency (%)
-95-
-------
TABLE 2-52
SUMMARY OF OPACITY MEASUREMENTS
COARSE ORE STOCKPILE - TP-1 - WEST OF STOCKPILE
Test No.
Date
Time
1
8/23/79
1305-1405
2
8/23/79
1415-1515
3
8/23/79
1520-1620
Six Minute
Interval - AVERAGE OPACITY (%) -
1
2
3
10
10
5
0
1
3
4
2
0
4
5
6
4
0
0
1
4
1
7
10
7
7
8
9
10
0
0
0
0
5
0
0
0
2
5
3
4
-96-
-------
TABLE 2-53
SUMMARY OF FUGITIVE EMISSION OBSERVATIONS
COARSE ORE STOCKPILE TP-1 WEST OF STOCKPILE
Test No. 1 2 3 Average
Date 8/23 8/23 8/23
Test Period 1305-1405 1415-1515 1520-1620
Test Duration (sec.) 3600 3600 3600 3600
Duration of Fugitive
Emissions (sec.) 792 649 1963 1135
Fugitive Emissions 22.0 18.0 54.5 31.5
Frequency (%)
-97-
-------
TABLE 2-54
SUMMARY OF OPACITY MEASUREMENTS
COARSE ORE STOCKPILE - TP-2 - EAST OF STOCKPILE
Test No.
Date
Time
1
8/23/79
1305-1405
2
8/23/79
1415-1515
3
8/23/79
1520-1620
Six Minute
Interval - AVERAGE OPACITY (%) -
1
2
3
4
1
0
0
0
0
1
0
0
4
5
6
0
0
0
0
0
0
3
0
0
7
8
9
10
0
0
0
0
0
0
0
0
0
1
0
1
-98-
-------
TABLE 2-55
SUMMARY OF FUGITIVE EMISSION OBSERVATIONS
COARSE ORE STOCKPILE TP-2 EAST OF STOCKPILE
Test No. 1 2 3 Average
Date 8/23 8/23 8/23
Test Period 1305-1405 1415-1515 1520-1620
Test Duration (sec.) 3600 3600 3600 3600
Duration of Fugitive
Emissions (sec.) 309 60 390 253
Fugitive Emissions 8.6 1.7 10.8 7.0
Frequency (%)
-99-
-------
TABLE 2-56
SUMMARY OF OPACITY MEASUREMENTS
TAILINGS DISPOSAL - TP-1 - WEST OF POND
Test No.
Date
Time
1
8/23/79
0830-0930
2
8/23/79
0945-1045
3
8/23/79
1100-1200
Six Minute
Interval - AVERAGE OPACITY (%) -
1
2
3
4
5
6
0
0
1
3
0
0
0
0
0
0
0
0
0
0
0
0
0
0
7
8
9
10
0
0
0
0
0
0
0
0
1
0
0
0
-100-
-------
TABLE 2-57
SUMMARY OF FUGITIVE EMISSION OBSERVATIONS
TAILINGS DISPOSAL TP-1 WEST OF POND
Test No. 1 2 3 Average
Date 8/23 8/23 8/23
Test Period 0830-0930 0945-1045 1100-1200
Test Duration (sec.) 3600 3600 3600 3600
Duration of Fugitive
Emissions (sec.) 310 0 60 123
Fugitive Emissions 8.6 0.0 1.7 3.4
Frequency (%)
-101-
-------
TABLE 2-58
SUMMARY OF OPACITY MEASUREMENTS
TAILINGS DISPOSAL - TP-2 - EAST OF POND
Test No.
Date
Time
1
8/23/79
0830-0930
2
8/23/79
0945-1045
3
8/23/79
1100-1200
Six Minute
Interval - AVERAGE OPACITY (%) -
1
2
3
0
0
0
1
0
1
0
3
3
4
5
6
7
8
9
10
0
0
0
0
0
0
0
0
1
0
0
0
0
0
0
0
0
0
0
1
0
-102-
-------
TABLE 2-59
SUMMARY OF FUGITIVE EMISSION OBSERVATIONS
TAILINGS DISPOSAL TP-2 EAST OF POND
Test No. 1 2 3 Average
Date 8/23 8/23 8/23
Test Period 0830-0930 0945-1045 1100-1200
Test Duration (sec.) 3600 3600 3600 3600
Duration of Fugitive
Emissions (sec.) 0 192 363 185
Fugitive Emissions 0.0 5.3 ' 10.1 5.1
Frequency (%)
-103-
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TABLE 2-60
SUMMARY OF OPACITY MEASUREMENTS
TRUCK LOADING
0901-1348 AUGUST 29, 1979
General Data
Time Duration (Minutes) Average Opacity %
Truck 1
Tank 1
Tank 2
Tank 3
Truck 2
Tank 1
Tank 2
Tank 3
Truck 3
Tank 1
Tank 2
Tank 3
Truck 4
Tank 1
Tank 2
Tank 3
Truck 5
Tank 1
Tank 2
Tank 3
Truck 6
Tank 1
Tank 2
Tank 3
27
4.5
7.5
8.5
25
10.0
5.0
7.0
38
5.0
6.0
18.0
24
6.0
6.0
10.0
23
5.0
6.0
9.25
27
5.0
8.0
8.0
5
5
2
1
1
3
0
1
0
0
0
0
0
0
0
0
1
0
-104-
-------
TABLE 2-61
SUMMARY OF FUGITIVE EMISSION OBSERVATIONS
TRUCK LOADING
1
M
O
Ul
1
Truck No.
Date
Test Period
Test Duration (Sec.)
Duration of Fugitive
Emission (Sec.)
Fugitive Emissions
Frequency (%)
1
8/29
0902-0928
1560
737
47.2
2
8/29
1000-1026
1560
810
51.9
3
8/29
1102-1141
2460
325
13.2
4
8/29
1157-1222
1500
220
14.7
5
8/29
1245-1309
1440
25
1.7
6
8/29
1320-1347
1620
170
10.5
Average
-
-
1690
381
22.5
-------
TABLE 2-62
SUMMARY OF ORE SAMPLE ANALYSIS
Samplea
A
B
C
D
E
F
G
Location
Train
Conveyor
Train
Conveyor
Conveyor From
Stockpile
Conveyor To
Screen
Conveyor Leaving
Bucket Elevator
Date
8/27
8/27
8/28
8/28
8/29
8/29
8/29
Time
0840
0900
1015
1030
1228
1230
1345
Moisture
(%)
2.49
1.74
3.52
4.37
1.78
2.23
1.43
Degree
of
Hardness13
RC 65-70
RC 68-70
a See Appendix 6.2 for detailed description of samples.
b Only requested for Samples A and C.
-106-
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3.0 PROCESS INFORMATION
3.1 Process Description
A schematic flow diagram of the process is shown in Figure
3-1. Molybdenum occurs in the ore body as molybdenite (MoS2)
deposited with quartz and, to a lesser extent, with quartz-
fluorite. The ore is transferred by railcars through a 9.8
mile tunnel and a 4.8 mile surface rail to the Henderson Mill.
The rated capacity of the mill is 27,215 MT/day (30,000 tons/
day), while the 1978 operating rate was 16,100 MT/day (17,750
T/day). The plants' major processes are primary crushing,
screening, milling, and drying. The primary, crushing stage
includes a grizzly and a gyratory crusher to produce an ore to
9 inches. After being conveyed to storage bins, a screening
operation occurs to remove large pebbles (>1 1/2 x 3" size).
In the milling process, the ore passes through four cleaners,
three regrinds, and one of three semi-autogenous mills. The
final process in the wet process is filtration. The tailings
are fed by gravity to a 200 - 300 acre tailing pond. Drying of
the filter cake occurs at 50 - 60°C. A screw conveyor lifts
the finished process products to 7 or 10 ton tote bins or to 55
gallon drums. The product is then trucked 35 miles to a rail
head to be sold as concentrate or shipped to converters in the
United States or overseas.
Average mined ore characteristics are 3 percent moisture and
0.49 percent MoS2• The end product is 91 percent MoS2 at - 325
mesh or is further upgraded to 98 percent MoS2 through further
milling and flotation or through a 185°F leach in 5 percent HC1
to remove lead. Moisture contents before and after drying are
15 percent and 3 percent respectively.
Detailed descriptions of the operations and control equipment
tested are given in the following sections.
-107-
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MM feed
FLOW SHEET
HENDERSON MILL
Live ore storage
65%-100 Mesh feed
Ftocculanl Ihne
Overflow
JZnd Renrihd
*H t5
Reagents 1 »L fc
Concentrate
A (Decant wat
I | recycled
Concentrate holding tanks
ondMonerlH-
To lead leach circuit
o leach filters
TalRng pond
-------
Railcar Unloading, Primary Crushing, Coarse Ore Stockpile
Railcar unloading and primary crushing are the only operations
at Henderson that are not continuous. A typical train has 20,
19-ton cars and offloads at a rate of 100 tons/minute. Crude
ore is dumped through hinged car bottoms, and passes through a
grizzly, and a 54 x 84 inch Traylor gyratory crusher that re-
duces an ore to 9 inches. Ore then passes through an apron
feeder to a conveyor belt. Between the finish of one train
unloading and the start of another there is a delay of 15 - 30
minutes.
Emissions from these operations are controlled by wet suppres-
sion and a wet scrubber. The wet suppression system (Johnson-
March) is automatically activated as water is sprayed over 3/4
of the pit entrance, at the bottom of the crusher and at the
apron feeder. A Ducon Dynamic Wet Scrubber, Type UW-4, Model
III receives exhaust from the pit, bottom of the primary
crusher and the apron feeder. Plant data indicate that the
flow rate is 66,000 acfm at 60°F with a particulate concent-
ration of 1 grain/dscf.
Ore from the primary crusher travels 1000 feet by enclosed con-
veyor to overhead average drop points that fill one of three
stockpiles. Average stockpile dimensions are 430 feet x 272
feet base x 40 feet height. A water spray system is used to
control emissions.
Pebble Screening and Milling
An underground ore conveying system transfers crushed ore from
the stockpiles to one of three primary mills. Before milling,
screening removes large pebbles. Undersize ore goes through
three regrind mills via a critical sizing operation with a
final 1 1/2 x 3 inch size pebble as the regrind circuit
medium. Oversize goes to the pebble mill as a regrind medium.
-109-
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Milling occurs through one of three semi-autogenous mills (28
feet diameter x 14 feet) which uses a ball charge of 10 per-
cent, 5 inch balls. Milling is a conventional process includ-
ing four cleaners and three regrinders with vacuum filtration
as the final step. The resulting filter cake has a moisture
content of 15-20 percent before going to the dryers. Mill
tailings are a 35 percent solids slurry that is gravity fed to
a 200-300 acre (808,000 m2 - 1,212,000 m2) tailings pond.
A Ducon size 48 wet scrubber, Type UW-4, receives emissions
from a transfer point (reclaim conveyor to pebble screen) and
from the bucket elevator. Plant data show a flow rate of 5200
acfm at 70°F with a particulate concentration of 0.1 grain/
dscf.
Dryers
The dryers receive a 15-20 percent filter cake from the wet
mill process. Dryer temperature is 50-60°C using process heat
from steam generation. There are six Holoflite dryers. Four
(two at any one time, used in series) are used to produce 91
percent MoS2, with the other two used for producing 97 percent
MoS2. The final mill product has 3 percent moisture at -325
mesh. The dryer product is transferred by totally enclosed
screw conveyors into two 230T storage bins. It is delivered to
7 or 10 ton bins or 55 gallon drums and is trucked 35 miles to
a rail head.
A Ducon wet scrubber size 42 Type UW is used with a flow rate
of 4050 acfm at 85°F with a particulate concentration of 0.012
grain/dscf.
-110-
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3.2 Process Operation During Test
Primary Crusher/Railcar Unloading
These operations are cyclic with an average of three trains per
hour, with approximately 22 railcars (19 tons each), offload-
ing. It takes an average of 5 minutes to unload ore and 8
additional minutes for ore to leave the surge bin and be placed
on conveyor belts. Crusher tests were run continuously because
of these time constraints.
On August 27, three emission tests were run with the wet sup-
pression system on. During the first test only two trains
entered the crusher building during the 2 1/2 hour test
period and therefore the results are not considered to be
representative of the process. On August 28, three emission
tests were conducted with wet suppression system off. No major
problems arose and the production process was proceeding at a
normal rate.
A summary of the visual test results are presented in Table
3-1.
Pebble Screening and Milling
The operation of this process had been reduced by about 85 per-
cent prior to testing and was only operated for test purposes.
The pebble screen is used sparingly because the plant obtains
better pebble after the ore has passed through the grinding
mill. The process was determined to be running normally if the
conveyor belt was loaded with coarse ore. Testing was
discontinued every half hour when the grizzly leading to the
pebble screen conveyor became jammed with ore.
Table 3-2 summarizes the visual test results.
-Ill-
-------
TABLE 3-1
SUMMARY OF VISUAL TEST RESULTS
PRIMARY CRUSHER/RAIL CAR UNLOADING
Method 9
Location
Scrubber Outlet (TP-3)*
Scrubber Outlet
Transfer Point Hood (TP-4)*
Transfer Point Hood
Railcar Unloading (TP-5)*
Railcar Unloading
Crusher Building (TP-6)*
Crusher Building
Date
8-27
8-28
8-27
8-28
8-27
8-28
8-27
8-28
No. of 6 Minute
Intervals
46
72
40
60
19
61
47
73
Opacity Reading
Average
7
6
0
2
0
1
0
0
Maximum
10
10
0
6
1
3
0
0
Location Date
Transfer Point Hood (TP-4)* 8-27
Transfer Point Hood 8-28
Railcar Unloading (TP-5)* 8-27
Railcar Unloading 8-28
Crusher Building (TP-6)* 8-27
Crusher Building 8-28
Method 22
Test Duration
(sec.)
14400
21600
14400
22140
17220
26460
Fugitive Emission
(sec. )
30
8715
257
1580
0
0
Fugitive Emission
Frequency (%)
0.1
40
1.8
7.0
0
0
Sprays On
-------
TABLE 3-2
SUMMARY OF VISUAL TEST RESULTS
PEBBLE SCREENING AND MILLING
Method 9
Location
Pebble Screen-Scrubber
Outlet (TP-3)
Pebble Screen-Bucket
Elevator Hood (TP-4)
Pebble Screen-Screen
Hood (TP-5)
Date
8-29/
8-30
8-29/
8-30
8-29/
8-30
No. of 6 Minute
Intervals
53
48
50
Opacity Reading
Average Maximum
0
0
0
0
0
0
Location
Pebble Screen-Bucket
Elevator Hood
Pebble Screen-Screen
Hood (TP-5)
Date
8-29/
8-30
8-29/
8-30
Method 22
Test Duration
(sec.)
18000
18600
Fugitive Emission
(sec.)
0
0
Fugitive Emissio
Frequency (%)
0
0
-------
Molybdenum Dryers
After the ore has been concentrated by the wet mill process, it
passes through a two-stage Holoflite dryer before being loaded
into trucks. During testing, another two-stage Holoflite dryer
was running to handle the excess load. Instrumentation was not
available to monitor the operation of the process or the con-
trol equipment. Visible inspections of conveyor belts, stack
emissions and weight scales for truck loading were used to
determine if the process was operating at representative
steady-state conditions.
The first emission test began on August 23, 1979, but was nul-
lified (see Section 2.1). Three valid tests were performed on
August 23-24. During the entire test period, trucks were being
filled with concentrate ore. A summary of emission observ-
ations is presented in Table 3-3.
-114-
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TABLE 3-3
SUMMARY OF VISUAL TEST RESULTS
MOLYBDENUM DRYERS
Location
Dryer-Srubber Outlet (TP-2)
Dryer Area (TP-3)
Date
8-23/24
8-23/24
Method 9
No. of 6 Minute
Intervals
48
30
Opacity Reading
Average Maximum
15
0
24
0
Location
Date
Method 22
Test Duration
(sec.)
Fugitive Emission
(sec.)
Fugitive Emission
Frequency (%)
Dryer Area (TP-3)
8-23/24
10800
0
0
-------
4.0 SAMPLING METHODS
4.1 Test Port Locations and Sampling Point Determination
The location of the test ports and sampling points at each
location was determined in accordance with guidelines
outlined in EPA Method 1 (Sample and Velocity Traverses
for Stationary Sources).
Molybdenum Dryer
The sampling ports at the Molybdenum Dryer Inlet (TP-l)
are located in the ductwork between the common outlet of
the two dryers and the Ducon scrubber. The duct is 24.75
inches in diameter at this point. The ports are 75 inches
downstream (3.03 duct diameters) and 75 inches upstream
(3.03 duct diameters) from the nearest flow disturbances.
At this location, EPA Method 1 requires that 28 traverse
points be sampled. Fourteen points were sampled in each
of two ports (Figure 4-1) for three minutes each resulting
in a total test time of 84 minutes.
The sampling ports at the Molybdenum Dryer Outlet (TP-2)
are located in the stack which vents the exhaust from the
Ducon scrubber to the atmosphere. The stack is 21.5
inches in diameter at this point. The ports are at least
172 inches downstream (8.0 duct diameters) and 44.5 inches
(2.07 duct diameters) upstream of the nearest flow
disturbances. At this location, EPA Method 1 requires
that 8 traverse points be sampled. Four points were
sampled in each of two ports (Figure 4-2) for twelve
minutes each resulting in a total test time of 96
minutes.
-116-
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Sampling Point
1
2
3
4
5
6
7
8
9
10
11
12
13
14
Distance from stack wall (inches)
1.00
1.41
2.45
3.61
4.97
6.66
. 9.06
15.69
18.09
19.77
21.14
22.30
23.34
23.75
Molybdenum Dryer
TP-1 Sampling Point Locations
Figure 4-1
-117-
-------
Sampling Point
1
2
3
4
Distance from stack wall (inches
1.00
5.38
16.12
20.50
Molybdenum Dryer
TP-2 Sampling Point Locations
Figure 4-2
-118-
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Visual tests for opacity levels were taken at the
stack outlet (TP-2). The observer' was located on the roof
of the building in the area of the stack. Visual
observations for opacity and fugitive emissions were made
in the area of the dryers (TP-3). The observers were
located on the same level as the dryers observing the
general dryer area.
Primary Crusher/Rail Car Unloading
The sampling ports at the Primary Crusher Transfer Point
Exhaust (TP-1) are located in the ductwork that vents the
exhaust from the conveyor at the apron feeder and the
conveyor to the stockpile to the scrubber. The duct is 32
inches in diameter at this point. The ports are 256
inches downstream (8.0 duct diameters) and 165 inches
upstream (5.16 duct diameters) from the nearest flow
disturbances. At this location, EPA Method 1 requires
that 12 traverse points be sampled. Six points were
sampled in each of two ports (Figure 4-3) for 10 minutes
each resulting in a total test time of 120 minutes.
The sampling ports at the Primary Crusher Pit Exhaust
(TP-2) are located in the ductwork that vents the exhaust
from the crusher pit to the scrubber. The duct is 34.25
inches in diameter at this point. The ports are less than
2 duct diameters downstream and upstream from the nearest
flow disturbances. At this location, EPA Method 1
requires that 44 traverse points be sampled. Twenty-two
points were sampled in each of two ports (Figure 4-4) for
3 minutes each resulting in a total test time of 132
minutes.
The sampling ports at the Primary Crusher Scrubber Outlet
(TP-3) are located in the stack which vents exhaust from
-119-
-------
Sampling Point
1
2
3
4
5
6
Distance from stack wall (inches)
1.41
4.67
9.47
22.53
27.33
30.59
Primary Crusher
TP-1 Sampling Point Locations
Figure 4-3
-120-
-------
Sampling Point
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
Distance from stack wall (inches)
1.10
1.88
2.71
3.60
4.52
5.51
6.64
7.88
9.32
11.06
13.63
20.62
23.19
24.93
26.37
27.61
28.74
29.73
30.65
31.54
32.37
33.15
Primary Crusher
TP-2 Sampling Point Locations
Figure 4-4
-121-
-------
the scrubber. The stack is 77" in diameter at this
point. The ports are 249 inches (3.23 stack diameters)
downstream of the scrubber exit and 201 inches (2.61 stack
diameters) upstream of the stack exit. At this location,
EPA Method 1 requires that 48 traverse points be sampled.
Twenty-four points were sampled in each of two ports
(Figure 4-5) for 3 minutes each resulting in a total test
time of 144 minutes.
Visual tests for opacity levels were taken at the stack
outlet (TP-3). The observer was located outside the
crusher building north of the emission point. Visual
observations for opacity and fugitive emissions were made
at three separate locations. Observers were located at
the apron feeder (TP-4) recording emissions from the
transfer points from the crusher to the apron feeder and
conveyor to the stockpile, the crusher floor (TP-5)
recording emissions of the train unloading and crushing
operations and outside the crusher building (TP-6) record-
ing the emissions from the building.
Pebble Screening and Milling
The sampling ports at the Pebble Screening and Milling
Screen Exhaust (TP-1) are located in the ductwork which
vents the exhaust from the screens to the common inlet.
The duct is 9.25 inches in diameter at this point. The
ports are 64 inches downstream (6.92 duct diameters) and
34 inches upstream (3.68 duct diameters) of the nearest
flow disturbances. At this location, EPA Method 1 re-
quires that 8 traverse points be sampled. Four points
were sampled in each of two ports (Figure 4-6) for 10 min-
utes each resulting in a total test time of 80 minutes.
-122-
-------
Sampling Point
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
Distance from stack wall (inches)
1,
2,
00
46
4.24
6.08
8.09
10.16
12.40
14.94
17.71
20.94
24.87
30.65
46.35
52.13
56.06
59.29
62.06
64.60
66.84
68.92
70.92
72.77
74.54
76.15
Primary Crusher
TP-3 Sampling Point Locations
Figure 4-5
-------
Sampling Point
1
2
3
4
Distance from stack wall (inches)
1.00
2.31
6.94
8.25
Pebble Screening and Milling
TP-1 Sampling Point Locations
Figure 4-6
-124-
-------
The sampling ports at the Pebble Screening and Milling
Bucket Elevator Hood Exhaust (TP-2) are located in the
ductwork which vents the exhaust from the bucket elevator
to the common inlet. The duct is 7.125 inches in diameter
at this point. The ports are 153 inches downstream (21.47
duct diameters) and 37 inches upstream (5.19 duct
diameters) of the nearest flow disturbances. At this
location, EPA Method 1 requires that 8 traverse points be
sampled. Four points were sampled in each of two ports
(Figure 4-7) for 10 minutes each resulting in a total test
time of 80 minutes.
The sampling ports at the Pebble Screening and Milling
Total Inlet (TP-2A) are located in the ductwork which
vents the exhaust from the entire system to the scrubber.
The duct is 15 inches in diameter at this point. The
ports are 46 inches downstream (3.07 duct diameters) and
119 inches upstream (7.93 duct diameters) of the nearest
flow disturbances. At this location, EPA Method 1
requires that 24 traverse points be sampled. Twelve
points were sampled in each of two ports (Figure 4-8) for
4 minutes each resulting in a total test time of 96
minutes.
The sampling ports at the Pebble Screening and Milling
Scrubber Outlet (TP-3) are located in the duct which
vents the exhaust from the scrubber to the atmosphere.
The duct is 23.125 inches in diameter at this point. The
ports are 51 inches downstream (2.21 duct diameters) and
61 inches upstream (2.64 duct diameters) of the nearest
flow disturbances. At this location, EPA Method 1
requires that 28 traverse points be sampled. Fourteen
points were sampled in each of two ports (Figure 4-9) for
-125-
-------
Sampling Point
1
2
3
4
Distance from stack wall (inches)
1.
1,
5,
00
78
34
6.13
Pebble Screening and Milling
TP-2 Sampling Point Locations
Figure 4-7
-126-
-------
Sampling Point
1
2
3
4
5
6
7
8
9
10
11
12
Distance from stack wall (inches)
1.
1.
00
49
2.19
3,
4.
5,
,02
,04
,49
9.51
10.96
11.99
12.81
13.52
14.00
Pebble Screening and Milling
TP-2A Sampling Point Locations
Figure 4-8
-127-
-------
Sampling Point
1
2
3
4
5
6
7
8
9
10
11
12
13
14
Distance from stack wall (inches)
1.13
1,
2,
97
89
3.91
5.09
6.54
8.67
14.45
16.58
18.04
19.22
20.23
21.16
21.99
Pebble Screening and Milling
TP-3 Sampling Point Locations
Figure 4-9
-128-
-------
4 minutes each resulting in a total test time of 112
minutes.
Measurements of opacity levels were made at the stack out-
let (TP-3). The observer was located outside the mill
building east of the emission point. Visual observations
for opacity and fugitive emissions were made at two separ-
ate locations. Observers were located at the bucket ele-
vator transfer point (TP-4) recording emissions at the top
of the bucket elevator and at the pebble screen area
(TP-5) recording emission levels of the screening oper-
ation.
Truck Loading
Visual observations for opacity and fugitive emissions
were also made at the final product loading area. Observ-
ers were located in the building where the truck loading
took place.
Coarse Ore Stockpile and Tailings Disposal
Visual observations for opacity and fugitive emissions
were made at the coarse ore stockpile and tailings pond
areas. Two sets of observers were located, one at the
east end of the operation and one at the west end.
4 .2 Preliminary Measurements
Preliminary measurements of velocity pressure and gas
temperature were made at each location to determine gas
velocity. The measurements were made in accordance with
guidelines outlined in EPA Method 2 (Determination of
Stack Gas Velocity and Volumetric Flow Rate).
A precalibrated type "S" pitot tube and thermocouple were
rigidly attached to each sampling probe. The velocity
-129-
-------
pressure was measured on an inclined manometer, and the
temperature on a pyrometer. Readings were recorded at
each traverse point.
At the Primary Crusher Outlet, TP3, the stack flow was
determined to by cyclonic after measurements were made
according to Method 1, Section 2.4.
4.3 Gas Composition
The gas composition was determined in accordance with
guidelines outlined in EPA Method 3 (Gas Analysis for
Carbon Dioxide, Oxygen, Excess Air and Dry Molecular
Weight). Since there is no combustion involved in the
process, the gas composition at each test location was
assumed to be air. A check was made with a Fyrite®
analyzer for carbon dioxide and oxygen content.
4.4 Particulate
The particulate concentrations were determined in accord-
ance with guidelines outlined in EPA Method 5 (Determin-
ation of Particulate Emissions from Stationary Sources).
The sampling train at each location consisted of a nozzle,
probe, filter holder, impinger train and metering system.
The train is shown schematically in Figure 4-10. All con-
nections were leak free.
The proper nozzle size was determined using data from the
preliminary measurements. The stainless steel probe is
able to maintain a temperature of 248 ± 25°F. A thermo-
couple and calibrated S-type pitot tube are rigidly
attached to the probe. The exit-end of the probe was con-
nected to the fiter holder, which was contained in a heat-
ed box (also 248 ± 25°F). A flexible sample line connect-
ed the filter holder to the impinger train. The train
-130-
-------
MODIFIED PARTICULATE SAMPLING TRAIN
I
M
U)
M
I
STACK WALL
NOZZL
THERMOCOUPLE
INCLINED
\MANOMETER
(API
VACUUM GAUGE
THERMOMETER
BY-PASS
:VALVE
COARSE
CONTROL
VALVE
THERMOMETERS
ORIFICE
} *=>
PYROMETER
100 mis distilled
water
empty
AIR-TIGHT
PUMP
DRY GAS
METER
300 0
silica gel
INCLINED
MANOMETER
(AH)
Figure 4-10
ES-093
-------
consisted of five Greenburg-Smith impingers connected in
series. The first impinger was modified by replacing the
impinger tip with a blank stem. This impinger was
initially filled with 100 milliliters of distilled water.
The second impinger was a standard Greenburg-Smith
impinger containing 100 milliliters of distilled water.
The third and fourth impingers were identical to the first
and were left dry while the fifth contained 300 grams of
indicating type silica gel.
A short sample line connected the last impinger to the RAC
Train Stacksamplr® meter box which contains:
• Vacuum gauge
• Air-tight pump
• Dry gas meter (measures volume within 2 percent)
• Thermometers (measures temperature within 5.4°F)
• Calibrated orifice
• Vertical, inclined, dual manometer
• Electrical controls for sampling
During the test the following data were recorded at each
traverse point:
• Traverse point
• Sampling time
• Clock time
• Gas meter reading (cf)
• Velocity pressure (Ap, in. H2O)
• Orifice pressure drop (AH, in. H2O)
• Stack temperature (°F)
• Dry gas meter temperature-inlet and outlet (°F)
-132-
-------
• Pump vacuum (in. Hg)
• Sample box temperature (°F)
• Gas temperature at exit of last impinger (°F)
The relationship of Ap to AH is a function of the
following variables:
• Pitot tube coefficient
• Orifice calibration factor
• Gas meter temperature
• Moisture content of flue gas
• Ratio of flue gas pressure to barometric
pressure
• Stack temperature
• Sampling nozzle diameter
A nomograph was used to correlate all the above variables
such that a direct relationship between Ap and AH was
determined by the sampler and isokinetic conditions could
be maintained.
At the completion of the test, the samples were recovered
in the following manner:
Container #1 - The filter was removed from the filter
holder and placed in its original con-
tainer.
Container #2 - The nozzle, probe, cyclone bypass and
front half filter holder were brushed
with acetone. The acetone was placed
in a glass jar.
Container #3 - The silica gel was returned to its
original container.
-133-
-------
All sample containers were sealed with tape and labeled
with the date, test number and location. Glass sample
jars had Teflon-lined lids. The volume of water in the
first four impingers was measured and recorded. The water
was discarded.
4-5 Particle Size Distribution
The particle size distribution samples were collected
using an Andersen Cascade Impactor. The impactor consists
of multiple stages which collect different particle sizes
(Figure 4-11). Each stage consists of an orifice of a
specific diameter above a collection plate. The orifice
sizes of each stage are different and are arranged in
descending order, the largest being stage 1. The sampling
system was set up as shown in Figure 4-12. The stack
conditions were determined and the sample was extracted
isokinetically.
As the gas flows through each orifice, it is deflected off
a glass fiber substrate filter placed on the collection
plate, particles of a specific size become impacted on the
substrate while the remaining particles entrained in the
gas stream proceed to the next collection stage. The
range of particle sizes retained on the substrate varies
according to the velocity of the gas (as determined by the
sampling rate and orifice diameter), the gas viscosity and
the particle density. Since the orifices are arranged in
descending diameters, the gas velocity increases and the
particle size collected on each stage decreases.
During the sampling a cyclone preseparator was used to
pre-cut particles above 10 microns and avoid overloading
the collection substrates. At the completion of each test
the contents of the preseparator and an acetone wash were
-134-
-------
ANDERSEN STACK SAMPLER
BACKUP
FILTER'
JET STAGE (9 TOTAL)
SPACERS
NOZZLE
GLASS FIBER
COLLECTION
SUBSTRATE
PLATED
HOLDER
INLET
CORE
ES-095
Figure' 4-11
_•" "5 C_
-------
ANDERSEN SAMPLING TRAIN
ANDERSON
SAMPLER
IMPINGERS
PUMP
GAS METER
ORIFICE
MANOMETER
Figure 4-12
ES-094
-------
placed in a sample jar. The glass fiber substrate filters
were returned to their original containers. All sample
containers were sealed and labeled.
4.6 Opacity Measurement
Certified personnel conducted visual tests to determine
opacity in accordance with guidelines outlined in EPA
Method 9 (Visual Determination of the Opacity of Emissions
from Stationary Sources).
4.7 Fugitive Emissions Frequency
The frequency of fugitive emissions were determined in
accordance with guidelines outlined in EPA Method 22
(Visual Determination of Fugitive Emissions from Material
Sources, see Appendix 6.6).
-137-
-------
5.0 ANALYTICAL PROCEDURES
5.1 Particulate Samples
To determine particulate concentration and emission rate,
the particulate test samples were analyzed in the
following manner:
Container #1 - The filter was removed from its sealed
container and placed on a tared watch
glass. The filter and watch glass
were dessicated with anhydrous CaSC>4
and weighed to a constant weight. The
weight was recorded to the nearest
0.01 mg.
Container #2 - The acetone washings were transferred
to a tared beaker. The acetone was
then evaporated at ambient temperature
and pressure, dessicated and weighed
to a constant weight. The weight was
recorded to the nearest 0.01 mg.
Container #3 - The silica gel was weighed to the
nearest 0.1 gram on a beam balance.
Samples from the Molybdenum Dryer were then analyzed for
polonum-210 by measuring the radioactivity of the sam-
ples. A filter sample from the Primary Crusher/Rail Car
Unloading was analyzed for various trace elements by SSMS.
5.2 Particle Size Distribution Samples
The fiberglass substrate filters were dessicated and
-139-
-------
weighed to a constant weight. The net weight gain was
recorded to the nearest 0.01 mg.
The acetone rinse of the cyclone preseparator was trans-
ferred to a tared beaker. The beaker was heated to a
temperature well below the boiling point until the acetone
was evaporated. The beaker was then dessicated and
weighed to a constant weight. The net weight gain was
recorded to the nearest 0.01 mg.
Bahco analysis was also performed on certain locations due
to the high moisture content restricting applicability of
the Andersen Impactor.
5. 3 Ore Samples
Moisture Content
A representative sample was weighed and transferred to a
tared aluminum pan. The sample was dried for 24 hours at
103°C. The dried sample was dessicated and weighed. The
percent moisture was determined from the net weight loss.
Ore Hardness
Ore hardness was measured on a Rockwell® C-Scale Tester.
-140-
-------
Job No. 01-9517-17
FINAL REPORT
Prepared by
Reviewed by:
Approved by:
Maria Denaro
Project Scientist
Roorir A. KnisJe^rn
Project Manager
James W. Davison
Vice President
-------
6.0 APPENDIX
-------
6.1 Complete Computer Data Printouts
-------
Molybdenum Dryer
-------
TP-1 Scrubber Inlet
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: MQLY DRYER TP1
JOB NUMBER: 9517-17
PARTICIPATE SUMMARY IN ENGLISH UNITS
DESCRIPTION
UNITS
TPt-2
TP1-3
TP1-4
AVERAGE
GENERAL DATA
DATE OF RUN AUG
BAROMETRIC PRESSURE TN.HG
STACK PRESSURE. APS. IN.HG
STACK AREA SO. FT
NET TIME OF RUN MTN
PERCENT ISOKINETIC
GAS DATA
AVG STACK GAS VELOCITY FPS
AVG STACK TEMPERATURE DEG.F
ACTUAL STACK FLOWRATE ACFM
STK FLOWRATE, DRY. STD DSCFM
MOLECULAR WT-DRY STK GAS
MOLECULAR WT-STK GAS
MOLE FRACTION DRY GAS
GAS ANALYSIS (DRY PERCENT BASIS)
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION DATA
TOTAL H20 COLLECTED ML
VOL H20 VAPOR-STD CONO SCE
VOL DRY GAS-METER COND DEF
VOL DRY GAS-STD COND DSCF
AVG GAS METER TEMP DEG.F
AVG ORIF PRES DROP IN.H20
PARTICIPATE WEIGHT DATA
NET WEIGHT PARTIAL MG
NET WEIGHT TOTAL MG
23,79
21.42
21.18
3.34
84.0
107.4
26.124
151 .8
5237.
2611.
28.82
26.80
0.813
0.0
20.5
0.0
79.5
18.7
125.3
5.94
37.25
25.80
88.6
0.489
0.00
354.50
AUG 23,79
21.42
21.18
3.34
84.0
103.7
30.240
150.0
6062.
3106.
-28.82
27.01
0.833
0.0
20.5
0.0
79.5
16.7
125.3
5.94
42.84
29.62
89.8
0.597
0.00
322.39
AUG 24,79
21.48
21.24
3.34
84.0
96.6
27.460
150.4
5505.
3061.
28.82
27.76
0.902
0.0
20.5
0.0
79.5
9.8
62.2
2.95
38.69
27.20
82.0
0.493
0..00
517.89
102.6
27.941
150.7
5601.
2926.
0.0
20.5
0.0
79.5
15.1
0.00
398.26
PARTTCULATE EMISSIONS
PARTIAL
GRAINS PER SCFD
GRAINS PER SCFD B12%C02
GRAINS PER ACE
POUNDS PER HOUR
POUNDS PEP PROCESS UNIT
TOTAL
GRAINS PER SCFD
GRAINS PER SCFD 012%C02
GRAINS PER ACE
POUNDS PER HOUR
POUNDS PER PROCESS UMIT
0.00000
0.00000
o.ooooo
0.00
o.ooooo
0.21161
0.00000
0.10549
4.73
o.ooooo
0.00000
0.00000
0.00000
0.00
o.ooooo
0.16763
0.00000
0.08588 '
4.46
o.ooooo
o.ooooo
0.00000
0.00000
0.00
0.00000
0.29319
o.ooooo
0.16306
7.69
0.00000
0.00000
0.00000
0.00000
0.00
0.00000
0.22415
0.00000
0.11814
5.63
0.00000
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION* CMMAX MOLY
UNIT TESTED: MOLY DRYER TP1
JOB NUMBER: 9517-17
PARTTCULATE SUMMARY IN METRIC UNITS
DESCRIPTION
UNITS
TP1-2
TP1-3
TP1-4
AVERAGE
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE
STACK PRESSURE. ABS.
STACK AREA
NET TIME OF RUN
PERCENT ISOKINETIC
GAS DATA
AVG STACK GAS VELOCITY
AVG STACK TEMPERATURE DEG.C
ACTUAL STACK FLOWRATE AM3/M
STK FLOWRATE,DRY,STD DNM3/M
MOLECULAR WT-ORY STK GAS
MOLECULAR WT-STK GAS
MOLE FRACTION DRY GAS
GAS ANALYSIS (DRY PER
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION DATA
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD CONO
VOL DRY GAS-METER COND
VOL DRY GAS-STD COND
AVG GAS METER TEMP
AVG ORTF PRES DROP
PARTTCULATE WEIGHT DATA
NET WEIGHT PARTIAL
NET WEIGHT TOTAL
PARTTCULATE EMISSIONS
PARTIAL
MG/NORMAHZED CU.METERS
MG/NORM. CU.M «M2% C02
MG/ACTUAL cu. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
TOTAL
MG/NORMALIZF.D CU.METERS
MG/NORM. CU.M 012% C02
MG/ACTUAL cu. METERS
KILOGRAMS/HOUR
KTLOGM PER PROCESS UNIT
AUG
MM.HG
MM.HG
M2
MIN
M/S
DEG.C
AM3/M
NM3/M
AS
ENT BASIS)
ML
NM3
D"3
DNM3
DEG.C
M.H20
' A
A
MG
MG
23,79
544.07
538.09
0.310
84.0
107.4
7.963
66.5
148.
74.
28.82
26.80
0.813
0.0
20.5
0.0
79.5
18.7
125.3
0.17
1.05
0.73
31.4
12.419
0..00
354.50
AUG 23,79
.544.07
538.09
0.310
84.0
103.7
9.217
65.6
172.
88.
28.82
27.01
0.833
0.0
20.5
0.0
79.5
16.7
125.3
0.17
1.21
0.84
32.1
15.167
0.00
322.39
AUG 24,79
545.59
539.62
0.310
84.0
96.6
8.370
65.8
156.
87.
28.82
27.76
0.902
0.0
20.5
o.o
79.5
9.8
62.2
0.08
1.10
0.77
27.8
12.532
0..00
517.89
102.6
8.517
66.0
159.
83.
0.0
20.5
0.0
79.5
15.1
0..00
398.26
0
0.00
0.00
0.00
0.00
.00000
484.25
0.00
241.39
2.15
).00000
0.00
0.00
0.00
0.00
0.00000
383.61
0.00
196.53
2.02
0.00000
0.00
0.00
0.00
0.00
0.00000
670.94
0.00
373.14
3.49
0.00000
0.00
0.00
0.00
0.00
0.00000
512.93
0.00
270.36
2.55
o.ooooo
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE', STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: MOLY DRYER TP1
DUCT NUMBER: TP1
DUCT AREA: 3.34SQ.FT..24.75" I.D.
DUCT LOCATION: SCRUBBER INLET
FILTER NUMBERS: 03070
TEST NUMBER: Tpi-2
DATE: AUG 23,79
TEST COND: 2 DRYERS ON
BAR. PRESS-IN HG: 21.42
PITOT TUBE FACTOR: 0.900
TIME TEST STARTED: 1312
SAMPLE ELAP SAMPLE
POINT TIME VOLUME
fMIN) (DCF)
START
B-l
2
3
4
5
6
7
9
9
to
11
12
13
14
START
A-l
2
3
4
5
6
7
ft
9
to
11
12
1 J
14
0.0
3.0
6.0
9.0
12.0
15.0
18.0
21 .0
24.0
27.0
30.0
33.0
36.0
39.0
42.0
42.0
45.0
48.0
51 .0
54.0
57.0
60.0
63.0
66.0
69.0
72.0
75.0
78.0
81.0
84.0
916.
917.
918.
920.
921.
922.
923.
924.
926.
927.
928.
930.
931.
933.
936.
936.
938.
939.
941.
943.
944.
946.
947.
948.
949.
950.
951.
952.
953.
954.
798
860
750
060
160
270
350
610
120
550
920
210
780
880
711
71 1
350
950
570
200
810
400
730
950
950
930
900
660
330
044
PITOT ORIFICE METERTEMP NOZ
RDG RDG (OEG.F) DIA
fINH20)CINH20) IN OUT (IN)
0.050
0.070
0.070
0.070
0.070
0.070
0.100
0.140
0.130
0.110
0.100
0.180
0.300
0.550
0.160
0.170
0.170
0.170
0.150
0.150
0.100
0.080
0.050
0.050
0.050
0.030
0.030
0.030
0.200
0.280
0.280
0.280
0.280
0.280
0.400
0.560
0.520
0.450
0.400
0.660
1.200
2.500
0.600
0.640
0.640
0.640
0.600
0.600
0.400
0.320
0.200
0.200
0.200
0,120
0.120
0.120
80.
83.
83.
84.
85.
86.
87.
89.
90.
92.
93.
94.
95.
99.
88.
90.
92.
94.
96.
97.
98.
100.
101.
101.
103.
103.
103.
101.
80.
80.
80.
80.
80.
80.
80.
81.
82.
82.
82.
82.
83.
84.
84.
84.
85.
85.
86.
86.
86.
86.
87.
88.
89,
90.
91.
91.
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
Q..259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0,259
0,259
0.259
0.259
STACK
TEMP
(DF)
155.
155.
155.
155.
155.
155.
155.
155.
155.
155.
150.
150.
150.
150.
150.
150.
150.
150.
150.
150.
150.
150,
150.
150.
150,
150,
150.
150.
STACK
VEL
(FPS)
17.906
21.186
21.186
21.186
21.186
21.186
25.322
29.962
28.872
26.558
25.219
33.835
43.681
59.144
31.900
32.882
32.882
32.882
30.887
30.887
25.219
22.557
17.833
17.833
17.833
13.813
13.813
13.813
*I
• •
127.3
90.0
132.4
111.1
112.1
108.9
106.3
107.5
105.4
109.6
107.7
97.7
101.3
100.8
108.5
102.6
103.7
104.2
109.3
107.8
110.3
1 1 .3 . 0
116.9
114.5
113.1
114.3
100.7
107.4
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE1. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: MOLY DRYER TPI
DUCT NUMBER: TPI
DUCT AREA: 3.34SQ.FT..24.75" ID
DUCT LOCATION: SCRUBBER INLET
FILTER NUMBERS: 02350
TEST NUMBER: TPi-3
DATE: AUG 23,79
TEST COND: 2 DRYERS ON
BAR. PRESS-IN HG: 21.42
PITOT TUBE FACTOR: 0.900
TIME TEST STARTED: 1550
SAMPLE ELAP SAMPLE
POINT TIME VOLUME
(MIN) (DCF)
START
8-1
2
3
4
5
6
7
9
9
10
1 1
12
13
14
START
A-1
2
3
4
5
ft
7
8
9
1.0
11
12
13
14
0.0
3.0
6.0
9.0
12.0
15.0
18.0
21.0
24.0
27.0
30.0
33.0
36.0
39.0
42.0
42.0
45.0
48.0
51.0
54.0
57.0
60.0
63.0
66.0
69.0
72.0
75.0
78.0
81 .0
84.0
954.
956.
957.
959.
961.
962.
964.
966.
967.
968.
969.
970.
971.
972.
973.
973.
974.
976.
977.
979.
981.
983.
985.
987.
988.
990.
992.
993.
995.
997.
588
190
900
490
270
900
500
050
400
640
820
770
72-0
600
614
614
970
400
950
560
200
030
000
040
640
220
040
860
840
425
PTTOT
RDG
(INH20)
0.170
0.170
0.170
0.200
0.170
0.170
0.150
0.150
0.100
0.080
0.050
0.050
0.050
0.050
0.120
0.120
0.140
0.170
0.170
0.210
0.240
0.280
0.150
0.150
0.200
0.280
0.200
0.100
ORIFICE
RDG
CINH20)
0.640
0.640
0.640
0.80Q
0.640
0.640
0.600
0.600
0.400
0.320
0.200
0.200
0.200
0.200
0.480
0.480
0.560
0.640
0.640
0.820
0.980
1.100
0.600
0.600
0.800
1.100
0.800
0.400
METERTEMP NOZ
(DEG.F) DIA
IN OUT (IN)
81.
83.
86..
88.
90.
91.
94.
95.
96.
97.
99.
99.
99.
98.
88.
91.
92.
94.
95.
96.
97..
98..
99.
98.
98.
98.
99.
98.
81.
81.
81.
82.
82.
83.
84.
84.
84.
85..
85.
86.
87.
86.
86.
86.
86.
87.
87.
87.
87.
88.
88.
88.
88.
88.
88.
87.
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0-.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
STACK
TEMP
(OF)
150.
150.
150.
150.
150.
150.
150.
150.
ISO.
150.
150.
150.
150.
150.
150.
150.
150.
150.
150.
150.
150.
150.
150*
ISO.
150.
150.
150.
150.
STACK
VEL
CFPS)
32.749
32.749
32.749
35.522
32.749
32.749
30.763
30.763
25.1 18
22.466
17.761
17.761
17.761
17.761
27.515
27.515
29.719
32.749
32.749
36.399
38.912
42.030
30.763
30.763
35.522
42.030
35.522
25.118
%I
*•
101.6
108.3
100.4
103.5
102.6
100.5
103.4
90.0
101.1
107.3
109.1
109.0
100.9
116.5
101.4
106.7
107.0
100.6
102.4
102.8
103.5
99.1
106.0
104.7
104.5
88.4
113.6
128.7
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE1. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: MOLY DRYER TPI
DUCT NUMBER: Tpt
DUCT AREA: 3.34SO.FT.,24.75" ID
DUCT LOCATION: SCRUBBER INLET
FILTER NUMBERS: 02760
TEST NUMBER: Tpi-4
DATE: AUG 24,79
TEST CONO: 2 DRYERS ON
BAP. PRESS-IN HG: 21.48
PITOT TUBE FACTOR: 0.900
TIME TEST STARTED: 805
SAMPLE ELAP
POINT
START
B-.l
2
3
4
5
6
7
8
9
10
1 1
12
13
14
START
A-l
2
1
4
5
6
7
8
9
0
1
2
3
4
TIME
(WIN)
0.0
3.0
6.0
9.0
12.0
15.0
18.0
21.0
24.0
27.0
30.0
33.0
36.0
39.0
42.0
42.0
45.0
48.0
51.0
54.0
57.0
60.0
63.0
66.0
69..0
72.0
75.0
78.0
81.0
84.0
SAMPLE
VOLUME
(DCF)
14.775
16.290
17.730
19.310
20.880
22.290
23.950
25.390
26.700
27.810
28.900
29.900
30.800
31.680
32.709
32.709
34.420
36.120
37.700
39.300
40.910
42.400
44.100
45.300
46.870
48.170
49.510
50.800
52.120
53.468
PITOT
RDG
f INH20)
0.150
0.170
0.190
0.180
0.170
0.160
0.140
0.140
0.070
0.070
0.050
0.050
0.050
0.050
0.160
0.190
0.190
0.170
0.150
0.140
0.140
0.140
0.130
0.130
0.100
0.100
0.100
0.100
ORIFICE
RDG
(INH20)
0.600
0.640
0.670
0.665
0.640
0.620
0.560
0.560
0.280
0.280
0.200
0.200
0.200
0.200
0.620
0.670
0.670
0.640
0.600
0.560
0.560
0.560
0.510
0.510
0.400
0*400
0.400
0.400
METERTEMP NOZ
(DEG.F)
IN
65..
68.
72.
75.
78.
80.
82.
85.
85.
86.
86.
86.
87.
87.
88.
92.
94.
95.
96.
96.
96.
96.
98.
98.
98.
98.
97.
97.
OUT
63.
64.
64.
65.
66.
67.
68.
69.
69.
71.
71.
73.
74.
74.
79.
80.
81.
82.
83.
84.
84.
85.
85.,
85.
86.
86.,
87.
87.
DIA
(IN)
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
0.259
STACK
TEMP
(OF)
145.
150.
150.
150.
150.
150.
150.
150.
150.
150.
150.
150.
150.
150.
150.
150.
155.
155.
155.
150.
150.
150..
150..
150.
150.
150.
150.
150.
STACK %I
VEL
(FPS)
30
32
34
33
32
31
29
29
20
20
17
17
17
1 7
31
34
34
32
30
29
29
29
28
28
24
24
24
24
.177
.259
.103
.194
.259
.295
.274
.274
.700
.700
.495
.495
.495
.495
.295
.103
.243
.391
.426
.274
.274
..274
.209
.209
.741
.741
.741
.741
98.5
88.0
91.1
92.6
85.3
103.3
95.5
86.6
103.7
101.5
110.2
99.0
96.7
113.0
104.7
95.0
88.5
94.6
101.1
96.4
110. 0
77.6
105.1
87.0
102.2
98.4
100.6
102.8
-------
YORK RESEARCH CORPORATION JOB NUMBER
ONE RESEARCH DRIVE, STAMFORD, CONNECTICUT 06906
CLIENT: EPA TEST NUMBER: 2
PLANT LOCATION? CLIMAX MOLY
UNIT TESTED: PRODUCT DRYER
STACK NUMBER: TPI
STACK
LOCATION: SCRUBBER INLET
r 9517-17
DATE: AUG 23,79
CONDITIONS: NORMAL
AMBIENT TEMP-DEG F: 70
BAR. PRESS - IN HG:21.63
ANDERSEN PARTICLE SIZING
STAGE
1
2
3
: 4*
5
6
7
8
EILTER
STACK
STACK
DIAMETER
(MICRONS)
> 11.44
11.44-7.12
7.12-4.81
4.81-3.27
3.27-2.08
2.08-1.02
1* 02-0. 61
0.61-0.28
< 0.28
WEIGHT
(MILLIGRAMS)
7.81
6.t8
9.10
19.88
82.98
57.24
9. ,60
3~84
9. ,49
TEWP.CDBG.F). . . . 150.,0
PReSSURE(IN.HG) i . 21.39
GAS ANALYSIS (DRY
CO? -
CO .
N2 .
02 .
H20 .
PERCENT)
.... 0.00
.... 0.00
. . . . 79.00
.... 21.00
.... 18.00
% PER CUM% GR/SCFD MG/NCMD
STAGE •
18.75
27.61
60.31r
251 .75
173.66
29.13
11.65
28.79
0.762
0.388
0.011
150.0
1.00
30.00
206.1
0.27323
625.35
-------
YORK RESEARCH CORPORATION JO& NUMBER* 9517-17
ONE RESEARCH DRIVE
CLIENT! EPA
. STAMFORD, CONNECTICUT 06906
TEST NUMBER: 3
PLANT L0CA^i:0!<% CMMAJCI MOLYi ;
UNIT TESTED:; P R 00 U CT. : D 'R^feRr •"• <•'
STACK- NUMBER:; TPfc
STACK
LOCATION: SCRUBBER INLET
-•.-"••.. -.;;:-:' " fr V Dft^TE:i: fcUGv 24:>T'9i • '
: ; : K; CONDITIONS: NORMAL
AMBIENT TEMP-OEG Ft 70
BAR. PRESS - IN
HG:21.63
ANDERSEN 'PARTICLE SIZING
STAGE
1
2
3
*" '
5
6
7
8
FILTER
STACK
STACK
GAS AN
I
DIAMETER
(MICRONS)
> 11.75
11.75-7.32
7.32-4,95
4.95-3.36
3.36-2.14
2.14-1.05
1.05-0 .,63
0.63-0 .,29-
< 0*29
TEMP.(DEG.F)
PRESSUREJULN.,
ALYSIS CORY
C02 .
CO .
N2 .
02 .,
H20 .
WEIGHT
(MILLIGRAMS)
25.34
2.51
10.12
13.30
94.94
0.00
55,18
4. ,20
11.84
.... 150.0
HG) . .. 2L.39
PERCENT)
.... 0.00
.... 0.00
. ... 79.10
. ., « . 10.50
. . . . 28.00
% PER CUM% GR/SCFD
STAGE
-------
TP-2 Scrubber Outlet
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: MOLY DRYER TP2
JOB NUMBER: 9517-17
PARTICULATE SUMMARY IN ENGLISH UNITS
DESCRIPTION
UNITS
TP2-2
TP2-3
TP2-4
AVERAGE
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE
STACK PRESSURE, ABS.
STACK AREA
NET TIME OF ftUfJ
PERCENT ISOKINETTC
GAS DATA
AVG STACK GAS VELOCITY
AVG STACK TEMPERATURE DEG.F
ACTUAL STACK FLOWRATE
STK FLOWRATE,DRY,STD
MOLECULAR WT-DRY STK GAS
MOLECULAR WT-STK GAS
MOLE FRACTION DRY GAS
GAS ANALYSIS (DRY P
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION DATA
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD COND
VOL DRY GAS-METER COND
VOL DRY GAS-STD COND
AVG GAS METER TEMP
AVG ORTF PRES DROP
PARTICULATE WEIGHT DATA
MET WEIGHT PARTIAL
NET WEIGHT TOTAL
PARTICIPATE EMISSIONS
PARTIAL
GRAINS PER SCFD
GRAINS PER SCFD P12%C02
GRAINS PER ACF
POUNDS PER HOUR
POUNDS PER PROCESS UNIT
TOTAL
GRAINS PER SCFD
GRAINS PER SCFO 312%C02
GRAINS PER ACF
POUNDS PER HOUR
POUNDS PER PROCESS UNIT
AUG
IN.HG
IN.HG
SO. FT
MIN
Y FPS
DEG.F
: ACFM
DSCFM
GAS
CENT BASIS)
> A
A
ML
ID SCF
!D DEF
DSCF
DEG.F
IN.H20
i* A
iTA
MG
MG
23,79
21.42
21.42
2.52
96.0
96.1
35.921
109.5
5433.
3056.
28.82
27.14
0.844
0.0
20.5
0.0
79.5
15.6
154.1
7.30
56.08
39.66
78.2
0.920
0^00
32.23
AUG 23,79
21.42
21.42
2.52
96.0
98.6
38.365
103.8
5803.
3171.
28.82
26.79
0.812
0.0
20.5
0.0
79.5
18.8
206.3
9.78
60.42
42.24
84.5
1.028
0.00
16.01
AUG 24,79
21.48
21.48
2.52
96.0
93.5
31.308
92,8
4736.
2988.
28.82
27.92
0.917
0.0
20.5
0.0
79.5
8.3
72.1
3.42
52.05
37.73
66.3
0.754
0.00
18.01
96. 1
35.198
102.0
5324.
3072.
0.0
20.5
0.0
79.5
14.2
0.00
22.08
0.00000
o.ooooo
0.00000
0.00
0.00000
0.01252
0.00000
0.00704
0.33
0.00000
0.00000
0.00000
o.ooooo
0.00
0.00000
0.00584
0.00000
0.00319
0.16
0.00000
0.00000
0.00000
0.00000
0.00
0.00000
0.00735
0.00000
0.00464
0.19
0.00000
0.00000
0.00000
0.00000
0.00
0.00000
0.00857
0.00000
0.00496
0.22
0.00000
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE, STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: MOLY DRYER TP2
JOB NUMBER: 9517-17
PARTICULATE SUMMARY IN METRIC UNITS
DESCRIPTION
UNITS
TP2-2
TP2-3
TP2-4
AVERAGE
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE
STACK PRESSURE, ABS.
STACK AREA
MET TIME OF RUN
PERCENT ISOK1NETIC
GAS DATA
AVG STACK GAS VELOCITY
AVG STACK TEMPERATURE DEG.C
ACTUAL STACK FLOWRA'
STK FLOWRATE,DRY,STD DNM3/M
MOLECULAR WT-DRY STK GAS
MOLECULAR WT-STK GAS
MOLE FRACTION DRY GAS
GAS ANALYSIS (DRY PER
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION DATA
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD COND
VOL DRY GAS-METER COND
VOL DRY GAS-STD COND
AVG GAS METER TEMP
AVG ORIF PRES DROP
PARTTCULATE WEIGHT DATA
NET WEIGHT PARTIAL
MET WEIGHT TOTAL
PARTTCULATE EMISSIONS
PARTIAL
MG/NORMALIZED cu.METERS
*G/NORM. CU.M 012% C02
MG/ACTUAL ClJ. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
TOTAL
MG/NORMALIZED CU.METERS
MG/NORM. CU.M 012% C02
MG/ACTUAL CU. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
AUG
MM.HG
MM.HG
M2
MTN
M/S
DEG.C
AM3/M
NM3/M
AS
ENT BASIS)
ML
NM3
DM3
DNM3
DEG.C
M.H20
i a
A'
MG
MG
23,79
544.07
544.07
0.234
96.0
96.1
10.949
43.1
154.
87.
28.82
27.14
0.844
0.0
20.5
0.0
79.5
15.6
154.1
0.21
1.59
1..12
25.7
23.368
0..00
32.23
AUG 23,79
544.07
544.07
0.234
96.0
98.6
11.694
39.9
164.
90.
2-8.82
26.79
0.812
0.0
20.5
0.0
79.5
18.8
206.3
0.28
1 .7 1
1.20
2 9. ,2
26.099
0..00
16.01
AUG 24,79
545.59
545.59
0.234
96.0
93.5
9.543
33.8
134.
85.
28.82
27.92
0.917
0.0
20.5
0.0
79.5
8.3
72.1
0.10
1.47
1.07
19.0
19.145
0..00
18.01
96.1
10.728
38.9
151.
87.
0.0
20.5
0.0
79.5
14.2
0.-00
22.08
0.00
0.00
0.00
0.00
,00000
28.64
0.00
16.1!
0.15
,00000
0.00
0.00
0.00
0.00
o.ooooo
13.36
0.00
7.30
0.07
0.00000
0.00
0.00
0.00
0.00
0.00000
16.82
0.00
10.62
0.09
0.00000
0.00
0.00
0.00
0.00
o.ooooo
19.61
0.00
11.34
0.10
0.00000
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE1 , STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: MOLY DRYER TP2
DUCT NUMBER: TP2
DUCT AREA: 2.52SO.FT.,21.5" I.D.
DUCT LOCATION: SCRUBBER OUTLET
FILTER NUMBERS: 03020
SAMPLE ELAP SAMPLE
POINT TIME VOLUME
(MIN) (DCF)
TEST NUMBER: TP2-2
DATE: AUG 23,79
TEST COND: 2 DRYERS ON
BAR. PRESS-IN HG: 21.42
PITOT TUBE FACTOR: O.R70
TIME TEST STARTED: 1322
START
B-l
2
3
4
START
A-l
2
3
4
0,
12,
24,
36,
48,
48,
60,
72,
84,
96,
,0
,0
,0
,0
.0
.0
.0
.0
.0
.0
1
1
1
1
t
1
1
1
86
94
02
09
16
16
23
30
36
42
.372
.065
.600
.350
.000
.000
.899
.625
.715
.455
PITOT
RDG
INH20)
0.300
0.360
0.220
0.230
0.300
0.210
0.170
0.150
ORIFICE
ROG
(INH20)
1.150
1.350
0.840
0.870
1.150
0.800
0.640
0.560
METERTEMP NQZ
(DEC
IN
68.
77.
80.
78.
86.
8R.
88.
92.
,F)
OUT
70.
68.
70.
70.
76.
78.
78.
84.
DIA
(IN)
0*255
0.255
0.255
0.255
0.255
0.255
0.255
0.255
STACK
TEMP
(DF)
112.
114.
120.
100.
115.
110.
110.
95.
STACK
VEL
(FPS)
40.407
44.340
34.843
35.007
40.512
33.747
30.364
28.144
%I
--
— •
95.6
96.5
97.6
92.5
96.5
97.4
98.0
96.3
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE1, STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: MQLY DRYER TP2
DUCT NUMBER: TP2
DUCT AREA: 2.52SO.FT.,21.5" I.D.
DUCT LOCATION: SCRUBBER OUTLET
FILTER NUMBERS: 03010
TEST NUMBER: TP2-3
DATE: AUG 23,79
TEST COND: 2 DRYERS ON
BAR. PRESS-IN HG: 21.42
PITOT TUBE FACTOR: 0.870
TIME TEST STARTED: 1545
SAMPLE ELAP SAMPLE PITOT ORIFICE METERTEMP NOZ STACK STACK
POINT TIME VOLUME RDG RDG CDEG.F) DIA TEMP VEL
(MIN) (DCF) (INH20HINH20) IN OUT (IN) (OF) (FPS)
0.320 1.200 75.,
0.250 0.850 86.
0.220 0.840 84.
0.200 0.760 90.
0.340 1.300 88. 84. 0.255 115.
0.380 1.450 92. 84. 0.255 115.
0.240 0.910 94. 84. 0.255 115.
0.240 0.910 92. 84. 0.255 90.
START
A-l
2
3
4
START
B-l
2
3
4
0.0
12.0
24.0
36.0
48.0
48.0
60.0
72.0
84.0
96.0
42.707
50.710
57.700
64.435
71.123
71.125
79.630
88.525
95.860
103.125
%I
75.
78.
80.
82.
0.255
0.255
0.255
0.255
100.
100.
105.
90.
41.561
36.735
34.614
32.562
97.3
95.0
98.0
100.1
43.410 100.0
45.893 98.6
36.472 102.0
35.670 99.0
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE', STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-1?
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: MOLY DRYER TP2
DUCT NUMBER: T?2
DUCT AREA: 2.52SO.FT.,21.5" I.D.
DUCT LOCATION: SCRUBBER OUTLET
FILTER NUMBERS: 02820
TEST NUMBER: TP2-4
DATE: AUG 24,79
TEST COND: 2 DRYERS ON
BAR. PRESS-IN HG: 21.48
PITOT TUBE FACTOR: 0.870
TIME TEST STARTED: 815
SAMPLE ELAP
POINT TIME
(MIN)
START
B-l
2
3
4
START
A- 1
2
3
4
0.0
12.0
24.0
36.0
48.0
48.0
60.0
72.0
84.0
96.0
SAMPLE
VOLUME
(DCF)
18.926
23.255
30.310
37.085
43.484
43.490
51.435
58.620
64.840
70.986
PITOT
RDG
(INH20)
0.070
0.250
0.220
0.190
0.300
0.230
0.170
0.160
ORIFICE
RDG
(INH20)
0.230
0.950
0.840
0.730
.
1.150
0.880
0.640
0.610
METERTEMP NOZ
(DEG.F) DIA
IN OUT (IN)
45.
52.
60.
63.
70.
86.
92.
92.
44.
46.
52.
58.
63.
72.
80.
85.
0.255
0.255
0.255
0.255
0.255
0..255
0.255
0.255
STACK
TEMP
(OF)
105.
105.
100.
75.
92.
90.
90.
85.
STACK %I
VEL
(FPS)
19
36
33
30
39
34
29
28
.097
.091
.706
.616
.078
.154
.363
.357
108.2
92.7
93.3
91.9
91.4
92.1
9! .6
92.5
-------
YORK RESEARCH CORPORATION
JOB NUMBER! 9517-17
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
TEST NUMBER! 1
PC,ANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRODUCT DRYER
STACK NUMBER: TPI
DATEr AUG 23,79
CONDITIONS: NORMAL
AMBIENT TEMP-PEG Ft 75
STACK LOCATION: SCRUBBER OUTLET
BAR, PRESS - IN HG:21.60
ANDERSEN--PARTICLE SIZING
DIAMETER WEIGHT % PER CUM% GR/SCFD MG/NCMD
STAGE (MICRONS) (MILLIGRAMS) STAGE 10.39
10.39-6.47
6.47-4.37
2.35
2.30
2.26
3.03
2.96
2.91
9(^97
94.01
0.001095
0.001072
0.001053
2. St.'. - .., t ..:.,
2.45
2.41
I 4
5
6
7
8
FILTER
4.37-2
2.97-1
1.8 9-0
0.93-0
0*56-0
< 0.35
.97
.89
.93
.56
.35
3
.66
19.67
39
4
3
0
.69
.36
*1»
.00
4.71
25,33
51.10
5.61
__ 4v35
0.00
91
86
61
9
4
0
.10
,39
.07
.97
.35
.00
0
0
0
0
0
0
.001705
.009165
.018493
.002031
.001575
.000000
3
20
42
4
; .3
0
,90
.98
.32
.65
..6:0.. _ _
.00
STACK TEMP.,(DBG.F)^.•'•'.' ^ ^ £05vO
STACK ..PRESSURE (.1N. HG.L...........2 U. 60.
GAS ANALYSIS '(DRY PERCENT)
C02 0.00
C0__«_._,_ . . O.J>0
N2 . ..... 79.10
02 . ... . . 20.90
H20 . . . . . 9.40
SAMPLING RATE(ACFH) . . . 0.900
__ _ .....CSCFMD),. ... . 0.552
(NCMMO). . . 0.016
IMPACTOR TEMP.(DEC.F) . . 105.0
._.PARTLCLE_.DENSITY.(GM./CC.).. 1...0.Q_
TEST TIME (MIN) 60.00
TOTAL WEIGHT (MG) . . . . 77.67
TOTAL GR/SCFD > .. . ._.._...JX.0.3-6_L9_
TOTAL MG/NCMD 82.83
-------
Primary Crusher - Sprays On
-------
TP-1 Transfer Point Exhaust
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER TPI SPRAYS ON
JOB NUMBER: 9517-17
PARTICULATE SUMMARY IN ENGLISH UNITS
DESCRIPTION
UNITS
TPt-1
TP1-2
TPI-3
AVERAGE
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE
STACK PRESSURE, ABS
STACK AREA
NET TIME OF RUN
PERCENT ISOKINETIC
GAS DATA
AVG STACK GAS VELOCITY
AVG STACK TEMPERATURE DEG.F
ACTUAL STACK FLOWRATE
STK FLOWRATE,DRY,STD
MOLECULAR WT-DRY STK GAS
MOLECULAR *T-STK GAS
MOLE FRACTION DRY GAS
GAS ANALYSIS (DRY P
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION DATA
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD COND
VOL DRY GAS-MtTER COND
VOL DRY GAS-STD COND
AVG GAS METER TEMP
AVG ORIF PRES DROP
PARTTCULATE WEIGHT DATA
NET WEIGHT PARTIAL
NET WEIGHT TOTAL
PARTICULATE EMISSIONS
PARTIAL
GRAINS PER SCFD
GRAINS PER SCFD 012%C02
GRAINS PER ACF
POUNDS PER HOUR
POUNDS PER PROCESS UNIT
TOTAL
GRAINS PER SCFD
GRAINS PER SCFD «12%C02
GRAINS PER ACF
POUNDS PER HOUR
POUNDS PER PROCESS UNIT
AUG
IN.HG
IN.HG
SO. FT
MIN
.
ry FPS
^ DEG.F
! ACFM
DSCFM
GAS
*CENT BASIS)
n »
L A
ML
JO SCF
JD DEF
DSCF
DEG.F
IN.H20
t T A
\ 1 A
MG
MG
27,79
21.70
21.44
5.59
120.0
105.2
67.069
63.8
22475.
16054.
28.82
28.66
0.985
0.0
20.5
0.0
79.5
1.5
24.4
1.16
111.59
76.82
101.6
1.762
0.00
502.44
AUG 27,79
21.70
21.44
5.59
120.0
103.5
66.857
65.4
22404.
15869.
- 28.82
28.60
0.980
0.0
20.5
0.0
79.5
2.0
32.1
1.52
108.84
.74.68
103.3
1.678
0.00
1243.90
AUG 27,79
21.70
21.44
5.59
120.0
' 104.4
67.307
63.1
22555.
16064.
28.82
28.62
0.981
0.0
20.5
0.0
79.5
1.9
0.0
0.00
111.49
76.54
103.2
1.760
0.00
821.91
104.4
67.078
64.1
22478.
15996.
0.0
20.5
0.0
79.5
1.8
0.00
856.08
0.00000
0.00000
0.00000
0.00
0.00000
0.10072
0.00000
0.07195
13.86
o.ooooo
0.00000
0.00000
0.00000
0.00
0.00000
0.25651
0.00000
0.18170
34.89
o.ooooo
0.00000
0.00000
0.00000
0.00
0.00000
0.16538
0.00000
O.t 1778
22.77
o.ooooo
0.00000
0.00000
0.00000
0.00
0.00000
0.17420
o.ooooo
0.12381
23.84
0.00000
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER TP1 SPRAYS ON
JOB NUMBER: 9517-17
PARTICULATE SUMMARY IN METRIC UNITS
DESCRIPTION
UNITS
TP1-1
TP1-2
TP1-3
AVERAGE
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE
STACK PRESSURE, ABS.
STACK AREA
NET TIME OF RUN
PERCENT ISOK1NETIC
GAS DATA
AVG STACK GAS VELOCITY
AVG STACK TEMPERATURE DEG.C
ACTUAL STACK FLOWRATE AM3/M
STK FLOWRATE,DRY,STD DNM3/M
MOLECULAR WT-DRY STK GAS
MOLECULAR WT-STK GAS
MOLE FRACTION DRY GAS
GAS ANALYSIS (DRY PER
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION DATA
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD COND
VOL DRY GAS-METER COND
VOL DRY GAS-STD COND
AVG GAS METER TEMP
AVG ORIF PRES DROP
PARTICULATE HEIGHT DATA
NET WEIGHT PARTIAL
NET WEIGHT TOTAL
PARTICULATE EMISSIONS
PARTIAL
MG/NORMALIZED cu.METERS
MG/NORM. CU.M ai2% C02
MG/ACTUAL cu. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
TOTAL
MG/NORMALIZED CU.METERS
MG/NORM. CU.M 012% C02
MG/ACTUAL CU. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
AUG
MM.HG :
MM.HG
M2
MIN
M/S
DEG.C
AM3/M
NM3/M
AS
ENT BASIS)
ML
NM3
DM3
DNM3'
DEG.C
M.H20
A
A
M&
MG'
27,79
551.18
544.64
0.519
120.0
105.2
20.443
17.6
636.
455.
28.82
28.66
0.985
0.0
20.5
0.0
79.5
1.5
24.4
0.03
3.16
2.18
38.6
44.746
0.00
502.44
AUG 27,79
551.18
544.64
0.519
120.0
103.5
20.378
18.6
634,
449.
.- 28.82
28.60
0.980
0.0
20.5
0.0
79.5
2.0
32.1
0.04
3.08
2.11
39.6
42.630
0,00
1243.90
AUG 27,79
551.18
544.64
0.519
120.0
104.4
20.515
17.3
639.
455.
28.82
28.62
0.981
0.0
20.5
0.0
79.5
1.9
0.0
0.00
3.16
2.17
39.5
44.704
0..00
821.91
104.4
20.445
17.8
637.
453.
0.0
20.5
0.0
79.5
1.8
0,00
856.08
0.00
0.00
0.00
0.00
0,00000
230.49
0.00
164.64
6.29
0.00000
0.00
0.00
0.00
0.00
0.00000
587.00
0.00
415.79
15.83
0.00000
0.00
0.00
0.00
0.00
0.00000
378.44
0.00
269.53
10.33
0.00000
0.00
0.00
0.00
0.00
0.00000
398.65
0.00
283.32
10.81
0.00000
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE'. STAMFORD, CONNECTICUT 06906
JOB DUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER TP1
DUCT NUMBER: TP1
DUCT AREA: 5.59SO.FT.,32" 1.0.
DUCT LOCATION: TP EXHAUST
FILTER NUMBERS: 02520
TEST NUMBER: TPI-I
DATE: AUG 27,79
TEST CONO: SPRAYS ON
BAR. PRESS-IN HG: 21,
70
PITOT TUBE FACTOR: 0.910
TIME TEST STARTED: 913
SAMPLE ELAP
POINT
—
START
A-l
2
3
4
5
6
7
8
9
10
1 1
12
START
8-1
2
3
4
5
6
7
8
9
10
11
12
TIME
CMIN)
0.0
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0
0.0
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0
SAMPLE
VOLUME
C
464
469
474
478
483
488
493
498
502
508
511
516
520
520
524
529
534
539
544
548
553
558
562
567
571
576
DCF)
.569
.110
.090
.470
.360
.210
.050
.330
.960
.010
.990
.740
.631
.631
.790
.640
.250
.000
.090
.890
.570
.390
.810
.420
.990
.156
PITOT
RDG
CINH20)
0.910
0.860
0.950
0.970
0.980
0.990
0.900
0.910
0.770
0.750
0.770
0.760
0.830
0.840
0.990
1.000
0.970
0.980
0.900
0.890
0.840
0.870
0..700
0.670
ORIFICE
RDG
(INH20)
1.800
1.700
2.100
1.950
1.950
1.950
1.900
1.800
1.600
1.600
1.450
1.500
1.650
1.700
1.900
2.000
1.950
1.950
1.800
1.730
1.700
1.700
1.500
1.400
METERTEMP NOZ
(DEC
IN
84.
90.
96.
102.
106.
108.
1 10.
112.
113.
113.
112.
112.
109.
112.
114.
115.
116.
118.
118.
1 18.
118.
118.
116.
116.
.F)
OUT
78.
80.
81.
84.
86.
89.
90.
92.
94.
96.
96.
98.
98.
96.
97.
97.
97.
97.
98.
97.
98.
98.
96.
96.
DIA
(IN)
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
-0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
STACK
TEMP
(DF)
65.
65.
65.
65.
60.
60.
60.
60.
60.
60.
65.
65.
65.
65.
65.
. 65.
65.
65.
65.
65.
65.
65.
65.
65.
STACK
VEL
(FPS)
68.586
66.675
70.077
70.81 1
70.835
71.195
67.882
68.258
62.788
61.968
63.090
62.679
65.501
65.895
71.537
71.897
70.811
71.175
68.208
67.828
65.895
67.061
60.154
58.850
%I
--
•-
104.5
117.0
97.4
106.8
104.3
103.1
1 17.6
102.2
120.7
96.3
114.0
93.8
96.3
111.5
97.4
99.8
108.5
101 .6
103.3
107.0
100.9
103.4
114.6
106.8
-------
ONE:
YORK RESEARCH CORPORATION
RESEARCH DRIVE1, STAMFORD, CONNECTICUT
JOB NUMBER: 9517-17
06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER TP1
DUCT NUMBER: TP1
DUCT AREA: 5.59SO.FT.,32" I.D.
DUCT LOCATION: TP EXHAUST
FILTER NUMBERS: 02510
TEST NUMBER: Tpi-2
DATE: AUG 27,79
TEST COND: SPRAYS ON
BAR. PRESS-IN HG: 21.70
PITOT TUBE FACTOR: 0.910
TIME TEST STARTED: 1253
SAMPLE ELAP SAMPLE
POINT TIME VOLUME
(MIN) (DCF)
START
B-l
2
3
4
5
6
7
8
9
to
11
12
START
A-l
2
3
4
5
6
7
8
9
10
11
12
0..0
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0
0.0
5.0
10.0
1 5 . 0
20.0
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0
582
586
591
596
601
605
610
615
619
624
628
632
636
636
640
645
650
655
660
665
669
674
678
683
687
691
.175
.780
.740
.350
.170
.840
.650
.490
.930
.250
.340
.380
.428
.428
.940
.610
.430
.320
.190
.140
.910
.570
.920
.070
.040
.019
PITOT
RDG
(INH20)
0.940
0.950
0.920
1 .000
0.970
0.980
0.830
0.840
0.680
0.680
0.620
0.640
0.890
0.900
1.000
0.990
1.000
2.000
0.900
0.870
0.690
0.710
0.550
0.560
ORIFICE METERTEMP NOZ
RDG (DEG.F) DTA
(INH20) IN OUT (IN)
1.900
1.900
1.870
2.000
1.950
1.950
1.700
1.650
1.350
1.350
1.250
1.270
1.800
1.800
2.000
1.970
2.000
2.000
1 .800
1.750
1.370
1.400
1.100
1.150
92.
100.
102.
105.
108.
110.
112.
112.
112.
112.
112.
110.
108.
110.
112.
114.
116.
117.
116.
117.
115.
115..
115.
112.
86.
86.
86.
88.
90.
90.
94.
94.
94.
96.
96.
98.
99.
98.
99.
99.
99.
99.
9.9.
102.
103.
103.
104.
103.
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
-0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
STACK
TEMP
(DF)
65.
65.
65.
65.
60.
60.
65.
60.
60.
65.
65.
70.
65.
65.
65.
70.
65.
65.
70.
70.
70.
70.
65.
65.
STACK
VEL
(FPS)
69.775
70.145
69.028
71.967
70.541
70.904
65.565
65.644
59.062
59.346
56.667
57.847
67.894
68.274
71.967
71.946
71.967
101.777
68.598
67.445
60.064
60.929
53.372
53.855
::
103.3
109.8
103.6
103.4
100.8
103.1
112.6
102.2
110.4
104.8
108.4
107.4
101.3
104.2
101.8
104.1
102.5
73.6
106.3
105.2
110.3
103.7
112.0
111.6
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE', STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIF.NT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER TPI
TEST NUMBER: TP1-3
DATE: AUG 27,79
TEST COND: SPRAYS ON
DUCT NUMBER: TPI BAR. PRESS-IN HG: 21.70
DUCT AREA: 5.59SO.FT.,32" I.D. PITOT TUBE FACTOR: 0.910
DUCT LOCATION: TP EXHAUST TIME TEST STARTED: 1621
FILTER NUMBERS: 020600
SAMPLE ELAP SAMPLE PITOT ORTFICE METERTEMP NOZ STACK STACK %I
POINT TIME VOLUME RDG RDG (DEG.F) DIA TEMP VEL
CMIN) (DCF) f TNH20KINH20) IN OUT (IN) (DF) (FPS)
START
A-l
2
3
4
5
6
7
8
9
10
1 1
12
START
B-l
2
3
4
5
6
7
8
9
10
It
12
0.0
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0
0.0
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0
50.0
55»0
60.0
691.366
695.970
700.750
705.540
710.610
715.680
720.800
725.620
730.430
734.700
738.920
743.360
747.880
747.880
752.490
757.190
761.950
766.930
771.880
776.820
781.460
786.170
790.340
794.450
798.640
802.860
0.900
0.870
0.990
1.050
1.050
1.050
0.900
0.920
0.720
0.720
0.800
0.840
0.900
0.920
0.960
1.050
1 .000
1.000
0.880
0.920
0.680
0.660
0.750
0.660
1.800
1.700
1.990
2.100
2.100
2.100
1.800
1.850
1 .450
1.450
1.600
1.650
1.800
1.850
1.900
2.100
2.000
2.000
1.750
1.850
1.350
1.300
1.450
1.300
86.
90.
98.
104.
106.
108.
110.
112.
112.
112.
112.
112.
110.
112.
112.
114.
116.
116.
116.
116.
116.
116.
114.
114.
88.
88.
88.
88.
90.
91.
92.
94.
95.
95.
96.
98.
100.
100.
100.
100.
100.
102.
102.
102.
102.
102.
102.
103.
0.
0.
0.
0.
0.
0.
0.
0.
0.
-0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
o.
0.
0.
0.
197
197
197
197
197
197
197
197
197
197
197
197
197
197
197
197
197
197
197
197
197
197
197
197
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
65.
65.
65.
65.
65.
70.
65.
65.
65.
65.
65.
65.
65.,
65.
67.934
66.792
71.250
73.377
73.377
73.377
67.934
68.685
60.762
60.762
64.356
65.946
6tf .260
69.014
70.499
74.080
71.952
71.952
67.497
69.014
59.334
58.454
62.313
58.454
102.2
109.8
101.4
103.7
103.4
104.1
105.5
103.8
103.9
102.7
102.9
102.1
100.6
101 .3
100.5
100.9
102.0
101.7
101 .7
101.0
103.8
103.9
99.6
106.7
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD^: CONNECTICUT 06906
JOB NUMBER :; 9517-17-
CLIENT: EPA
PLANT LOCATION: CLIMAX MPLY
_UN.1 T._T.EST£.Q.:__PRTMARY CRUSHER
i STACK NUMBER: TP1
j STACK LOCATION: TRANSFER POINT' EXHAUST
TEST NUMBER: 1
DATE: AUG 27,79
_CQNJ1LT.LCLN S_L. JIPJ?JLY__Q M
AMBIENT TEMP-OEG F: 65
BAR. PRESS ~ IN HG:21.60
ANDERSEN PARTICLE SIZING
DIAMETER WEIGHT % PER CUM% GR/SCFD MG/NCMD
STAGE fMTCRONs* f MILLIGRAMS! STA.GE_ 15.29
11 .81
31.40
0.094035 215.22
1 1 7
i * -
i. .
3
4
S! * -
•''. . . 6_. .
7
'i 8
ii
; FILTER
STACK
15.29-9.54
9v54-6.,46^
6.46-4.40
4.40-2.82
2.82-1.41
1 .41-0.87
0.87-0.57
< 0.57
TEMP.(DEG.F
Y STACK PRESSUREdN
3i GAS' ANALYSIS (DRY
'i CO? .
ll
(1
CO
N2 ..
02 .
H20 „
4.21 . 11.19
5.57 14.81
4.12 10.95
4.60 12.23
4-10 11-43
1.42 3.78
0.64 t.70
•>- . . - 65.0 SAMPL
.HG) . . 21.34
PERCENT') -
..... 0.00 PARTI
., _ . . 79.10 TEST
- T . - 20.90 TOTAL
• . . ., 2.00 TOTAL
TOTAL
68.60
57.40
42.60
3H64
7.98
4.20
2,50
ING RATE
CLE DENS
TIME (MI
WEIGHT
GR/SCFD
MG/NCMD
0.033521 76.72
0.044350 101.50
0.032805
0.036626
0.011306
0.005096
0.^007485
15LCr_MX..^_^..
(SCFMD)., .
(NCMMOyj., »'
ITYCGM/CC)
N) . . . .
fM
-------
YORK RESEARCH CORPOR A TJ[ ON ________ JOB NUMBER! 9517-17
ONE RESEARCH DRIVF, STAMFORD, CONNECTICUT 0690*
L 2
PLANT LOCATION: CLIMAX MOLY DATE-:: AUG 27,79
UNIT TESTED: PRIMARY CRUSHER CONDITIONS: SPRAY ON
STACK NUMBER: ..TILt _______________________ ...... ___ „ ._AMRIENT. TEMP-DEG F: .65
STACK LOCATION: TRANSFER POINT EXHAUST BAR. PRESS - IN HG:21.60
ANDERSEN PARTICLE SIZING
DIAMETER" WEIGHT '% PER ~cTfM%"GR/SCFO MG/NCMD
STAGE fMICRONS) fMILLIGRAMS) STAGE 16.32 2.15 69.13 0.022917 52.45
7 1.6._32-10_.J .°._00 _.Q..°.P...._3_0.sJ7__ 0.000000 0.00
1 in.19-6.90 0.00 0.00 30.87 0.000000 0.00
4 6.90-4..71 0.00 0.00 30.87 0.000000 0.00
5 4.7.1-3.02 0., 00 . ... _ 0.00 30..R7. 0 ..000000.. Q..OO..
6 3.02-1.51 0.38 12.22 30.87 0.004050 9.?7
7 1.51-0.93 0.00 0.00 18.65 0.000000 0.00
8 Q.93-Q_..6_2 0...48. 15.43 ._ ..18.65 0.00.5116 11 ._7 1
FILTER < o.62 o.io 3.22 3.22 o.001066 2.44
STACK TEMP.COEG.F)., . . . 65.0 SAMPLING RATE(ACFM) . . . 0.360
STACK PRESSURE(IN.HG) ... 21.34 ... . (SCFMD). . . 0.254
GAS ANALYSIS (DRY PERCENT) (NCMMD). . . 0.007
C02 0.00 IMPACTOR TEMP.(OEG.F) . . 65.0
CO ._.__...._...._ Q.OO PA.R.TICLE_PEIMSITY(GM/CC) . 1.00
N2 . .- . ., .. 79.10 TEST TIME (MTN.) ....... 5.70
02 .. ., .. . . 20.90 TOTAL WEIGHT (MG) .. . . . 3.11
H2Q ..... 2.00 .TOTAL GP^AQFtL.. _..,__. . „... _ . 0 . 03 3 1 5
TOTAL MG/NCMD 75.87
-------
YORK; RESEARCH CORPORATION JOB -NUMBER-'; 9517-1 7
ONE RESEARCH DRIVE.. STAMFORD, CONNECTICUT Q6906 ~"
CLIENT; EPA ; TEST NUMBER :_ J
PLANT LOCATION* CLIMA-X: MQLY . • DATE: AIJG 27,79
UNIT TESTED:: PRIMARY CRUSHER CONDITIONS;; SPRAY: ON
STACK NUMBER :.:1P.11_; *??BT.E;NT TEMP-DEG Fr 65
STACK LOCATION": "TRANSFER POINT EXHAUST aAR." PRESS - IN HG:2i.6o
ANDERSES PARTICLE SIZING
DIAMETER WEIGHT % PFR CUM% GR/sCFD
STAGE (MICRONS) (MILLIGRAMS) STAGE 14.75 34.06 65..99 0.270899 620.01
2 1.4.15-9_.li 3 ,_22, 6_.24 34*0.1 0.02561!'__ 58 .62
3 9.21-6.24 2.91 5.64 27.77 0.023145 52.97
4 6.24-4.25 3.25 6.30 22.13 0.025849 59.16
5 ...... .4.25-2.72 2.J..4 4..15 1.5«!H 0.017021 ..38..96
6 2.72-1.36 3.72 7.21 11.68 0.029587 67.72
7 1.36-0.83 1..12 2.17 4.48 0.008908 20.39
8 0.._83-0.,:5.5 0_^42 Q....81 _.._2.J1 0 ..003341 „ .7.._6.5___
FILTER < 0.55 0.77 1.49 1.49 0.006124 14.02
STACK TEMP.(DEG.F). . . . 65.;0 SAMPLING RATE (ACFM) . . .. 0.440
STACK PRESSUREdN.HG) ... 21.3.4 (SCFMD). . . 0.31.0
GAS ANALYSIS (DRY PERCENT) (NCMMD). . . 0.009
C02 ..... 0.00 TMPACTOR TEMP.(DEG.F) . . 65.0
__.Cp_.. ._.._..._,. 0.00 PARTICLE DENS ITY (GM/CC) . 1.00
N2 . .- .. .. . 79.10 TEST TIMF- (MIN) .... . 6.25
02 .„ . » .. . 20..90 TOTAL WEIGHT CMC) . . . . 51.61
. . . . . 2,*Q£ TOTAJD_.G;R/ISCFD_JU...^_._..,._.__.„.o.4.10.48
TOTAL MG/NCMD 939.48
-------
TP-2 Crusher Pit Exhaust
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER TP2 SPRAYS ON
JOB NUMBER: 9517-17
PARTICULAR SUMMARY IN ENGLISH UNITS
DESCRIPTION
UNITS
TP2-1
TP2-2
TP2-3
AVERAGE
GENERAL DATA
DATE OF RUN AUG
BAROMETRIC PRESSURE IN.HG
STACK PRESSURE. ABS. IN.HG
STACK AREA SO. FT
NET TIME UF RUN MIN
PERCENT ISOKINETIC
GAS DATA
AVG STACK GAS VELOCITY FPS
AVG STACK TEMPERATURE DEG.F
ACTUAL STACK FLQWRATE ACFM
STK FLOWRATE,DRY,STD DSCFM
MOLECULAR WT-DRY STK GAS
MOLECULAR WT-STK GAS
MOLE FRACTION DRY GAS
GAS ANALYSIS (DRY PERCENT BASIS)
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION DATA
TOTAL H20 COLLECTED ML
VOL H20 VAPOR-STD COND SCF
VOL DRY GAS-METER COND OEF
VOL DRY GAS-STD COND DSCF
AVG GAS METER TE"P DEG.F
AVG ORIF PRES DROP TN.H20
PARTICIPATE WEIGHT DATA
NET WEIGHT PARTIAL MG
MET WEIGHT TOTAL MG
27,79
21.70
21.39
6.40
132.0
100.5
86.803
60.0
33322.
23701.
28.82
28.56
0.976
0.0
20.5
0.0
79.5
2.4
23.2
I. 10
65.91
45.29
100.4
0.560
0.00
321.65
AUG 27,79
21.70
21.39
6.40
132.0
99.5
85.893
60.0
32973.
23603.
2-8.82
28.63
0.983
0.0
20.5
0.0
79.5
1.7
16.7
0.79
64.71
44.63
98.2
0.548
o.oo
320.21
AUG 27,79
21.10
20.79
6.40
132.0
100.9
86.838
63.2
33335.
23038.
28.82
28.63
0.982
0.0
20.5
0.0
79,5
1.8
17.1
0.81
66.16
44.18
100.7
0.556
0.00
260.44
100.3
86.51 1
61.1
33210.
23447.
0.0
20.5
0.0
79.5
2.0
0.00
300.77
PARTTCULATE EMISSIONS
PARTIAL
GRAINS PER SCFD
GRAINS PER SCFO (ai2%C02
GRAINS PER ACF
POUNDS PER HOUR
POUNDS PER PROCESS UNIT
TOTAL
GRAINS PER SCFD
GRAINS PCH SCFD (312%C02
GRAINS PER ACF
POUNDS PER HOUR
POUNDS PER PROCESS UNIT
0.00000
0.00000
o.ooooo
0.00
0.00000
0.10938
0.00000
0.07780
22.22
0.00000
0.00000
0.00000
o.ooooo
0.00
o.ooooo
0.11049
o.ooooo
0.07909
22.35
0.00000
0.00000
0.00000
0.00000
0.00
0.00000
0.09078
0.00000
0.06273
17.93
0.00000
o.ooooo
0.00000
0.00000
0.00
0.00000
0.10355
0.00000
0.07321
20.83
0.00000
-------
YORK RESEARCH CORPORATION
RESEARCH DRIVE, STAMFORD, CONNECTICUT 06906
JOB NUMBER: 95i?-i7
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED:. PRIMARY CRUSHER TP2
SPRAYS ON
PARTTCULATE SUMMARY IN METRIC UNITS
DESCRIPTION
UNITS
TP2-1
TP2-2
TP2-3
AVERAGE
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE
STACK PRESSURE, ABS.
STACK AREA
NET TIME OF HUN
PERCENT ISOKINETTC
GAS DATA
AVG STACK GAS VELOCITY
AVG STACK TEMPERATURE DEG..C
ACTUAL STACK FLOWRATE AM3/M
STK FLOWRATE,DRY,STD DNM3/M
MOLECULAR WT-DRY STK GAS
MOLECULAR WT-STK GAS
MOLE FRACTION DRY GAS
GAS ANALYSIS (DRY P
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION DATA
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD COND
VOL DRY GAS-METER COND
VOL DRY GAS-STD CONO
AVG GAS METER TEMP
AVG ORIF PRES DROP
PARTICULATE WEIGHT DATA
NET WEIGHT PARTIAL
NET WEIGHT TOTAL
PARTTCULATE EMISSIONS
PARTIAL
MG/NORMALIZED CU.METERS
MG/NORM. CU.M 012% C02
MG/ACTUAL CU. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
TOTAL
MG/NORMALIZED CU.METERS
MG/NORM. CU.M 012% C02
MG/ACTUAL cu. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
AUG
MM.HG
MM.HG
M2
MIN
Y M/S
DEG..C
AM3/M
DNM3/M
GAS
CENT BASIS)
*
A
ML
D NM3
D OM3
DNM3
DEG.C
MM.H20
T A
1 H
MG
MG
27,79
551.18
543.34
0.594
132.0
100.5
26.457
15.6
944.
671.
28.82
28.56
0.976
0.0
20.5
0.0
79.5
2.4
23.2
0.03
1.87
1.28
38.0
14.212
0..00
321.65
AUG 27,79
551.18
S43..34
0.594
132.0
99.5
26.180
15.6
934.
668.
28.82
28.63
0.983
0.0
20.5
0.0
79.5
1.7
16.7
0.02
1.83
1.26
36.8
13.918
0.00
320.21
AUG 27,79
535.94
528.10
0.594
132.0
100.9
26.468
17.3
944.
652.
28.82
28.63
0.982
0.0
20.5
0.0
79.5
1.8
17.1
0.02
1.87
1.25
38.1
14.114
0..00
260.44
100.3
26.369
16.1
940.
664.
0.0
20.5
0.0
79.5
2.0
0..00
300.77
0
0
0.00
0.00
0.00
0.00
.00000
250.29
0.00
178.02
10.08
.00000
0.00
0.00
0.00
0.00
0,00000
252.84
0.00
180.99
10.14
0.00000
0.00
0.00
0.00
0.00
0.00000
207..73
0.00
143.56
8.13
0.00000
0.00
0.00
0.00
0.00
0.00000
236.95
0.00
167.53
9.45
0.00000
-------
KOMK RESEARCH CORPORATION
ONE RESEARCH DRIVE', STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER TP?
DUCT NUMBER: TP2
DUCT AREA! 6.40SO.FT..34.25" I.D.
DUCT LOCATION: PIT EXHAUST
FILTER NUMBERS: 02620
TEST NUMBER: TP2-1
DATE: AUG 27,79
TEST COND: SPRAYS ON
BAR. PRESS-IN HG: 21.70
PITOT TUBE FACTOR: 0.920
TIME TEST STARTED: 917
SAMPLE ELAP SAMPLE
POINT TIME VOLUME
(MIN) (DCF)
START 0.0
A-l
2
3
4
5
6
7
8
q
10
11
12
13
14
15
16
17
19
19
20
21
22
3.0
6.0
9.0
12.0
15.0
18.0
21 .0
24.0
27.0
30.0
33.0
36.0
39.0
42.0
45.0
48.0
51.0
54.0
57.0
60.0
63.0
66.0
422.698
424.300
426.020
427.740
429.500
431.100
432.850
434.350
435.950
437.680
439.540
441.250
442.810
444.400
446.120
447.890
449.240
450.750
452.550
454.160
456.140
457.100
458.520
PITOT
RDG
(INH20)
2.100
2.200
2.000
2.000
2.000
1.800
1.800
1.800
1.800
2.000
2.100
1 .800
1.600
1.600
1.600
1.600
1.600
1.500
1.400
1.500
1.300
1 .300
ORIFICE METERTEMP NOZ
RDG (OEG.F) DIA
(INH20) IN OUT (IN)
0.800
0.840
0.760
0.760
0.760.
0.680
0.680
0.680
0.680
0.760
0.800
0.680
0.610
0.610
0.610
0.610
0.610
0.570
0.530
0.570
0.490
0.490
92.
98.
100.
102.
103.
104.
104.
104.
104.
105.
105.
106.
106.
106.
106.
106.
106.
106.
106.
106.
106.
106.
88.
88.
89.
90.
90.
90.
91.
92.
92.
92.
93.
93.
94.
94.
95.
95.
95.
95.
95.
96.
96.
96.
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
STACK
TEMP
CDF)
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
STACK %I
VEL
(FPS)
105
107
102
102
102
97
97
97
97
102
105
97
91
91
91
91
91
88
85
88
82
82
.133
.607
.600
.600
.600
..335
.335
.335
.335
.600
.133
.335
.768
.768
.768
.768
.768
.854
.841
.854
.718
.718
90.4
94.4
98.7
100.7
91.5
105.4
90.2
96.2
104.0
106.0
95.0
93.5
101.0
109.2
112.3
85.7
95.8
117.9
109.2
129.6
67.5
99.8
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
LIENT: EPA
PLANT LOCATION: CLIMAX «OLY
UNIT TESTED: PRIMARY CRUSHER TP2
TEST NUMBER: TP2-1
SAMPLE ELAP SAMPLE
POINT TIME VOLUME
(MIN) (OCF)
START 66.0
B-l
2
3
4
5
6
7
9
9
to
11
12
13
14
15
16
17
18
19
20
21
22
69.0
72.0
75.0
78.0
81.0
84.0
87.0
90.0
93.0
96.0
99.0
102.0
105.0
108.0
111 .0
1 14.0
117.0
120.0
123.0
126.0
129.0
132.0
458
459
460
460
461
462
464
465
467
469
470
472
473
475
476
478
480
481
483
484
485
487
488
.520
.260
.040
.970
.840
.980
.220
.730
.350
.040
.500
.400
.810
.860
.930
.450
.000
.250
.030
.410
.700
.240
.612
PITOT
RDG
(INH20)
0.420
0.420
0.420
0.600
0.760
1.100
1.300
1.500
1.700
1.700
1.700
1.600
1.500
1 .500
1.400
1.300
1.300
1.300
1.300
1.200
1.200
1.200
ORIFICE METERTEMP NOZ
RDG (DEG.F) DIA
CINH20) IN OUT (IN)
0.160
0.160
0.160
0.230
0.280
0.420
0.490
0.570.
0.650
0.650
0.650
0.610
0.570
0.570
0.530
0.490
0.490
0.490
0.490
0.460
0.460
0.460
100.
100.
101.
102.
103.
103.
104.
105.
107.
108.
108.
110.
1 10.
110.
110.
109.
109.
109.
109.
109.
109.
109.
96.
96.
97.
97.
98.
97.
98.
98.
97.
98.
98.
98.
99.
99.
99.
100.
100.
100.
100.
100.
100.
100.
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0..130
0.130
0.130
0.130
07130
0.1 30
0.130
0.130
0.130
0.130
0.130
0.130
0.130
STACK
TEMP
CDF)
60..
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
6-0.
60.
60..
60.
60.
60.
60.
STACK
VEL
(FPS)
47.017
47.017
47.017
56.196
63.247
76.090
82.718
88.854
94.592
94.592
94.592
91.768
88.854
88.854
85.841
82.718
82.718
82.718
'82.718
79.473
79.473
79.473
%I
91.9
96.9
115.3
90.2
104.8
94.9
106.2
106.0
103.8
89.5
116.5
88.9
133.4
69.6
102.4
108.3
87.4
124.4
96.4
93.8
112.0
99.8
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE1. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION; CLIMAX MQLY
UNIT TESTED: PRIMARY CRUSHER TP2
DUCT NUMBER: TP2
DUCT AREA: 6.40SO.FT..34.25" T.D.
DUCT LOCATION: PIT EXHAUST
FILTER NUMBERS: 02910
TEST NUMBER: TP2-2
DATE: AUG 27,79
TEST COND: SPRAYS ON
BAP. PRESS-IN HG: 21.70
PITOT TUBE FACTOR: 0.920
TIME TEST STARTED: 1252
SAMPLE ELAP
POINT
—
START
A-t
2
3
4
5
6
7
9
9
to
11
12
13
14
15
16
17
18
19
20
21
22
TIME
(MIN)
0.0
3.0
6.0
9.0
12.0
15.0
18.0
21 .0
24.0
27.0
30.0
33.0
36.0
39.0
42.0
45.0
48.0
51 .0
54.0
57.0
60.0
63.0
66.0
SAMPLE
VOLUME
(DCF)
489.050
490.900
492.800
494.550
496.170
497.800
499.400
501.100
502.550
504.200
505.350
507. 1RO
508.650
510.300
511.750
513.380
514.860
516.300
518.000
519.400
520.830
522.410
523.858
PITOT
RDG
(TNH20)
2.300
2.300
2.000
1.800
1 .700
1.600
1.500
1.700
1 .700
2.000
2.000
1 .700
1 .600
1 .600
1 .600
1.500
1.500
1.500
1.400
1.400
1.300
1.300
ORIFICE
RDG
(INH20)
0.870
0.870
0.760
0.680
0.650-
0.610
0.570
0.650
0.650
0.760
0.760
0.650
0.610
0.610
0.610
0.570
0.570
0.570
0.530
0.530
0.490
0.490
METERTEMP NOZ
(DEC
IN
80.
84.
88.
90.
92.
93.
96.
97.
98.
too.
101.
102.
103.
103.
104.
104.
105.
105.
105.
106.
106.
106.
.F)
OUT
80.
82.
82.
82.
83.
83.
84.
85.
86.
86.
88.
88.
89.
89.
91.
91.
92.
92.
94.
94.
95.
95.
DIA
(IN)
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0^130
0.130
0.130
0.130
0.1 30
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
STACK
TEMP
(DF)
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
STACK %I
VEL
(EPS)
109
109
102
97
94
91
88
94
94
102
102
94
91
91
91
88
88
88
85
85
82
82
.895
.895
.478
.219
.480
.659
.748
.480
.480
.478
.478
.480
.659
.659
.659
.748
.748
.748
.739
.739
.620
.620
101.1
103.3
101.6
99.0
102.2
103.3
112.9
90.3
102.6
65.8
104.5
90.9
105.0
92.3
103.4
97.0
94.2
111.2
94.6
96.6
110.6
101.4
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
LIENT: EPA
PLANT' LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER TP2
JOB NUMBER: 9517-17
TEST NUMBER: TP2-2
SAMPLE ELAP SAMPLE
POINT TIME VOLUME
CM IN) (DCF)
START 66.0
8-1
2
3
4
5
6
7
8
9
10
tl
12
13
14
15
16
17
1*
19
20
21
22
69.0
72.0
75.0
78.0
81.0
84.0
87.0
90.0
93.0
96.0
99.0
102.0
105.0
108.0
111.0
1 14.0
117.0
120.0
123.0
1,26.0
129.0
132.0
524.
525.
525.
526.
527.
529.
530.
531.
533.
534.
536.
538.
539.
541.
542.
544.
545.
547.
548.
550.
551.
552.
554.
100
030
900
950
820
050
210
680
150
730
710
050
720
110
610
080
510
030
650
050
600
750
000
PITOT
RDG
CINH20)
0.400
0.400
0.500
0.600
0.760
1.000
1.300
1 .500
1.700
1 .800
1.800
1.600
1 .500
1.400
1,400
1.300
1.300
1.400
1.300
1.200
1.200
1.200
ORIFICE
RDG
(INH20)
0.150
0.150
0.190
0.230
0.280
0.360
0.490
0.570
0.650'
0.680
0.680
0.610
0.570
0.530
0.530
0.490
0.490
0.530
0.490
0.460
0.460
0.460
METERTEMP NOZ
(DEG.F) DIA
IN OUT (IN)
104.
104.
103.
104.
104.
104.
106.
106.
108,
109.
109.
110.
110.
110.
110.
110.
110.
110.
110.
HO.
110.
110.
96.
96.
96.
97.
98.
98.
98.
98.
98.
99.
99.
100.
100.
100.
100.
too.
100.
100.
100.
100.
100.
100.
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.430
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
STACK
TEMP
(DF)
60.
60.
60.
60,
60,
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60,
STACK
VEL
(FPS)
45.829
45.829
51.239
56.129
63.172
72.463
82.620
88.748
94.480
97.219
97.219
91.659
88.748
85.739
85.739
82.620
82.620
85.739
82.620
79.379
79.379
79.379
%I
117.4
109.8
118.6
89.6
112. 4
92.5
102.6
95.6
96.4
117.2
79.3
104.6
89.9
100.4
98.4
99.3
105.6
108.4
97.2
112.0
83.1
90.4
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE'. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA TEST NUMBER: TP2-3
PLANT LOCATION: CLIMAX MOLY DATE: AUG 27,79
UNIT TESTED: PRIMARY CRUSHER TP2 TEST COND: SPRAYS ON
DUCT NUMBER: TP2 BAR. PRESS-IN HG: 21
DUCT AREA: 6.40SQ.FT..34.25" I.D. PITOT TUBE FACTOR: 0
DUCT LOCATION: PIT EXHAUST TIME TEST STARTED: 1
FILTER NUMBERS: 02980
SAMPLE ELAP SAMPLE PITOT ORIFICE METERTEMP NOZ STACK STACK
POINT TIME VOLUME RDG RDG (DEG.F) DIA TE^P VEL
(MIN) (DCF) f INH20)(INH20) IN OUT (IN) CDF) (FPS)
START 0.0
A-l
2
3
4
5
6
7
8
9
10
11
12
1 3
14
15
16
17
18
19
20
21
22
3.0
6.0
9.0
12.0
15.0
18.0
21.0
24.0
27.0
30.0
33.0
36.0
39.0
42.0
45.0
48.0
51.0
54.0
57.0
60.0
63.0
66.0
554.
556.
558.
559.
561.
563.
564.
566.
567.
568.
570.
572.
574.
575.
577.
578.
580.
581.
583.
584.
586.
588.
589.
856
600
580
750
560
000
630
170
740
850
500
240
000
580
160
730
260
800
450
050
600
160
712
2.000
2.000
1 .500
1.400
1.500
1 .500
1 .500
1 .600
1.600
1 .800
2.000
2.000
1.600
1.600
1.600
1.500
1.500
1.700
1.600
.1 .500
1.500
1.500
0.760
0.760
0.580
0.540
0.580-
0.580
0.580
0.610
0.610
0.680
0.760
0.760
0.610
0.610
0.610
0.580
0.580
0.650
6.610
0.580
0.580
0.580
82.
86.
92.
92.
95.
97.
98.
100.
100.
102.
104.
105.
106.
106.
106.
106.
106.
108.
108.
108.
108.
108.
85.
86.
85.
85.
86.
87.
88.
88.
88.
89.
90.
90.
92.
93.
93.
94.
94.
95.
95.
96.
96.
97.
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.1.30
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
60.
60.
60.
65.
65.
62.
60.
60.
65.
62.
62.
65.
65.
60.
60.
70.
60.
60.
60.
60.
60.
60.
103.958
103.958
90.030
87.394
90.462
90.203
90.030
92.982
93.428
98.812
104.157
104.456
93.428
92.982
92.982
90.891
90.030
95.844
92.982
90.030
90.030
90.030
.10
.920
624
• •»-
100.2
113.3
76.9
123.7
94.7
106.6
100.4
98.9
70.3
98.0
97.8
99.1
99.2
98.6
98.0
99.5
99.2
99.6
37.3
163.6
100. 1
99.5
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-1?
LIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER
TEST NUMBER: TP2-3
TP2
SAMPLE ELAP SAMPLE PITOT ORIFICE METERTEMP NOZ
POINT TIME VOLUME RDfi RDG (DEG.F) DIA
(WIN) (DCF) (INH20HINH20) IN OUT (IN)
START
B-t
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
66.0
69.0
72.0
75.0
78.0
81.0
84.0
87.0
90.0
93.0
96.0
99.0
02.0
05.0
08.0
11 .0
14.0
17.0
20.0
23.0
76.0
29.0
32.0
589.860
590.860
591.820
592.870
593.970
595.240
596.560
598.000
599.600
601.340
602.900
604.640
606.240
607.800
609.350
610.840
612,
613
615,
320
800
290
616.750
618.210
619.670
621.167
0.550
0.510
0.630
0.720
0.990
1.100
1.500
1.600
1.700
1.800
1.700
0.160
1.500
1.500
1.400
'1.400
1.400
1.400
1.300
1.300
1.300
1.300
0.220
0.190
0.240
0.270
0.370
0.400
0.570
0.610
0.650
0.660
0.650
0.610
0.570
0.570
0.520
0.520
0.520
0.520
0.500
0.500
0.500
0.500
107.
107.
106.
106.
106.
108.
109.
110.
111.
112.
113.
114.
114.
113.
113.
113.
113.
113.
113.
113.
113.
113.
98.
98.
98.
98*
98.
98.
99.
99.
100.
100.
100.
too.
101.
101 .
101.
102.
102.
102.
102.
102.
102.
102.
0.130
0.130
0.130
0.130
0.130
0.130
0,130
0.130
0.130
0.130
0.130
0.130
0.130
OU30
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
STACK
TEMP
(OF)
60.
60.
65.
65..
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
STACK
VEL
(FPS)
54.516
52.496
58.626
62.674
73.491
77.467
90.462
93.428
96.304
99.096
96.304
29.545
90.462
90.462
87.394
87.394
87.394
87.394
84.215
84.215
84.215
84.215
%I
•»«•
— "
105.7
105.4
104.3
102.2
100.7
99.1
92.5
99.4
104.8
91.2
104.6
313.1
99.6
99.1
98.6
97.8
97.8
98.5
100. I
100.1
100. 1
102.7
-------
YORK RESEARCH CORPORATION
JOB NUMBER? 9517-17
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
TEST NUMBER: i
PLANT LOCATION:; CLIMAX M0DY
UNIT TESTEDr PRIMARY CRUSHER
STACK NUMBER: TP2
DATEr AUG; 27,79*
CONDITIONS:: SPRAY ON
AMBIENT TEMP-PEG Fg 65*
STACK LOCATION: CRUSHER PIT EXHAUST
BAR. PRESS - IN HG:21.70
ANDERSEN -PARTICLE SIZING
STAGE
v
1
2
3
DIAMETER
(MICRONS)
> 13.39
13.39-8.35
8.35-5.66
WEIGHT
(MILLIGRAMS
3.82
1.67
% PER
) STAGE
67 .32
14.14
6.18
CUM%
0.016549
MG/NCMO
PER STAGE
412.55
86.64
37.88
4 5.66-3.85
J5 l..£S??,,Al
1.27
4.00 12.36
. 4.70 8.36
0.010702 24.49
O._012585 2JLJ.O..
6
T
FILTER
STACK;
STACK
2.47-1.23
1.23-0.7>
< 0.49
TEMP.(DE5iF)
PRESSUREUN.
GAS ANALYSIS (DRY
CO? .
CO .
N2 .
02 .
H20 .
0.64
0-1:6
0.08
0.11
V '•> .- .60
HG) . .... 2.2..
PERCENT)
. . . . 0.
. . . . 0.
. . . . 79.
. . . . 20.,
.0 '
01
00
00
10
90
00
2.37 3.66 0.006342
0.59 1.30 0..001586
0.30 0.70 0 -.000793
0.41 0.4-1 0. 00 1090
SAMPLING RATECACFM) . .,
(SCFMD). .
(NCMMD). .
IMPACTOR TEMP. (DEC. F) .
PARTICLE DENSITY(GM/CC)
TEST TIME (MIN) ....
TOTAL WEIGHT (MG) . . .
TOTAL GR/SCFD .....
14.52
3.63
2.49
0.530
O.J89
0.011
60.0
1.00
. 4.00
27.02
. 0.26775
. 612.81
-------
YORK RESEARCH CORPORATION JOB NUMBER: 9517-17
ONE RESEARCH DRIVE
CLIENT: EPA
. STAMFORD, CONNECTICUT 06906
TEST NUMBER: 2
PLANT LOCATION: CLIMAX MQLY
UNIT TESTED: PRIMARY CRUSHER
STACK NUMBER:; TP2
DATE: AUG 27 ,79
CONDITIONS: SPRAY ON
AMBIENT TEMP-DEG F: 65
STACK LOCATION: CRUSHER PIT EXHAUST BAR. PRESS - IN
HG:21.70
ANDERSEN PARTICLE; SIZING: - ;
DIAMETER
STAGE (MICRONS)
1 > 13.26
2 13.26-8.27
3 8.27-5.60
4 5.60-3.81
5 3. 8 1-2. ,44
6 2.44-1.21
••?••:. 1.21-0.74
8 0 .,7 4-0. 48
FILTER < 0.48
STACK TEMP.(OEG.,F)
STACK PRESSUREdN.
GAS ANALYSIS (DRY
C02 .
CO .
N2 .
;•;"• 02 .,
H20 .
WEIGHT
(MILLIGRAMS)
10.06
2.89
5.47
3.40
7.84
1.71
1.67
2.39
0.05
. . . . 60.0
HG) JL_, 21,39
PERCENT)
. . . . 0.00
. . . *_ 0.00
. ... . ... 79.10
i,-.;-: i,..: 20.90
. . . . 2.00
% PER CUM% GR/SCFD
STAGE
-------
YORK RESEARCH CORPORATION
JOB NUMBER r. 9517* 17
OMB RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT! EPA
TEST NUMBER! 3
PLANT LOCATION::; CLIMAX MOLY
UNIT TESTEDr PRIMARY CRUSHER"
STACK NUMBER: TP2
DATE:; AUG 27>,79>
CONDITIONS:? SPRAY ON
.JTE M.P -OEG1. £ :__
STACK LOCATION: CRUSHER PIT EXHAUST
BAR. PRESS - IN HG:21.70
ANDERSEN PARTICLE SIZING
STAGE
1
2
3
4;
5
6
7
8=
FILTER
STACK
STACK
DIAMETER
(MICRONS)
> 11.14
13.14-8.20
8.20-5.55
5.55-3.78 -
3.78-2.42
2.42-1.20
t. 2 0-0. ,73:,
0 ..73-0. ,4fr
< 0.48
TEMP. (DEC. F)
PRESSURECIN.
GAS ANALYSIS (DRY
C02 .
CO .
N2,.
02 .
WEIGHT
(MILLIGRAMS)
8.45
1.91
1.53
1.07
0.83
0.93
' -.:. 0*00
0^00
0.02
. » . . 60.0
HG) ... . 21.39
PERCENT)
. . . . 0.00
. . . . 0.00
. .... . . 79.10
. . '.,• . 20.90
. . . . 2.00
% PER CUM% GR/SCFD MG/NCMD
STAGE 66'i ...: ...;,;.
19.91
22.31
o.;oo
0.00
0.48
0.550
0..393
0.011
60.0
1.00
3.75
14.74
0.15447
TOTAL MG/NCMD 353.54
-------
TP-3 Scrubber Outlet
-------
. ... YORK RESEARCH....CORPORATION.. .. .... . _.
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT. :_EP A __
PLANT LOCATION: CLIMAX, MOLY
UNIT TESTED:, PRI;MAR^ CRUSHER TP3^ SPRAYS ON
JQB. .N.U.M.B..EJR:. 9517-17_
PARTICULATE SUMMARY IN ENGLISH UNITS
DESCRIPTION
UNITS
TP3-1
TP3-3
TP3-2
AVERAGE
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE IN,HG
STACK- PRESSURE. ABS..; IN«.;HG
STACK AREA SOv FT
NET TIME OF RUN MTN
PERCENT ISOKINETIC
GAS DATA
AVG STACK GAS VELOCITY EPS
AVG STACK TEMPERATURE DEG.F
ACTUAL STACK FLOWRATE ACFM
STK 7LOWRATE.DRY.STD DSCFM
MOLECULAR WT-DRY STK GAS
MOLECULAR WT-STK GAS
MOLE FRACTION DRY GAS
AUG 27,79
21.70
21.59
' 33.18
144.0
92.6
73.266
55.0
145871.
105617..
28.82
28.55
0.975
GAS ANALYSIS (DRY PERCENT BASIS)
CARBON DIOXIDE 0.0
OXYGEN 20.5
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION- DKTA1
; TOTAL H20 COLLECTED . l*Lv
' VOL H20 VAPOR-STD COND SCF
VOL DRY GAS-METER COND DEF
VOL DRY GAS-STD COND DSCF
AVG GAS METER TEMP DEG.F
0.0
79.5
2.5
' ••.. • 47vO
2,2*
123.36
88.00
82.5
AUG 27,79 AUG
21.70
215.59
33V18
144.0
94.6
75.506
- 55.7
150331. 1
108102. 1
28.82
28.49
0.970
0.0
20.3
0.0
79.5
3.0
60.2?
2.85
131.83
92.07
94.4
27,79
21 ..70
21.59
33.18
144^0
95.7
74.07V
55.1
47475.
06705.
28.82
28.55
0.975
0.0
20.5
o.o
79.5
2.5
50.2
2.3*
130.52
91.88
89.9
94.3
74.281
55.3
147H92.
106808.
0.0
20.5
0.0
79.5
2.7
AVG ORIF' PRES DROP; /s rN
PARTICULATE WEIGHT DATA
N|ET_ WFJGJLT_PARTJLAL
NET WEIGHT TOTAL
PARTICULATE EMISSIONS
PARTIAL
MG
2:..OT1
_JI. OJL
48.98
2.202
__O..J)JL
19.76
2.130
22.06
30.27
GRAINS
GRAINS
GRAINS
POUNDS
POUNDS
TOTAL
GRAINS'
! GRAINS
GRAINS
POUNDS
POUNDS
PER
PER
PER
PER
PER
PER
PEH
PER
PER
PER
SCFD
SCFD (at2%C02
ACF
HOUR
PROCESS UNIT
SCFD
SCFD; *H2%C02
ACF
HOUR
PROCESS UNIT
0.
0.
0.
0.
0.
0.
0.
0.
ooooo
ooooo
ooooo
0.00
ooooo
00857
ooooo
00621
7.76
OOOOO
0
0
0
0
0
0
0
0
.00000
.00000
.00000
0.00
.00000
.00331
.00000
.00238
3.06
.00000
0.00000
o.ooooo
0.00000
0
0
0
0
0
o.oo
.00000
.00370
.00000
*-Q-0-2£8
3.38
.00000
0.
o.
0.
0.
0.
0.
0.
0.
ooooo
ooooo
ooooo
0.00
ooooo
00519
ooooo
00375
4.73
OOOOO
-------
JOB NUMBER:. 9517-17
ONE RESEARCH DRIVE. STAMFORD
CLIENT: EPA
PLANT LOCATION: CLIMAX HOLY
UNIT TESTED: PRIMARY CRUSHER
PARTICULATE
DESCRIPTION UNITS
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE MM.HG
STACK PRESSURE. ARS. MM.HG
STACK AREA M2
NET TIME OF RUN MIN
PERCENT ISOKINETTC
GAS DATA
AVG STACK GAS VELOCITY M/S
AVG STACKs TEMPERATURE*: DEG-.C:;
ACTUAL STACK FLOWRA^^ AM;3f2$s C02
! MG/ ACTUAL Cuidt METERS;
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
TOTAL
MG/NORMALIZED CU. METERS
MG/NORM.: CU.M
-------
, .YORK ..RESEARCH. .CORPORATION _
ONE RESEARCH DRIVE'. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION; CLIMAX MQLY
UNIT TESTED:; PR;I;M-ftR¥: CRUSHER Tp3 .. -N : . '•'.">
DUCT NUMBER:- TP* •
DUCT AREA: 33 . 1 8SO .FT. , 6 .5 ' I.D.
DUCT LOCATION: SCRUBBER OUTLETS
FILTER NUMBERS: 02970
SAMPLE ELAP
POINT TIME
(MJN)
START 0.0
A-l
2
3
4
5
6
7
8
9
10
1 1
12
13
14
1 5 ...
16
17
18
19
1 20
21
22
23
24
3.0
6 .0'
9.0
12.0
15.0
18.0
21 .0
24.0
30.0
33.0
36.0
> SAMPLE
VOLUME
(DCF)
73.000
75.615
80.820
83.525
86.240
89.060
91 .,990
94.930
97_._as_0_
100.750
103.530
106.115
39.0 107.435
42.0 108.635
45,0 110.300
48.0
51.0
54.0
57JK
60..0
61-0
66.0
69..0
72.0
112.390
114.665
1 17.240
1221750
I 24 .5 10
125.486
128.430
131.071
PI TOT
RDG
(INH20)
• 11
:: V
1
1
1
1
1
1
1
1
1
1
; 0
0
0
0
0
1
-I
1
1
1
.250
.200
.200
.300
.300
.400
.500
.500
*5QJD_
.400
.300
.100
.050
.210
.600
.720
.850
.100
1*0*
.500
.500
,100
ORIFICE
RDG
(INH20)
2.200
2.100
2^100
2.330
2.300
2.450
2.650
2.650
_2..650
2.450
2.300
1.950
0.300
0.370
1 .050
1.250
1.500
1.950
2.100
2.450
2-650
2.650
2.650
METER
(DEC.
IN
55.
64.
70,
74.
75.
78.
80.
84.
. 88..
90.
90.
90-
9o":
_8_0.
82.
84.
86.
'• Q T'*
Q. 4
86.
84.
90.
TEM1
F)
OUT
52.
55*
56.
58.
60,
61.
60.
6.4 ._
66.
70.
70.
70.
70.
.72:^
74.
74.
76.
78 .,-
78,
79.
80.
80.
82.
TEST NUMBER: TP.3-1
DATE:; AUG 27,79
TEST COND: SPRAYS ON
BAR. PRESS-IN HG: 21.70
PITOT TUBE FACTOR: 0.880
TIME TEST STARTED: 91 a
> N0£ STACK
DIA TEMP
(IN)
0.195
0.195
0.195
0.195
0.195
0.195
0-.195
0.195
0,195
0,195
0.195
0. 19S
0.195
0.195
0T195
0.195
0.195
0,195
0.195
0.195
0T195
0.195
0.195
0.195
(DF)
45.
45.
45.
45.
45.
45.
45 .
45.
.45.
45.
45.
52.
52.
52.
..52. ..
52.
52.
52.
52.
52.
STACK
VEL
(FPS)
76.1 20
74.582
74.58^
77.628
77.628
80.558
83.386
83.386
83.386
80.558
77.628
7_L^.9AQ_
15.329
31.415
53..L0.2_
58.170
63.204
JLL^.9_OJL
75.097
81.114
81.961
52. 83.961
60. 84.615
65. 72,807
!I
«•
93.9
95.1
92.9
93.2
93.3
93.0
93.1
93.2
92 T 8
93.1
93.2
94.7
225.7
100. I
94.8
94.9
94.2
90.7
29.9
93.0
97-0
-------
YORK; RESF/ARCI* CORPORATION;
JOB NUMBER t 9517-17
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
LIENT: EPA
TEST NUMBER I TP3-1
PLANT LOCATION: CLIMAX MOLY
UNIT, TESTED: PRIMARY CRUSHER TP3
SAMPLE ELAP
POINT TIME
(MIN)
START 72.0
8-1 75.0
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
18
19
20
21
22
23
24
78.0
81.0
84.0
87.0
90.0
93.0
96.0
99.0
102.0
105.0
108.0
111.0
114.0
117.0
120.0
123.0
126.0
129.0
132.0
1 35.0
138.0
141.0
144.0
SAMPLE
VOLUME
(OCF)
31.000
33.730
36.625
39.490
42.500
45.560
48.615
51.660
54.540
57.280
59.880
62.540
64.950
66.925
69.045
71.460
73.990
76.715
79.460
82.325
85.200
88.275
91.040
93.750
96.288
PITOT
RDG
f INH20)
1.200
1.400
1.400
1.500
1.550
1.500
1.500
1.300
1.200
1 .050
1.200
0.850
0.550
0.700
0.930
1.050
1.200
1.200
1.300
1.300
1.300
1.400
1.150
0.920
ORIFICE METERTEMP NOZ STACK
ROG (DEG.F) DTA TEMP
(INH20) IN OUT (IN) (OF)
2.100
2.450
2.450
2.650
2.700
2.65.0
2.650
2.300
2.100
1.850
2.100
1.500
0.970
1.250
1.650
1.850
2.100
2.100
2^300
2.300
2.300
2.450
2.000
1*650
84.
84.
90.
92.
92.
95.
95.
96.
96.
96.
96.
96.
94.
92.
92.
92.
92.
96.
97«_
98.
100.
100.
100.
80.,
80.
80.
82.
82.
82.
82.
84.
84.
84.
85.
85.
86.
86.
86.
86.
86.
86.
86..
88.
89.
90.
90.,
90.
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0..195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
50.
50^
70.
50.
75.
50.
70.
70.
50.
70.
70.
65.
STACK
VEL
(EPS)
75.682
81.746
81.746
84.615
86.014
84.615
84.615
78.772
75.682
70.794
75.682;
50.742
58.356
65.982
71.H08
74.,951
.T&lojt
79.526
78.011
82.528
74.797
66;.584
11
96.2
94
93
94
94
95
95
96
95
96
: 92
98
100
97
94
95
93
96
.6
.1
.2
.,4:' : •
.1
.2
.2
.5
*0
.3
.4
.4
„*. • -
•*%•<• .
96.5
100.9
89.1
96
100
.2
.2 •
-------
.. JT.ORK_R£JSEAJiCH_CDPP.QRA_TrON .
ONE RESEftKCH DRIVE'. STAMFORD, CONNECTICUT 06906
.NUMBER : _951.7-1.7
. CLIENT_: _EP A
PLANT' LOCATION: CLTMAX
UKIT. TES TED :;• PRJMARTP CRUSHER TP3;
DUCT NUMBER: TPI
_TEST._NU,M8ER:.;r.P3-2
DATE: AUG 27,79
CONDt SPRAYS" ON
DUCT AREA: 33.18SO.FT.,6.5' I.D.
DUCT LOCATION: SCRUBBER OUTLET
FTLTER NUMBERS: 02910
SAMPLE ELAP
POTNT TIME
(WIN)
START 0.0
8-1
2
3
4
5
6
7
8
q
10
11
12
13
14
15
16
17
IJ
19
20
2 15
22
23
24
3.0
6 ..0:
9.0
12.0
15.0
18.0
21.0
24.0
27.0
30.0
33.0
36.0
39.0
42.0
45.0
48.0
51.0
54.0
57. ,0
60v,0
63.0
66.0
69.0
72.0
SAMPLE' PltOT
. VOLUME RD.G._..
(DCF) (TNH20)
96.592
-- 99 .,3:00;
102.200
104.980
107.860
110.740
113.765
116.780
119.800
122.770
125.620
128.450
130.990
133*280
135.050
lr.250
1..450
1.300
1.400
1.400
1 .550
1.500
1.500
_l »_450
1.300
1.300
1.100
O.S50
OV450
137.390 0.950
139.935
142.660
145.520
148-400
is 51 ,280*
154.280
157.285
160.090
162.850
1.050
1.200
1.300
1.300s
£.300
Is. 400
1.400
1 .200
0.950
PITOT TUBE FACTOR: 0.880
TIME TEST STARTED: 1255
ORIFICE METERTEMP NOZ
__RD.G (DEG..F) _DIA
CIMH20) IN OUT (IN)
2.200
2.550
68.
75.
68.
70.,
0.195
0.195
2.300 80. 70. 0.195
2.500
2.500
2,750
2.650
2.650
2.550
2.300
2.300
1.950
I?.15
102.
102.
102.
101.
70.
71.
74.
74.
74.
76. _
76.
80.
80.
80.,
82.
82_«^_
82.
84.
84 .
84.
84*
88.
88.
89.
90.
0.195
0.195
0,195
0-.195
0 . 1 95
0 ..1 93
0.195
0.195
0.195
0.195
0.195
0.1 95
0.195
0. t^S
0.195
0.195
0..195
0.195
0.195
0.195
0.195
STACK
TEMP
CDF)
50.
50.
55^.
55.
55.
55.
55.
55.
. .55.
55.
55.
55.
55 .
55.
55.
55.
55.
55.
55.
5;5.,
50.
50.
55.
55.
STACK %I
.. VEL -- _.
(FPS)
76
82
78
81
81
85
84
84
82
78
78
72
55
46
67
70
75
78
78
78
.504
. 397
• 45 1
.360
.360
.608
.216
.216
.800
.401
.401
..LI 8
.438
.127
.021
.460
.325
.401
.401
,401
80.964
80
75
_A1
.964
.325
.021
95.1
93.8
95.0
94.5
94.2
93.6
94.4
94.5
94.3
95.4
94.3
91.9
107.9
100.1
91,4
94.6
94.4
95.3
95.4
95.4
94 .9
95.0
96 ..1
106.1
-------
RESEARCH CORPORATION
JOB NUMBER;: 9517-17
ONE RESEAKCH DRIVE. STAMFORD, CONNECTICUT 06906
LTENT: FPA
TEST NUMBER: TP3-2
PLANT LOCATION: CLIMAX MOL*
;UNIT TESTED: PRIMARY CRUSHER TPJ
SAMPLE ELAP SAMPLE
POINT TIME VOLUME
(MIN) (DCF)
START 72.0
A-l 75.0
2
3
4
5
6 •-'
7
8
9
10
11
12
13
14
1.5
16
•11
19
20
21
22
23
24
78.0
81.0
84.0
87.0
90.0
93.0
96.0
99.0
102.0
105vO
lll!o
114.0
117.0
120.0
123.0
126.0
129.0
132.0
135.0
1.38.0
141.0
144.0
62.900
65.770
68.680
71.600
74.550
77.550
80.450
83.685
86.750
89.830
92.820
95.610
98.150
98.150
100.300
102.350
104.585
107.070
109.590
112.440
115.440
118.510
121.530
124.530
127.166
PITOT ORIFICE
RDG ROG
f INH20HINH20)
1.300
1 .350
1.350
1.400
1.500
1.500
1.500
1.500
1.400
1.200
1.000
0.000
0.350
0.680
0.800
1*000
1.000
1.400
1.500
1.400
1.400
1.050
2.JOO
2.300
2.400
2.400
2.500
2.650
2.650..
2.650
2.650
2.500
2.100
1.750
0.000
0.600
1.200
1.400
1.750
1.750
2.300
2.500
2.650
2.500
1 .850*
METERTEMP NOZ
(DEG.F) DIA
IN OUT (IN)
92_*_
97.
97.
97.
98.
98.
98. .
98.
99.
100.
too.
98.
98.
98.
97.
97.
10 If.
101.
102.
102..
97.
98 .,
86.
90.
90.
90.
88.
88.
88.
88.
88.
88.
88.
88.
88.
88.
90.
90.
91.
91.
92.
92.
90.
90.
;9o.
STACK
TEMP
(OF)
STACK
VEL
(FPS)
!f
0.195 55. 78.401 95.6
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
a. 195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
60.
60.
6.O..
55.
55.
5J5_.
60.
60.
5_5_.
55.,
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55^,
78.780
80.281
80._2.8J_
81.360
84.624
84.624
81.360
75v325
68O62
0.000
40.680
56.703
61.503
68 .762 >
68.762
78...4JXL,:_
81.360
84.216
81.360
81.360
70.460
96
95
96
95
89
94
95
95
95
95
0
136
93
93
93
94
91
95
94
96
95
96
.6
.2
.2
U-." •
.7
.9
.3
.2
lo
.3
.3
.9
•4 '• '•'•'•'
.0
.4
.1
Hjr ::.,
. * -••'-•
!
1
-------
_YORK_SES.EA.R.C.H_.CORP.ORATION JOB_
ONE RESEARCH DRIVE1
CLIENT: EPA
, STAMFORD, CONNECT
ICUT
PLANT LOCATION; CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER TP3
DUCT NUMBER: TP3
OUCT AREA: 33. 18SO.FT. ,6.5' I.D
DUCT f.OCATION: SCRUBBER OUTLET
FILTER NUMBERS: 03060
SAMPLE ELAP
POINT TIME
(WIN)
STiRT 0.0
A-l
2
3 ....
4
5
6
7
8
9
10
1 1
12
1 .3
14
15
16
17
18
19
20
21
22
23
24
3.0
6.0
9.0
12.0
15.0
1 8.0
21.0
24.0
27.0
30.0
33.0
36.0
39.0
42.0
45.0
48.0
51 .0
54.0
57.0
60.0
63.0
66.0
69.0
72.0
SAMPLE
VOLUME „
(DCF)
31.409
34.395
37.380
40,430
43.500
46.670
49.935
53.300
56.675
59.900
62.47S
65. IPO
67.770
67.770
69.800
71.920
74.300
76.870
79.700
82.430
85.360
88.430
91.555
94.810
98.010
PI TOT
RJ1G
CIMH20)
1.500
1.500
_A.._5_5J1_
1.600
1.650
1.800
1 .900
1.900
1 .700
I. 000
1 .350
1 .050
0.000
0.350
0.750
0.900
1.100
1.250
1.250
1.400
1 .550
1 .550
1 .700
1 .600
069Q6
TEST N
DATE:
TEST C
8AR. F
PITOT
TIME 1
ORIFICE METERTEMP MOZ
. _RDG (OEG.E) DF.. A
(IMM20) IN OUT (IN)
2.650
2.650
2^750.
2.800
2.900
3,200
3.350
3.350
3.000
1 .750
2.200
1 .850
0.000
0.620
1 .300
1.600
1.950
2.200
2.200
2.450
2.750
3.000
2.. 800
74.
80.
80.
90.
92.
94.
94.
97.
97.
97.
97.
98.
99.
99.
95.
95.
100.
100.
104.
104.
106.
106.
108.
10J.
74.
78.
78. _
78.
78.
78.
78.
78,
80.
80.
81.
82.
82.
84.
84.
86.
86.
90.
90.
92_.
92.
94.
95_._
0.195
0.195
.O.J.9_5.__
0.195
0.195
0.195
0.195
0.195
0.1.95
0. 195
0.195
0.195
0.195
0 . 1 95
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
CL.X95.
LUM.BER:.
AUG 27
!OND: SI
LR.ES.Sr I j
TUBE Ft
'EST STi
STACK
.. TEMP...
(DF)
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
60.
60.
60.
...60.
60.
60.
60.
55.
55.
55.
55.
55.
_ 55.
TP3-3
,79
PRAYS ON
U HG: 21.70
4CTOR: 0.880
4RTED: 1625
STACK %I
(EPS)
84
84
85
87
88
92
94
94
.89
68
79
70
. 0
40
59
65
72
77
76
81
85
85
89
87
.293
.293
.686.
.057
.407
.338
.868
.868
.737
.825
.967
.866
.000
.914
.893
.609
.534
.321
.949
.435
.686
.686
.737
.057
95.6
94.7
95.2
93.5
94.9
93.5
9.3.9
9.3.9
94.8
98.1
88.8
96.6
0.0
130.4
93.4
95.8
93.1
96.3
91 .8
93.1
92.5
94.2
93.4
9 4.. 5
-------
ONE RESEARCH DRIVE.
LIENT: EPA
STAMFORD, CONNECTICUT 06906
TEST NUMBER:
; PLANT LOCATION: CLIMAX MOLY
| UNIT TESTED: PRIMARY CRUSHER T?3
SAMPLE FLAP
POINT TIME
f.MlN)
START 72.0
fl-
2
3
4
5
6
7
8
9
10
1 1
12
1 3
14
15
_16
17
1 8
1 9
20
21
_22
23
; 24
1 75.0
7«.0
81.0
' 84.0
87.0
90.0
93.0
96.0
99.0
102.0
105.0
1. 0 P . 0
SAMPLE
VOLUME
(DCE)
98.010
.100.450
103.160
105. 8PO
108.610
It 1.650
1 15.000
1 17.550
1 20.390
123.250
126.000
128.760
130.945
111.0 132.930
114.0
117.0
120.0
123.0
126.0
129..0 .
132.0
135.0
135.170
137.650
140.235
142.950
145.870
14 8.. 9 00..
151.730
154.770
L3_fi.._0_lJ37_.JLLQ_
141.0
.144.0
160.700
1.63.241
PITOT ORIFICE METFRTEMP MOZ STACK
RDG RDG (DEG.E) DIA TEMP
( TWH20) (INH20) IN OUT flM) (DF)
0.920
1 .200
1 .200
1 .200
1.500
1 .500
1 .200
1 .300
1 .300
1 .200
1 .200
0.670
1.650
2.100
2.100
2.100
2.650
2.650
2.100
2.300
2.300
2.100
2.100
1.150
0.570 1.000
0.750
0.970
1 .050
1.200
1.350
_ 1.3 50
1.350
1 .500
_L.J50_£L_
1.300
0.970
1 .350
1 .700
1.850
2.100
2.350
2.J50
2.350
2.650
2.JS50__
2.300
1.700
97.
97.
98.
100.
104.
104.
top.
t fit? .
109.
1 09.
1. 10.
110.
1 08.
108.
105.
92.
92.
92.
92.
92.
92.
94.
94.
96.
96,
98.
98.
99.
98.
too.
104. 100.
1.04.
100.
100.
100.
100.
100 ...
100.
100.
100.
95.
95..
92.
92.
.__9 0 .._
90.
90.
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0,195
0.195
0.195
0.1 95
0.195
0.195
0. 195
0.195
0.195
.O.L95._.
0.195
0.195
_Q ._1_9_5
0.195
0.195
55.
55.
55.
55,
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
.. 55..
55.
55.
TP3-.3
STACK
VEL
(EPS)
66.014
75.394
75.394
75.394
84.293
84.293
75.394
79.472
78.472
75.394
75.394
56.336
51 .962
59.604
67.785
70.524
75.394
79.967
79.967 ...
79.967
94.293
84.293 _
78.472
67.785
"
95
93
93
93
93
102
86
92
93
93
93
98
97
95
93
91
92
94
94
95
93
...93
95
97
.8
.3
. 5
. 8
.3
.8
.8
.7
.7
.4
.5
.8
. 3
.9
.6
.9
.3
.4
.7
.0
.6
.7 .
. 6
.t
-------
YORK RESEARCH CORPORATION
JOB NUMBER! 9517-17
ONE RESEARCH DRIVE
CLIENT: EPA
PLANT LOCATION: CL
UNIT TESTED: PRIMA
STACK NUMBER: TP3
STACK
. STAMFORD,
IMAX MOLY
RY CRUSHER
CONNECTICUT 06906
TEST
NUMBER: 1
DATE: AUG 27,79
. CONDITIONS: SPRAY ON
AMBIENT TEMP-DEG F: 60
LOCATION; SCRUBBER OUTLET
ANDERSEN PARTICLE
STAGE
1
3
4
5
6
7
8
FILTER
STACK
STACK
DIAMETER
(MICRONS)
> 14.62
14.62-9.12
9. 12-6.18
6.18-4.21
4.21-2.70
2.70-1.35
1.35-0.83
0.83-0.54
< 0.54
TEMP. ( DBG. F)
PRESSUREUN.
GAS ANALYSIS (DRY
C02 .
CO .
N2 .
02 .
H20 .
WEIGHT
(MILLIGRAMS
0.00
0.14
0.06
{: 0.12
0.01
0.03
0.06.
0.03
0.16
. . . . 55
HG) . . 21.
PERCENT)
. . . . 0.
. . . . 0.
. . . . 79.
. . . • . 20.
. . .. . 3.
BAR.
SIZING
PRESS - IN HG:
:21 ,60
% PER CUM% GR/SCFD MG/NCMD
) STAGE
MG/NCMO
N) .....
(MG) . . . .
0.00
0 . 1. 3
0.05
0.11
0.01
0.03
0.05
0.03
0.14
0.440
0.316
0.009
55.0
1.00
.124.0
0.61
.00024
0.55
-------
Primary Crusher - Sprays Off
-------
TP-1 Transfer Point Exhaust
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER TPI SPRAYS OFF
JOB NUMBER: 9517-17
PARTICULATE SUMMARY IN ENGLISH IJMITS
DESCRIPTION
UNITS
TP1-4
TPI.-5
TP1-6
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE IM.HG
STACK PRESSURE. ABS. TN.HC,
STACK AREA SO. FT
MET TIME OF RUN "TN
PERCENT ISOKINETIC
GAS DATA
AVC STACK GAS VELOCITY FPS
AVG STACK TEMPERATURE DEG.F
ACTUAL STACK FLQWRATE ACFM
STK FLOWRATE/ORY.STD OSCFM
MOLECULAR WT-DRY STK GAS
MOLECULAR VJT-STK GAS
MOLE FRACTION DRY GAS
GAS ANALYSIS (DRY PERCENT BAS
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION DATA
TOTAL H20 COLLECTED ML
VOL H20 VAPOR-STD COND SCF
VOL DRY GAS-METER COND DEE
VOL DRY GAS-STD COND DSCE
AVG GAS METER TEMP DEG.F
AVG ORIF PRES DROP I.N.H20
PARTICULATE WEIGHT DATA
NET WEIGHT PARTIAL MG
NET WEIGHT TOTAL MG
PARTTCULATE EMISSIONS
PARTIAL
GRAINS PER SCFD
GRAINS PER SCFO $12%C02
GRAINS PER ACE
POUNDS PER HOUR
POUNDS PER PROCESS UNIT
TOTAL
GRAINS PER SCFD
GRAINS PER SCFO
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 069(16
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION; CLIMAX MOLY
UMTT TESTED: PRIMARY CRUSHER TP1.
SPRAYS OFF
PARTICULATE SUMMARY IN METRIC UNITS
DESCRIPTION UNITS
GENERAL DATA
DATE OE RUN
BAROMETRIC PRESSURE
STACK PRESSURE. ARS
STACK AREA
NET TIME OF RUN
PERCENT ISOKINETIC
GAS DATA
AVG STACK GAS VEI..O
AVG STACK TEMPERATURE
ACTUAL STACK FLO1'
STK FLOWRATE.ORY.STD
MOLECULAR WT-ORY S
MOLECULAR wT-STK G
MOLE FRACTION DRY
GAS ANALYSIS (DRY
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION 0
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD
VOL DRY GAS-METER
VOL DRY GAS-STO COMD
AVG GAS METER TEMP
AVG ORIE PRES DROP
PARTTCULATE HEIGHT
NET WEIGHT PARTIAL
NET WEIGHT TOTAL
PARTICULATE EMISSIONS
PARTIAL
MG/NORMALIZED cu.METERS
MG/NORM. CU.M 012% C02
MG/ACTUAL cu. METERS
KILOGRAMS/HOUR
KTLOGM PER PROCESS UNIT
TOTAL
MG/NORMALIZEO CM.METERS
MG/MORM. CU.M ai?% C02
MG/ACTUAL CU. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
TPl-4
TP1-5
TP1-6
AVERAGE
MM.HG
. MM.HG
M2
MIN
TTY M/S
RE DEG.C
TE AM3/M
D DNM3/M
K GAS
S
AS
ERCENT BAS
ATA
A 1 A
ML
own MM 3
OND DM 3
D DNM3
DEG.C
MM.H20
DATA
MG
MG
AUG 28.79
548.64
542.10
0.519
120.0
10.3.8
20.998
18.2
654.
463.
28. 82
29.64
0.983
IS)
0.0
20.5
0.0
79.5
1.7
27.9
0.04
3.17
2.18
37.0
46.471
0.00
812.49
AUG 28,79
548.64
542.10
0.519
120.0
103.6
20.645
18.3
643.
453.
28.92
28.59
0.979
o.o
20.5
0.0
79.5
2.1
34.4
0.05
3.13
2.13
40.1
45.085
0.00
906.65
AUG 28,79
548.64 .
542.10
0.519
120.0
104.0
19.978
18.3
622.
437.
29.82
28.56
0..976
0.0
20.5
0.0
79.5
2.4
38.3
0.05
3.02
2.07
39.2
41.889
0.00
753.83
103,8
20.540
18.3
639.
451.
0.0
20.5
0.0
79.5
2.1
o.oo
824.32
0.00
0.00
o.oo
0.00
o.ooooo
371.27
o.oo
262.90
10.31
o.ooooo
0.00
0.00
0.00
.0.00
o.ooooo
424.11
o.oo
298.87
1 1.53
0.00000
0.00
0.00
0.00
o.oo
0.00000
364.25
0.00
255.88
9.55
0.00000
0.00
0.00
.0.00
0.00
o.ooooo
386.54
0.00
272.55
10.46
0.00000
-------
YORK RESEARCH CORPORATION
ONE: RESEARCH DRTVF'. STAMFORD, CONNECTICUT 0690A
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER TP1
DUCT NUMBER: TPt
DUCT 4REA: 5.59SQ.FT..32" I.D.
DUCT LOCATION: TP EXHAUST
FILTER NUMBERS: 02540
TEST NUMBER: TP1-4
DATE: AUG 28,79
TEST COMD: SPRAYS OFF
BAR. PRESS-IN HG: 21.60
PTTOT TUBE FACTOR: 0.910
TIME TEST STARTED: 831
SAMPLE
POINT
--
START
B-1
2
3
4
5
6
7
8
9
10
1 1
1 2
START
A-l
2
3
4
5
6
7
8
q
1 0
1 1
12
FLAP
TIME
(WIN)
0.0
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0
0.0
5.0
1 0.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0
SAMPLE
VOLUME
(DCF)
803.149
807 .040
811.620
816.540
821 .580
826.660
831 .780
836.570
841 . 1 60
845.590
849.870
853.840
857.675
857.675
862.330
867.130
872.070
877.1 00
881.970
887. 3Q0
892.180
896.990
901 .580
904.980
909.390
915.088
PITOT
RDG
INH20)
0.
0.
1 .
I.
1.
1.
o.
o.
0.
n .
0.
0.
0.
0.
1 .
1.
1.
1 .
o.
0.
o.
o.
0.
o.
960
940
ooo
100
1 00
1 00
850
8(SO
800
820
600
580
950
990
1 00
000
100
100
Q60
940
750
7.30
880
870
ORIFICE METERTEMP NO
RDG (OEG.F) 01
( TNH20:
1 .930
1 .900
2.050
2.200
2.150
2.200
1.700
1 .750
1.550
1 .500
1 .200
1 .150
1 .900
1.930
2.200
2.000
2.200
2.200
1.850
1.900
1.500
1 .450
1.750
1 .750
1 IN
74.
82.
88.
95.
100.
J03.
104.
105.
106.
106.
107.
108.
108.
109.
112.
1 13.
113.
115.
116.
116.
1 16.
1 15.
115.
115.
OUT
82.
82.
83.
83.
83.
84.
85.
87.
88.
90.
91.
92.
92.
94.
95.
96.
97.
97.
97.
99.
99.
100.
100.
100.
CTN
0.1
Ll
A
)
97
0.197
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0. 1
0.1
0.1
0.1
o.t
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
.0.1.
97
97
97
97
97
97
97
97
97
97
97
Q7
97
97
97
97
97
97
97
97
97
97
STACK
TEMP
(DF)
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
60.
65.
65.
65.
STACK %I
VEL
(EPS)
70.
69.
72.
75.
75.
75.
66.
66.
64.
65.
55.
54.
70.
71 .
75.
72.
75.
75.
70.
69.
62.
61 .
67.
67.
636
897
093
612
612
612
466
856
482
283
343
904
268
732
612
093
612
612
636
897
136
596
629
244
87
103
107
104
104
104
1 11
1.05
105
100
108
106
101
102
99
105
97
108
102
103
11.0
83
98
127
.7
.5
.2
.1
.4
.9
.3
.7
.5
.5
.7
.6
.4
.1
.4
.9
.8
.6
.6
.9
.3
.2
.4
.9
-------
ONE
YORK RESEARCH CORPORATION
RESEARCH DRIVE'. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CL.IFMT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER
DUCT NUMBER: TP1
DUCT AREA: 5.59SQ.FT. . 32"
DUCT LOCATION: TP EXHAUST
FILTER NUMBERS: 02530
SAMPLE ELAP SAMPLE PITOT OR
POINT
«• «•
START
A-t
2
3
4
5
6
7
3
9
10
1 1
12
START
8-1
2
3
4
5
6
7
8
9
10
11
12
TIME VOLUME
fMIN
0.0
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0
0.0
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0
) (DCF)
915.518
919.850
924.370
929.310
934.430
939.370
944.260
948.930
953.690
958.1 10
962.520
966.700
970.845
970.845
974.190
979.610
984.680
989.900
995.050
1000. 190
1004.980
1009.440
1013.660
1017.740
1021.820
1025.960
RDG
CINH20)
0.900
0.900
1 .100
1 .050
1 .000
0.980
0.890
0.900
0.760
0.840
0.690
0.670
0.910
0.980
1.1.00
1 .100
1 .050
1 .1 00
0.850
0.840
0.650
0.670
0.680
0.700
TP1
I.D.
IEICE
RDG
( INH20)
1
1
2
2
2
1
1
1
1
1
1
1
t
1
2
2
2
2
1
I
1
1
1
1
.800
.800
.200
.150
.000
.900
.750
.800
.550
.650
.400
.350
.800
.950
.200
.200
. 100
.200
.700
.700
.300
.350
.350
.400
TEST NUMBER: TPl-5
DATE: AUG 28,79
TEST COMD: SPRAYS OFF
BAR. PRESS-IN HG: 21.60
PITOT TUBE FACTOR: 0.910
TIME TEST STARTED: 1219
METERTEMP NQZ STACK STACK %i
(DEG.F)
IN
88.
94.
100.
107.
1 09.
1 .10.
112.
114.
114.
115.
115.
116.
1 12.
114.
1 16.
118.
1 20.
120.
120.
119.
117.
116.
116.
115.
OUT
88.
88.
88.
88.
89.
90.
92.
93.
93.
95.
96.
96.
97.
97.
99.
100.
101.
102.
102.
102.
102.
102.
101.
102.
DTA
(IN)
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0. 197
0.197
0.197
0.197
0.197
0.197
0.197
0. 197
TEMP
(DEI
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
VEL
(EPS)
68.449
68,449
75.674
73.934
72.152
71.427
68.068
68.449
62.901
66. 128
59.934
59.059
68.829
71.427
75.674
75.674
73.934
75.674
66.521
66.128
58.171
59.059
59.498
60.367
--
--
99.3
103.0
101.5
107.0
105.4
105.2
106.1
105.0
107.2
101.5
106.0
106.5
74.1
115.5
101.7
104.4
105.2
102.5
108.5
101 .7
109.4
104.3
103.6
103.7
-------
ONE
YORK RESEARCH CORPORATION
RESEARCH DRIVE', STAMFORD, CONNECTICUT
JOB NUMBER: 9517-17
06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER TP1
DUCT NUMBER: TP1
DUCT AREA: 5 . 5C'SO . FT . , 32 " T.D.
DUCT LOCATION: TP EXHAUST
FILTER NUMBERS; 02320
SAMPLE FLAP
POINT
--
START
R-l
2
3
4
5
6
7
R
9
10
11
12
START
A-l
2
3
4
5
6
7
8
9
10
1 1
12
TIME
f M I N )
n.o
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0
0.0
5.0
10.0 .
15.0
20.0
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0
SAMPLE
VOLUMF
(DCF)
26.442
30.620
35.110
39.810
44.5RO
49.360
54.210
58.5*0
62.840
66.990
71 . 170
75.230
79.254
79.254
83.740
88.040
92.720
97.480
102.190
106.950
111.510
115.960
1 19.000
124.060
128.430
1 33.095
PITOT
PDG
(INH20)
0.850
0.830
0.940
0.970
0.950
0.970
0.760
0.770
0.740
0.700
0.650
0.62,0
0.850
0.790
0.950
0.960
0.920
0.960
0.850
0.820
0.620
0.660
0.850
0.900
ORIFICE
RDG
(INH20)
1 .700
1.650
1 .900
1 .950
1 .900
1.950
1.500
1.500
1 .480
1 .400
1.300
1.250
1 .700
1 .500
1 .900
1 .900
1.850
1.900
1 .700
1.600
1 .250
1.300
1.700
1 .800
TEST NUMBER: Tpi-6
DATE: ALIG 28,79
TEST COND: SPRAYS OFF
BAP. PRESS-IN HG: 21.60
PITOT TUBE FACTOR: 0.910
TIME TEST STARTED: 1524
METERTEMP MOZ
(DEG
IN
88.
90.
98.
102.
105.
108.
110.
110.
1 10.
110.
110.
110.
108.
110.
1 12.
1 13.
1 14.
1 15.
1 15.
1 16.
116.
1 16.
II4.
114.
.F)
OUT
90.
92.
90.
"0.
90.
90.
94.
94.
94.
94.
96.
96.
98.
100.
100.
100.
1 00.
100.
100.
100.
100.
100.
1.00.
100.
Dl
(IN
0.1
0.1
0.1
0.1
0. 1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
A
)
97
97
97
97
97
97
97
97
97
97
97
97
97
97
97
97
97
97
97
07
97
97
97
97
STACK
STACK
%r
TE*P VEL
(DF)
65.
65.
65.
• 65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
(FPS)
66
65
69
71
70
71
62
63
62
60
58
56
66
64
70
70
69
70
66
65
56
58
66
68
.560
.772
.995
.103
.366
. 103
.938
.350
.104
.402
.205
.846
.560
. 168
.366
.736
.246
.736
.560
.375
.846
.651
.560
.490
98.6
106.9
104.6
104.1
105.2
105.3
105.5
104.1
102.5
106. 1
106.7
108.3
103.3
102.3
101.5
102.6
103.6
102.4
104.2
103.4
81.1
130.9
99.9
103.7
-------
YORK RESEARCH CORPORATION
JOB NUMBER; 9517-17
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
TEST NUMBER: 4
PLANT LOCATION; CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER
STACK NUMBER: TP1
STACK LOCATION: TRANSFER POINT EXHAUST
DATE: AUG 28,79
CONDITIONS: SPRAY OFF
AMBIENT TEMP-OEG F: 65
BAR. PRESS - IN HG:21.60
ANDERSEN PARTICLE SIZING
DIAMETER WEIGHT % PER CUM% GR/SCFO
STAGE (MICRONS) (MILLIGRAMS) STAGE 16.74
16.74-10.4
10.45-7.08
7.08-4.83
4.83-3.10
3.10-1.55
1.55-0.96
0.96-0.64
< 0.64
12.76
1.99
1.29
1.02
1.45
1.77
0 .52
0'.20
0.23
60.10
9.37
6.08
4.80
6.83
8.34
2.45
0.94
1.08
39.90
30.52
24.45
19.64
12.81
4.47
2.03
1.08
0.135505
0.021133
0.013699
0.010832
0.015398
0.018797
0.005522
0.002124
0.002442
310.13
48.37
31.35
24.79
35.24
43.02
12.64
4.86
5.59
STACK TEMP.(DEG.F). . . . 60.0
STACK PRESSURED IN .HG).__...2 1...3.4
GAS ANALYSIS (DRY PERCENT)
CQ2 0.00
CO 0.00
N2 . . . . . 79.10
02 . . . . . 20.90
H20 . . . . . 2.00
SAMPLING RATE(ACFM) ... . . 0.340
(SCFMD ) l._0 . 242
(NCMMD). . . 0.007
IMPACTOR TEMP.(OEG.F) . . 60.0
_P AJLTJ CLE DENSITY ( G M / CCJ _. .1. .00
TEST TIME (MIN) ..... 6.00
TOTAL WEIGHT (MG) ... . . 21.23
TOTAL GR/SCFD . . . . . . 0.22545
TOTAL MG/NCMD 515.99
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
JOB NUMBER! 9517-17
CLIENT: EPA
PLANT LOCATION: CLT«AX MOLY
U N T T . T E S. TED: _P_RI.M_ A RY CRUSH Eg .__
STACK NUMBER: TP1
'. STACK LOCATION: TRANSFER' POINT EXHAUST
TEST NUMBER: 5
DATE: AUG 28,79
_CQ_N.D. IT. T 0 N S.: _. S P R.A Y1..Q fl f
AMBIENT TEMP-DEG F: 65
BAR. PRESS - IN HG:21.60
ANDERSEN P ARTI..C.L.FL SIZI_M_G_
DIAMETER WEIGHT % PER CUM% GR/SCED MG/NCMD
STAGE (M.I.CRO.N.SJ C,M.ILLI.GR AMSJ.. STAGE_ 15.48
2 15.48-9.66
3 9.66-6.55
4 6.55-4.46
34.54
57.85
0.249166 570.27
7.00 11.72 42.15 0.050497 115.57
JL.JJ 1. 22 3_Q.._4_3 0 ,_Q.31092 7_}_.,t_6_
3.73 6.25 23.21 0.026908 61.53
5 4.46-2.86
6 2.86-1.43
7 1.43-0.88
3.82
4_.L5_.
1.63
6.40 16.97
.6 ..95 L0..5JL
2.73 3.62
0.027557
_0.029_9.37_
0.011759
63.07
..._68.52..
26.91
8 0.88-0.57
.FILTER < p_._57
0.5.3
0.00
0.89 0.89 0.00382.3 3.75
_0_._0_Q Q_.J30. 0 .0.000 0_0_ .0.. J}_P_
65.0
STACK TEMP.(PEG.F). . .
STACK PRESSURE(IN.HG) . .21.34
GAS ANALYSIS (DRY PERCENT)
C02 . ..... . . 0.00
CO 0.00
N2 79.10
0? 20.90
H20
2.00
SAMPLING RATE(ACFM) . . .
(SCFMD). . .
(NCMMD). . .
TMPACTQR TEMP.(DEC
PARTICLE DENSITYCGM/CC) .
TEST TIME (MIN)
T 0 T A I,_ W EIG H T (M G.) . _._._..
TOTAL GR/SCFD 0.43074
TOTAL MG/NCMD 985.83
J3..JLO.O_
0.282
0.008
65.0
I.00
7.58
_5_9..JJ_.
-------
: YORK: RESEARCH CORPORATION :
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
-JOB''NUMBER': 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UN IT...TESTED : P.RIRA.R_Y_.CBiJ.SHF,R
STACK NUMBER: ;Tpi .-.•-,. . ,, ,'.-,. ,,
STACK LOCATION:: TRANSFER 'POINT'' EXHAUST
TEST NUMBER: 6
DATE: AUG 28,79
CQN.ni.TIQMS :... S PRAY-OFf
^AMBIENT: TEMP-DEC; Fl 65
: BAR. PRESS - IN HG:2 I.60
PARTICLE
DIAMETER : WEIGHT % PER CUM% GR/SCFO MG/NCMD
STAGE (MLCRON.SJ CM.LLLJLGR AMS ).. STAGE_ 14.93
7.99
19.75
14.93-9.31
6.31-4.30
tO.R2 24.71 81.75-
7_.JS 1.7 ..70 57_._0_4_
4.9R 11.37 39.35
0.052441
0.071015
120.02
162.53
0...0.5 086 6 1_.1_6 ,_4.2
0.032685 74.31
5
6
7
••• B
FILTER
STACK
>> STACK
•'-, GAS AM
u
.1
4.30-2.75
2.75-1.38
1 .38-0.84
0.84-0.55
< 0.55
TEMP.CDEG.F
PRESSURE (IN
ALYSIS (DRY
CO 2 .
CO .
02 .
H20>'.
. 4.81
4.99
1 .90
,/ ; 0.33- •;., •. .
0.22
). . . . 65.0
.HG) . .: 21.34
PERCENT)
. . . . 0.00
.... 0.00
. . . . 79.10
.... 20.90
. •".'- . . 2.00
10.98 27.97 0.031570
11.40 16.99 0.032751
4.34 5.59 0.012470
0.75 .; 1.26; : 0.002166
0.50 0.50 0.001444
SAMPLING RATE(.ACFM) . .
, . :; ..... .,, ^SCF^fO). .
..'• :' ' ;: CNCMMD). .
IMPACTOR TEMP. (DEG.F) .
PARTICLE DENSITY(GM/CC)
TEST TIME (MIN) . . . .
TOTAL WEIGHT (MG> . . .
TOTAL GR/SCFD . . . . .
TOTAL MG/NCMD .... .
72.25
28.54
4.96
1.JQ
0.430
. 0.303
0.009
65.0
1.00
. 7.75
43.79
. 0.28741
. 657. BO
-------
TP-2 Crusher Pit Exhaust
-------
YORK RESEARCH CORPORATION JOB
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION; CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER TP2 SPRAYS OFF
9517-17
PARTICIPATE SUMMARY IN ENGLISH UNITS
DESCRIPTION
UNITS
TP2-4
TP2-5
TP2-6
AVERAGE
GENERAL DATA
DATE OE RUN
BAROMETRIC PRESSURE TM.HG
STACK PRESSURE. ABS. IM.HG
STACK AREA SO. ET
MET TIME OE HUN MI.M
PERCENT ISOXiNETTC
GAS DATA
AVG STACK GAS VELOCITY EPS
AVG STACK TEMPERATURE DEG.E
ACTUAL STACK ELOWRATE ACFM
STK FLOWKATE,DRY.STD DSCFM
MOLECULAR WT-DRY STK GAS
MOLECULAR WT-STK GAS
MOLE FRACTION DRY GAS
GAS ANALYSIS (DRY PERCENT BAS
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION DATA
TOTAL H20 COLLECTED ML
VOL H20 VAPOR-STD COND SCF
VOL D»Y GAS-METER COND DEE
VOL DRY GAS-STD COND DSCE
AVG GAS METEK TE*P DEG.E
AVG HRIF PHES DROP IN.H20
PARTTCULATE WEIGHT DATA
NET WEIGHT PARTIAL MG
NET WEIGHT TOTAL MG
PARTTCULATE EMISSIONS
PARTIAL
GRAINS PER SCED
GRAINS PER SCFD fai2%C02
GRAINS PER ACE
POUNDS PEP HOUR
POUNDS PER PROCESS UNIT
TOTAL
GRAINS PER SCED
GRAINS PER SCED 012%C02
GRAINS PER ACE
POUNDS PER HOUR
POUNDS PER PROCESS UNIT
AUG 28.79
21.60
21.29
6.40
132.0
101 .0
84.066
60.0
32271.
22932.
28.82
28.60
0.980
IS)
0.0
20.5
0.0
79.5
2.0
19.0
0.90
83.55
44.02
93.2
0.521
0.00
201.27
0.00000
0.00000
0.00000
0.00
0.00000
0.07041
0.00000
0.05003
13.84
0.00000
AUG 28,79
21 .60
21.29
6.40
132.0
101 .1
82.268
60.3
31581.
22511 .
28.82
28.64
0.984
0.0
20.5
0.0
79.5
1 .6
15.2
0.72
62.70
43.29
95.3
0.663
o.oo
191 .27
0.00000
o.ooooo
0.00000
o.oo
0.00000
0.06805
0.00000
0.04850
13.13
0.00000
AUG 28,79
21 .60
21.29
6.40
132.0
100.0
85.865
64.8
32962.
23211.
28.82
28.60
0.980
0.0
20.5
0.0
79.5
2.0
18.9
0.90
64.24
44.14
97.7
0.534
o.oo
180.19
0.00000
0.00000
0.00000
0.00
0.00000
0.06287
0.00000
0.04427
12.51
0.00000
100.7
84.066
61.7
32271.
22884.
0.0
20.5
0.0
79.5
1.9
0.00
190.91
0.00000
0.00000
o.ooooo
o.oo
0.00000
0.0671 I
0.00000
0.04760
1 3.16
o.ooooo
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER
TP2 SPRAYS OFF
PARTICIPATE SUMMARY IN METRIC UNITS
UNITS
DESCRIPTION
GENERAL DATA
DATE OE RUN
BAROMETRIC PRESSURE
STACK PRESSURE. ARS
STACK AREA
NET TIME OE SUN
PERCENT ISOKINETTC
GAS DATA
AVG STACK GAS VELO
AVG STACK TEMPERATURE
ACTUAL STACK FLOt
STK FLOWRATE,DRY,STD
MOLECULAR WT-DRY s
MOLECULAR WT-STK G
MOLE FRACTION ORY
GAS .ANALYSIS (DRY
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY vot
SAMPLE COLLECTION T
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD
VOL DRY GAS-METER
VOL DRY GAS-STD CONO
AVG GAS METER TE*P
AVG ORIF PRES DROP
PARTICIPATE WEIGHT
NET WEIGHT PARTIAL
NET WEIGHT TOTAL
PARTICULATE EMISSIONS
PARTIAL
MG/NOR.MALIZED cu.METERS
MG/NORM. CU.M §12% C02
MG/ACTUAL cu. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
TOTAL
MG/MORMALIZED cu.METERS
MG/NORM. CU.M 012% C02
MG/ACTUAL Cu. METERS
KILOGRAMS/HOUR
KTLOGM PER PROCESS UNIT
TP2-4
TP2-5
TP2-6
AVERAGE
AUG
MM.HG
. MM.HG
M2
MIM
ITY M/S
RE DEG.C
TE AM1/M
n DMM3/M
K GAS
S
AS
ERCENT BASIS)
ATA
H 1. A
ML
0 N D N M 3
OND DM3
D DNM3
DEG.C
MM.H20
DATA
MG
MG
28,79
548.64
540.80
0.594
132.0
101 .0
25.623
15.6
914.
649.
28.82
28.60
0.980
0.0
20.5
o.o
79.5
2.0
19.0
0.03
1.80
1.25
34.0
13.225
0.00
201.27
AUG 28,79
548.64
540.80
0.594
132.0
101.1
25.075
15.7
894.
637.
28.82
28.64
0.984
0.0
20.5
0.0
79.5
.1.6
15.2
0.02
1.78
1.23
35.2
16.839
0.00
191.27
AUG 28,79
548.64
540.80
0.594
132.0
100.0
26.172
18.2
933.
657.
28.82
28.60
0.980
0.0
20.5
0.0
79.5
2.0
18.9
0.03
1.82
1.25
36.5
13.566
0.00
180.19
100.7
25.623
16.5
914.
648.
0.0
20.5
0.0
79.5
1.9
o.oo
190.91
0.00
0.00
0.00
0.00
.00000
161.12
0.00
114.49
6.28
.00000
0.00
0.00
o.oo
0.00
0.00000
155.71
o.oo
110.99
5.96
0.00000
0.00
0.00
0.00
0.00
o.ooooo
1 43.86
0.00
101.31
5.67
0.00000
o.oo
0.00
0.00
0.00
0.00000
1 53.57
0.00
108.93
5.97
o.ooooo
-------
YORK RESEARCH COPPORATION
RESEARCH DRIVE1, STAMFORD, CONNECTICUT
JOB NIJ.V8ER! 9517-17
06906
CLIENT: EPA
PLANT LOCATION:
UNIT TESTED: PR
CLIMAX MOLY
IMA.RY CRUSHER TP2
DUCT NUMBER: TP2
DUCT A
PEA:
D'JCT LOCAT
FILTER
SAMPLE
POTMT
--
START
A-1
2
3
4
5
6
7
8
9
10
1 1
12
1 3
14
IS
16
17
13
19
20
21
22
MUM
6
ION:
BERS:
.40SO.FT. ,34
PIT
EXHAUST
.25" I
.0.
TEST
DATE:
TEST
8AR.
PITOT
TIME
NUMBER: TP2-4
AUG 28,79
COND: SPRAYS OFF
PRESS-
TIJRE
IM HG: 21
FACTOR: 0
TEST STARTED:
.60
.920
835
02920
FLAP SAMPLE
TIM
( M I N
0.0
.1.0
6.0
9.0
12.0
15.0
18.0
21 .0
24.0
27.0
30.0
33.0
36.0
3^.0
42.0
45.0
48.0
51. .0
54.0
57.0
60.0
63.0
66.0
E VOL
U^E
) (DCF)
623.
625.
626.
628.
630.
631.
632.
634.
635.
637.
638.
640.
642.
643.
645.
646.
648.
649.
651.
652.
654.
655.
656.
572
330
950
500
200
510
900
280
7QO
200
880
800
350
880
440
800
350
900
540
700
230
500
887
PITOT ORIFICE
RDG
CT.MH2n) (
2.000
1 .800
1 .800
1 .700
J .200
1 .200
1 .200
1 .300
1 .600
1 .800
2.00Q
1 .700
1.600
1 .600
1.500
1 .500
1.500
1 i.500
1 .500
1 .300
1 .200
1.200
PDG
INH20)
0.760
0.680
0.680
0.650
0.460
0.460
0.460
0.490
0.610
0.680
0.760
0.650
0.610
0.610
0.570
0.570
0.570
0.570
0.570
0.490
0.460
0.460
METERTF.MP
(PEG
IN
72.
75.
78.
81.
84.
86.
86.
89.
89.
92.
95.
97.
08.
98.
99.
100.
100.
101.
101 .
101 .
102.
102.
.F)
OUT
68.
70.
70.
71.
71.
72.
72.
74.
74.
77.
79.
80.
81.
82.
84.
85.
85.
87.
88.
88.
89.
89.
MOZ
Dl\
(IN')
0. 130
0.13 0
0.130
0.130
0.1 30
0.130
0.1. ?0
0.130
0.130
0.130
0.130
0.1 30
0.130
0.130
0.1 30
0.130
0.130
O.I 30
0.130
0.130
0.130
0.130
STACK
TEMP
(DF)
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
STACK
VEL
(FPS)
102.769
' 97.495
97.495
94.748
79.605
79.605
79.605
82.855
91 .920
97.495
102.769
94.748
91 .920
91 .920
89.001
89.001
89.001
89.001
89.001
82.855
79.605
79.605
%T
--
--
104.9
101 .4
96.8
108.8
99.5
105.2
104.5
108.6
92.7
102.9
111.1
97.0
98.5
100.3
90.1
102.5
102.5
108.1
76.4
108.3
93.4
102.0
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRTVF. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
LTENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER
TP2
TEST MUM6ER: TP2-4
SAMPLE FLAP SAMPLE
POIMT TIME VOLUME
("I IN) (DCE)
START 66.0
R-1
7
3
4
5
6
7
8
9
10
1 1
1 7.
13
14
1 5
16
17
18
19
20
21
22
69.0
72.0
75.0
79.0
81 .0
84.0
87.0
90.0
93.0
96.0
99.0
102.0
105.0
108.0
111.0
1 14.0
1 17.0
120.0
123.0
1 26.0
129.0
132.0
657
658
658
659
660
661
663
664
666
668
669
671
673
674
676
677
679
680
631
683
684
686
687
.030
.080
.850
.840
.780
.980
.1.90
.600
. 180
.040
.570
.580
.160
.440
.170
.610
.030
.640
.920
.370
.730
.150
.265
PTTOT
RDG
(IMH20)
0.540
0.400
0.520
0.700
0.840
1.100
1.200
1 .500
1 .700
1 .700
1 .700
1 .600
1.600
1 .500
1.300
1 .500
I .300
1.200
1.200
1 .200
1 .200
1 .000
ORIFICE METERTE.wp NOZ
RDG (DEG.F) DIA
(TNH20) IN OUT (IN)
0.200
0.150
0.190
0.270
0.340
0.420
0.460
0.570
0.650
0.650
0.650
0.610
0.610
0.570
0.490
0.570
0.490
0.460
0.460
0.460
0.460
0.360
100.
100.
99.
100.
100.
102.
103.
104.
105.
108.
109.
109.
110.
t 10.
110.
111.
111.
110.
110.
1 10.
110.
110.
90.
90.
91.
92.
92.
9!3.
94.
94.
94.
96.
96.
96.
97.
97.
97.
98.
97.
98.
99.
99.
99.
99.
0.1 30
0.130
0.130
0.1 30
0.130
0.130
0.130
0.130
0.1.30
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
STACK
TEMP
(DF)
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
STACK
VEL
(EPS)
53.400
45.960
52.402
60.799
66.602
76.216
79.605
89.001
94.748
94.748
94.748
91.920
91.920
89.001
82.855
89.001
82.855
79.605
79.605
79.605
79.605
72.669
%I
115.1
98.0
110.6
90.3
105.3
92,6
103.1
103.3
114.1
93.5
122.7
99.4
80.4
112.2
100.3
91.9
112.0
92.7
104.9
98.4
102.8
88.4
-------
ONE
YORK RESEARCH CORPOR *\T ION
RESEARCH DRIVE1. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLAMT LOCATION: CLIMAX MQLY
TEST NUMBER: TP2-5
DATE: AUG 28,79
UNIT TESTED; PRIMARY CRUSHER TP2 TEST COND: SPRAYS OHF
DUCT NUMBER.. TP2 BAR. PRESS-IN HG : 21.60
DUCT ARFA: 6.40SO.FT. ,34.25" I.D. PITOT TUBE FACTOR: 0.920
DUCT LOCATION: PIT EXHAUST TIME TEST STARTED: 1223
FILTER NUMBERS: 02930
SAMPLE FLAP SAMPLE PITOT ORIFICE METERTEM? NOZ STACK STACK %I
POINT TIME VOLUME RDG RDG (DEG.F) DIA TEMP VEL
MIN) (DCF) f[MH20) (INH20) IN OUT (IN) (OF) (EPS)
START 0.0
A-l
2
3
4
5
6
7
8
q
10
It
12
1 3
14
15
16
17
18
19
20
21
22
3.0
6.0
9.0
12.0
15.0
19.0
21.0
24.0
27.0
30.0
33.0
36.0
39.0
42.0
45.0
48.0
51 .0
54.0
57.0
60.0
63.0
66.0
688.
689.
690.
692.
693.
695.
697.
699.
699.
701.
702.
704.
706.
708.
709.
711.
712.
714.
715.
716.
7.17.
718.
719.
135
530
920
280
930
380
030
400
950
550
950
650
600
220
850
530
940
280
360
460
680
830
935
1
1
1
1
1
1
1
1
1
1
1
2
2
1
1
1
0
o
0
0
0
0
.300
.400
.500
.500
.500
.500
.600
.500
.600
.500
.600
.000
.100
.800
.500
. 1 00
.950
.850
.820
.800
.680
.700
0.490
0.490
0.570
0.570
0.570
0.570
0.610
0.570
0.610
0.570
0.610
0.760
8.000
0.680
0.570
0.420
0.370
0.320
0.310
0.300
0.250
0.265
78.
80.
84.
87.
90.
93.
94.
97.
98.
99.
100.
102.
104.
106.
106.
1 06.
106.
106.
104.
104.
104.
103.
80.
80.
80.
80.
80.
81.
82.
84.
84.
85.
86.
88.
88.
89.
90.
90.
91.
91.
94.
94.
94.
95.
0.130
0.130
0.130
0.130
0.130
0.130
0. 130
0.1 30
0.1 30
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.1.30
0.130
0. 130
0.130
60.
60.
60.
60.
60.
60.
60.
60 .
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
82
85
88
88
83
88
91
88
91
88
"1
102
105
97
88
76
70
66
65
64
59
60
.798
.92.3
.939
.939
.939
.939
.856
.939
.856
.939
.856
.698
.234
.428
.939
.163
.780
.951
.759
.952
.883
.757
101.2
97.0
91 .4
1 10.5
96.9
109.8
88.2
102.5
102.4
92.4
108.4
110.9
91.9
97.3
109.7
107.4
109.7
93.5
96.9
108.8
111.2
105.3
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE, STAMFORD. CONNECTICUT 06906
JOB NUMBER: 9517-17
LTENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER
TEST NUMBER: TP2-5
TP2
SAMPLE ELAP SAMPLE
POINT TIME VOLUME
(MIN) (DCF)
START 66
B-l
2
3
4
5
6
7
8
9
10
1 1
12
13
14
15
16
17
18
19
20
21
22
69
72
75
78
81
84
87
90
93
96
99
102
105
108
1 11
114
1 17
1 20
123
1 26
129
1 32
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
720.150
721.090
721.950
722.830
723.730
724.880
726.380
727.850
729.600
731 .050
732.870
734.530
736.140
737.710
739.280
740.910
742.200
743.610
745.220
746.750
748.380
749.500
751.050
PITOT
RDG
(IMH201)
0.600
0.450
0.500
0.700
0.920
1 .200
1 .500
1.500
1 .700
1 .800
1 .700
1.700
1.500
1 .500
1.500
1 .400
1 .400
1 .400
1 .300
1 .300
1 .300
1 .300
ORIEICE METERTEMP NOZ
RDG (DEG.F) DIA
(INH20) IN OUT (IN)
0.230
0.170
0.190
0.265
0.350
0.460
0.570
0.570
0.650
0.690
0.650
0.650
0.570
0.570
0.570
0.530
0.530
0.530
0.490
0.490
0.490
0.490
102.
102.
102.
102.
102.
1.02.
102.
102.
102.
102.
104.
104.
104.
104.
104.
103.
104.
104.
106.
1.06.
106.
106.
93.
93.
93.
93.
94.
94.
94.
94.
94.
94.
94.
94.
94.
94.
93.
92.
92.
92.
94.
94.
94.
94.
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.1 30
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.5 30
0.1 30
0.1.30
0.130
STACK
TE^P
(OF)
60.
65.
60.
60.
65.
65.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
60.
STACK
VEL
(EPS)
56.250
48.947
51.349
60.757
69.987
79.931
88.9.39
88.939
94.683
97.428
94.683
94.683
88.939
88.939
88.939
85.923
85.923
85.92.3
82.798
82.798
82.798
82.798
%I
97.0
102.9
99.5
86.0
96.2
1 10.0
96.0
114.2
88.9
108.5
101.6
98.6
102.3
102.3
106.3
87.2
95.3
108.8
106.9
113.9
78.2
108.3
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE'. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA TEST NUMBER: TP2-6
PLANT LOCATION: CLIMAX MOLY DATE: AIJG 28,79
UNIT TESTED: PRIMARY CRUSHER TP2 TEST COND; SPRAYS OFF
DUCT NUMBER: TP2 BAR. PRESS-IN HG: 21.60
DUCT AREA; 6 . 40SO . FT. , 34 . 25" I.D. PTTOT TUBE FACTOR: 0.920
DUCT LOCATION: PIT EXHAUST TIME TEST STARTED: 1526
FILTER NUMBERS: 02720
SAMPLE ELAP SAMPLE PITOT ORIFICE METERTEMP MOZ STACK STACK %.I
POINT TIME VOLUME RDG RDG (DEG.F) DIA TEMP VEL
(WIN) (DCF) (INH20HINH20) IN OUT (IN) (DF) (FPS)
START 0.0
A-l
2
3
4
5
6
7
R
q
10
11
12
11
1.4
15
16
17
19
19
20
21
22
3.0
6.0
9.0
17.0
15.0
1 9.0
21.0
24.0
27.0
10.0
11.0
36.0
19.0
42.0
46.0
48.0
51 .0
54.0
57.0
60.0
61.0
66.0
751
751
754
756
757
759
760
762
763
765
767
769
770
772
773
775
776
778
779
791
782
784
785
.330
.090
.870
.450
.920
.300
.680
.too
.840
.590
.390
.030
.550
.090
.630
. 1 60
.690
.290
.770
.300
.790
.240
.239
2.200
2.100
1.600
1.400
1.400
1 . .1 0 0
1 .500
1 .700
2.000
2.100
1 .900
.1.600
1 .500
1.500
1 .500
1 .500
1 .600
1.500
1 .500
1 .400
1 .300
1.100
0.820
0.800
0.610
0.510
0.530
0.400
0.570
0.650
0.760
0.800
0.660
0.610
0.570
0.570
0.570
0.570
0.610
0.570
0.570
0.530
0.500
0.500
79.
8.1.
86.
89.
90.
92.
94.
96.
98.
1 00.
102.
102.
102.
103.
1 04.
104.
I 04.
105.
105.
105.
106.
106.
82.
82.
82.
82.
82.
82.
83.
84.
84.
85.
86.
88.
88.
89.
90.
91.
92.
92.
93.
93.
94.
94.
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0. 1 30
0 . 1 30
0. 1 30
0.1.10
0 . 1 .1 0
0.110
67.
65.
65.
65.
65.
60.
60.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
108.505
105.809
92.358
86.393
86.393
76.213
88.998
95.200
103.259
105.809
100.644
92.358
89.425
89.425
89.425
89.425
92.358
89.425
89.425
86.393
83.250
83.250
•
98.9
101.8
103.2
102.3
96.0
107.5
94.5
109.1
101.0
101.1
96.6
97.3
101 .8
101.7
75.6
151.1
101.9
97.1
100.5
101.3
102.1
70.3
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD. CONNECTICUT 06906
JOB NUMBER; 9517-17
LTEMT: EPA
PLANT LOCATION; CLTMAX
UNIT TESTED: PRIMARY CRUSHER
TEST NUMBER: TP2-6
TP2
SAMPLE ELAP SAMPLE
POINT TIME VOLUME
(HIM) (DCF)
START 66.0
B-l
2
3
4
5
6
7
8
9
10
1 1
12
13
14
15
16
17
18
19
20
21
22
69.0
72.0
75.0
78.0
81 .0
84.0
87.0
90.0
93.0
96.0
99.0
102.0
105.0
108.0
111.0
114.0
1 17.0
120.0
123.0
126.0
129.0
1 32.0
785
786
787
787
788
790
791
792
794
796
797
799
801
802
804
805
807
808
810
811
813
81 4
815
.500
.2*0
.130
.990
.980
.100
.500
.980
.460
.090
.740
.400
.000
.620
.200
.680
.350
.640
.100
.570
.000
.390
.827
PITOT
RDG
f INH20)
0.550
0.460
0.400
0.520
0.740
1 .200
1 .400
1 .400
1 .700
1.900
1 .900
1 .600
1 .600
1 .500
1 .400
1.400
1.400
1 .300
1.300
1 .200
1.200
1 .2.00
ORIFICE METERTEMP MOZ
RDG (DEG.E) OTA
(INH20) IN OUT (IN)
0.220
0.170
0.150
0.200
0.280
0.460
0.520
0.520
0.620
0.660
0.660
0.610
0.610
0.580
0.520
0.520
0.520
0.500
0.500
0.460
0.460
0.460
104.
103.
103.
102.
103.
104.
106.
107.
108.
1.09.
110.
110.
111.
HI.
1 10.
1 10.
110.
110.
110.
110.
1 10.
110.
95.
95.
95.
96.
96.
96.
97.
97.
97.
98.
98.
98.
99.
99.
99.
100.
100.
100.
100.
100.
100.
100.
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.130
0.1.30
0.130
0.130
0.1.30
0.130
0.1 30
0.130
0.130
0.130
0.1 30
0.130
0.130
STACK
TEMP
(OF)
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
STACK
VEL
(FPS)
54.149
49.521
46.179
52.652
62.810
79.984
86.393
86.393
95.200
100.644
100.644
92.358
92.358
89.425
H6.393
86.393
86.393
83.250
83.250
79.984
79.984
79.984
%I
82.2
103.0
109.2
110.3
104.5
102.6
100.1
100.1
99.9
95.5
96.0
100.9
101 .9
102.7
99.6
112.3
86.8
1 0 1 . 9
102.6
103.9
100.9
104.4
-------
'YORK RESEARCH CORPORATION
JOR NUMBER; 9517-17
ONE RESEARCH DRIVE, STAMFORD, CONNECTICUT 06906
CLIENT: EPA
TEST NUMBER; 4
PLANT LOCATION: CLIMAX MQLY
UNIT TESTED: PRIMARY CRUSHER
STACK NUMBER: TP2
STACK LOCATION: CRUSHER PIT EXHAUST
DATE: AUG 28,79
CONDITIONS: SPRAY OF?
AMBIENT TEMp-DEG _f_: _65
BAR. PRESS - IN HG:21.60
AMDERSEN PARTICLE SIZING
DIAMETER
STAGE (MICRONS)
WEIGHT
(MILLIGRAMS)
% PER CUM% GR/SCFD MG/NCMD
STAGE 13.14
13.14-8.20
ft. 20-5. 55
12.90
1.R5
2.29
59.34
H.58
10.62
40. $6
32.08
0.144299
0.020856
0.0253.1.6
330.26
47.73
59.09
4 5.55-3.78
.5 JL.JJI TL2_.JL2_
6 2.42-1.20
1.10 5.10 21.47
. 2,. JL2 9...B.3 -L6_.. 3 7_
0.93 4.31 6.54
7 1.20-0.73
fl 0.73-0.47
EILTER < 0.47
0.48
0.00
o.oo
2.23
0.00
0.00
2.23 0
0.00 0
0.00 0
0.012401
.O._0.23900_
0.010494
oT"o054Tr
P_. 0.0000.0.
0.000000
2H.38
.' 5_4_...7.Q_
24.00
1 2~ 3~8
0 . 0.0. -
0.00
STACK TEMP.(OEG.E). . . . 60.0
STACK .PRESSURES rN.HG)._. ... 21 . 3.1.._..
GAS ANALYSIS (DRY PERCENT)
C02 0.00
.CO ,_J._t_,_,__ 0.. 00__.
N2 79.10
02 20.90
H20 . . .___... 2_._QO
SAMPLING RATE(ACFM) . . . 0.550
(SCEMD )........ 0 . 39 L
(MCMMD). . .
IMPACTOR TEMP.(DEG.F) . .
_P. A-PJJ C LE_D E.N.S.I T Y ( G M / CCJ._..
0.011
60.0
._t ,P_0_
3.50
21.57
0..2_4JJ_7__
TOTAL MG/NCMD 556.54
TEST TIME (MIN) .
TOTAL WEIGHT CMC)
TOTAL GR/SCED . .
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE, STAMFORD. CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
i.JNIT. 1.ESTED :._£R_1M.A_B_Y._CRUSHEJ
STACK MtJiMBER: TP2 : :
STACK LOCATION: CRUSHER PIT EXHAUST
TEST NUMBER: 5
DATE: AUG 28,79
C.OND.I-tI..O.NS :..S P.RAY. ..
AMBIENT TEMP-DEG F: 65
BAR.' PRESS - IN HG:21.60
ANDERSEN PARTICLE ST7.TMG
DIAMETER WEIGHT % PER CUM% GR/SCFD MG/NCMD
STAGE (MICRONS) (MILLIGRAMS.J_ STAGE__ 13.14
1.3.14-8
8.20-5
5.55-3
3.78-2
7.42-1
1 .20-0
0.73-0
< 0.47
.20
.55
.78
.42
.20
.73
..47 -x:
1.
1.
, f
1.
1 .
1 .
0.
, 0.
0.
TEMP. (DEC. F) . . .
H4
1 V
03
62
18
01
40
20
16
. 60.0
21
12
17
18
13
11
4
2
•'•
1
.52
.98
.05
.95
.80
.8 1
.68
.3.4 , .
,87
SAMPL
78
.48
65.50
53
34
20
8
4
1
TNG
.45
.50
.70
.89
.21
:'•
.87
RATEU
0.020743
0 . 0 1. 2 5 1 3
0.011612
0.01826.3
0.013303
0.011 386
0.004509
0.002255
0.001 804
\ C F M ) . .
47.
28.
26.
41.
30.
26..
10.
.5.
4.
0.
47
64
58
80
45
06
32
16
13
550 .
' STACK: PRPJSSURECIN.HG) .-. 21.31.
:s; GAS ANALYSIS CDRY ^PERCENT) ; •
' C02 ... . .0.00 IMPACTOR TEMP . (PEG .F) .
CO 0.00 PARTICLE DENSITY(GM/CC)
(SCFMD). . ... 0.391
(NCMMD). . . O.Olt
6J1._Q_
1.00
N2 79.10
02 20.90
H20:
2.:00
TEST TIME («TN) 3.50
JnLtAli^!LlG_HJL_lMjCLI_._. . . 8.55
TOTAL GR/SCFD . ., .... . . . 0,09639
TOTAL MG/NCMD .... . . 220.60
-------
YORK. RESEARCH CORPORATION
JOR DUMBER! 9517-17
OME RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT; EPA
TEST NUMBER; 6
1 PLANT LOCATION: CLIMAX MOLY
'' UNIT TESTED: PRIMARY CRUSHER
STACK _N U.MB E RJ__T_P_2
DATE: AUG 28,79
CONDITIONS: SPRAY OFF
STACK
STAGE
1
2
1
4
5
6
7
8
FILTER
LOCATION: CRUSHER PIT EXHAUST
DIAMETER
(MICRONS)
> 13.26
13.26-8.27
8.27-5.60
5.60-3.81
3.81-2.44
2.44-1.21
.1 .21-0.74
0.74-0.47
< 0.47
ANDERSEN
WEIGHT
(.MILLIGRAMS)
11.05
3.20
0.00
2.22
1 .77
1.72
0.38
0.47
0.18
PARTICl
% PER
STAGE
52.64
. 15...2.5_
o.oo
10.58
8.43
8.19
1 .81
2.24
0.86
BAR. PRESS - IN
,E SIZING
CUM%
-------
TP-3 Scrubber Outlet
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
JOO NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER
TP3 SPRAYS OFF
PARTICIPATE SUMMARY IN ENGLISH UNITS
DESCRIPTION
UNITS
TP3-4
TP3-5
TP3-6
AVERAGE
DATA
DATE OE RUN
BAROMETRIC PRESSURE
STACK PRESSURE. ABS
STACK AREA
MET TIME OE RUN
PERCENT ISOKINETTC
HAS DATA
AVG STACK GAS VELO
AVG STACK TEMPERATURE
ACTUAL STACK FLO'-
STK ELOWRATE,DRY,STD
MOLECULAR *T-DRY S
MOLECULAR WT-STK G
MOLE FRACTION DRY
GAS ANALYSTS (DRY
CARRON DIOXIDE
OXYGEN
CARBON .MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD
VOL DRY GAS-METER
VOL PRY GAS-STO CO
AVG GAS METER TEMP
AVG ORIE PRES DROP
PARTICULARS WEIGHT
NET WEIGHT PARTIAL
NET WEIGHT TOTAL
PARTICIPATE EMISSIONS
PARTIAL
AUG
IN.HG
IN.HG
SO. FT
•MIN
ITY EPS
RE DEG.F
TE ACEM 1
D DSCEM 1
K GAS
S
AS
ERCENT BASIS)
ATA
A 1 M
ML
OND SCE
own DEE
D DSCE
DEG.E
IN.H20
DATA
MG
MG
28,79
21 .60
21 .49
33.81
1.44.0
99.5
74.314
51 .1
50766.
08690.
28.82
28.48
0.968
0.0
20.5
0.0
79.5
3.2
66.1
3.13
135.32
95.52
P6.2
2.346
0.00
10.00
AUG 28,79
21.60
21.49
33.18
144.0
98.9
78.003
54.8
155303.
111974.
28.82
28.55
0.975
0.0
20.5
0.0
79.5
2.5
53.3
2.53
141.93
99.61
89.7
2.524
o.oo
1. 8 . 9 2
AUG 28,79
21.60
21.49
33.18
144.0
99.0
74.4.34
55.0
1 48196.
106798.
28.82
28.55
0.975
0.0
20.5
0.0
79.5
2.5
51.1
2.42
136.74
95.17
94. 1
2.397
0.00
31 .66
99. I
75.584
53.6
151422.
109154.
0.0
20.5
0.0
79.5
2.7
0.00
20. 1 9
GRAINS
GRAINS
GRAINS
POUNDS
POUNDS
TOTAL
GRAINS
GRAINS
GRAINS
POUNDS
POUNDS
PER
PER
PER
PER
PER
PER
PER
PER
PER
PER
SCED
SCFD
ACE
HOUR
01
PROCESS
SCED
SCED
ACE
HOUR
91
PROCESS
2%C02
UNIT
2%C02
UNIT
0.00000
0.00000
o.ooooo
0.00
o.ooooo
0.00161
o.ooooo
0.001 1 6
1 .50
o.ooooo
0.00000
o.ooooo
0.00000
0.00
0.00000
0.00293
0.00000
0.0021 1
2.81
0.00000
0.00000
0.00000
0.00000
0.00
o.ooooo
0.00512
0.00000
0.00369
4.69
0.00000
o.ooooo
o.ooooo
0.00000
0.00
0.00000
0.00322
o.ooooo
0.00232
3.00
0.00000
-------
YORK RESEARCH CORPORATION
RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION; CLIMAX MQLY
UNIT TESTED: PRIMARY CRUSHER TP3 SPRAYS OFF
PARTICIPATE SUMMARY IN METRIC UNITS
DESCRIPTION
UNITS
TP3-4
TP3-5
TP.3-6
AVERAGE
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE
STACK PRESSURE, ABS
STACK AREA
NET TIME OF RUN
PERCENT ISQKINFTIC
GAS DATA
AVG STACK GAS VELO
AVG STACK TEMPERATURE
ACTUAL STACK FLQI
STK FLOWRATE,ORY,STD
MOLECULAR wT-ORY S
MOLECULAR WT-STK G
MOLE FRACTION DRY
GAS ANALYSIS CORY
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD
VOL DRY GAS-METER
VOL DRY GAS-STD COND
AVG GAS METER TEMP
AVG ORTF PRES DROP
PARTICIPATE WEIGHT
NET WEIGHT PARTIAL
NET WEIGHT TOTAL
PARTICIPATE EMISSIONS
PARTIAL
MG/NORMALIZED CU.METERS
MG/NORM. CU.M 012% C02
MG/ACTUAL cu. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
TOTAL
MG/NORMALIZED CU.METERS
MG/MORM. CU.M 912% C02
MG/ACTUAL cu. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
AUG
MM.HG
MM.HG
M2
MTN
ITY M/S
RE DEG.C
TE AM3/M
D D N M 3 / M
K GAS
S
AS
EPCENT BASIS)
A T ft
A A A
ML
0 N D N M 3
OND DM3
D DNM3
DFG.C
MM.H2O
DATA
MG
MG
29,79
548.64
545.84
3.141
144.0
99.5
22.651
10.6
4269.
3078.
28.82
28.48
0.968
0.0
20.5
0.0
79.5
3.2
66.1
0.09
3.83
2.70
30.1
59.595
0.00
10.00
AIJG 28,79
548.64
545.84
3.083
144.0
98.9
23.775
12.7
4398.
3171.
28.82
28.55
0.975
0.0
20.5
0.0
79.5
2.5
53.3
0.07
4.02
2.8?
32.1
64.119
0.00
18.92
AUG 28,79
548.64
545.84
3.083
144.0
99.0
22.687
12.8
4196.
3024.
28.82
28.55
0.975
0.0
20.5
0.0
79.5
2.5
51.1
0.07
3.87
2.69
34.5
60.886
0.00
31 .66
99.1
23.038
12.0
4288.
3091 .
0.0
20.5
0.0
79.5
2.7
0.00
20.19
0.00
0.00
0.00
0.00
00000
3.69
0.00
2.66
0.68
00000
0.00
0.00
0.00
0.00
0.00000
6.69
0.00
4.83
1.27
o.ooooo
0.00
0.00
0.00
0.00
0.00000
It. 72
0.00
8.45
2.13
0.00000
0.00
0.00
0.00
0.00
0.00000
7.37
0.00
5.31
1 .36
0.00000
-------
OWE
YORK RESEARCH CORPORATION
RESEARCH DRIVE*. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX «OLY
uviT TESTED: PRIMARY CRUSHER TP3
DUCT MIl.MfJER: TP3
DUCT AREA: 33.81SO.ET.,6.5' ID
DHCT LOCATION: SCRUR8ER OUTLET
FILTER NUMBERS: 02500
TEST NUMBER: TP3-4
HATE: MJG 28,79
TEST CQVQ: SPRAYS OFF
BAR. PRESS-IN HG: 21 .60
PITOT TUBE FACTOR: 0.890
TIME TEST STARTED: 835
SAMPLE ELAP SAMPLE
POINT TIME VOLUME
fMiN) (DCF)
START 0.0
B-1
2
3
4
5
6
7
9
9
10
1 1
1 2
1.3
1 4
15
16
17
18
19
20
21
22
23
24
3.0
6.0
9.0
12.0
15.0
1.8.0
21 .0
2A.O
27.0
30.0
33.0
36.0
39.0
42.0
45.0
48.0
51 .0
54.0
57.0
60.0
63.0
66.0
69.0
72.0
63
66
69
72
75
78
81
84
87
90
93
95
98
too
102
104
107
110
13
16
19
22
25
127
130
.828
.415
.350
.390
.460
.495
.71 5
.350
.800
.500
.200
.900
.5.35
.435
.505
.950
.670
.390
.240
.100
. 100
.060
.050
.810
.360
PITOT
PDG
f TNH20)
1.100
1.400
1 .500
1.500
1 .500
1 .600
1 .500
1 .300
1 .100
1 .100
1 .100
1.000
0.470
0.620
0.920
1 .100
.1.100
1 .200
1 .200
1 .300
1.300
1 .300
1 .100
0.900
ORIFICE
RDG
(IMH20)
2.100
2.700
2.900
2.900
2.900
.3.200
2.900
2.500
2. 100
2. 100
2.100
1.950
0.900
1.200
1 .750
2.100
2.100
2.300
2.300
2.500
2.500
2.500
2.100
1.750
METERTEMP MOZ
COEG.F) DTA
IN OUT (IN)
60.
60.
72.
77.
80.
85.
87.
90.
90.
90.
90.
92.
90.
90.
90.
92.
94.
94.
96.
96.
98.
98.
98.
96.
60.
60.
60.
62.
64.
65.
67.
68.
70.
70.
70.
74.
76.
76.
76.
90.
80.
82.
82.
82.
84.
84.
84.
85.
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0. 195
0.195
0.1 95
o. 105
0.195
0. 195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
STACK
TEMP
(DF)
55.
55.
55.
55.
55.
55.
50.
50.
45.
45.
45.
45.
45.
45.
45.
45.
45.
50.
45.
45.
45.
50.
50.
50.
STACK
VEL
(EPS)
72.375
81 .650
84.516
94.516
84.5) 6
87.298
84.105
73.297
71 .669
71.669
7 1 .669
6 8 . 3 3 4
46.847
53.806
65.543
71 .669
71 .669
75.226
74.856
77.912
77.912
78.297
72.023
65.147
%r
• *»
99.0
99.8
98.8
99.1
97.6
99.8
99.4
100.0
98.7
98.7
98.7
100.4
105.2
99.9
97.1
98.3
98.2
99.8
98.5
99.4
97.7
99.2
99.4
101.5
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER
TEST NUMBER: TP3-4
TP3
SAMPLE ELAP
POINT TIME
(WIN)
START 72.0
A-l
2
3
4
5
6
7
fl
9
10
1 1
12
13
14
15
16
1.7
18
19
20
21
22
23
24
75.0
78.0
81 .0
84.0
87.0
90.0
93.0
96.0
99.0
102.0
105.0
108.0
1 1 1 . 0
1 14.0
1 17.0
120.0
1 23.0
126.0
129.0
132.0
135.0
138.0
141.0
144.0
SAMPLE
VOLUME
(DCE)
30
33
36
39
42
45
48
51
55
58
61
65
68
68
70
72
74
77
80
82
86
89
92
95
99
.360
.230
.200
. 190
.280
.370
.560
.750
.060
.460
.860
.260
.030
.030
.175
.290
.640
. 1 80
.040
.975
.075
.290
.495
.900
.144
PTTOT
RDG
(IWH20)
1 .250
1.300
1 .300
1 .400
1 .400
1.500
1.500
1 .600
1 .700
1 .700
1 .700
1 .000
0.000
0.400
0.650
0.790
0.940
1.200
1.250
1 .400
1 .500
1 .500
1.700
1.500
ORIEICE METERTEMP NOZ
RDG (DEG.E) DIA
(TNH20) IN OUT. (IN)
2.400
2.500
2.500
2.700
2.700
2.900
2.900
3.100
3.300
3.300
3.300
1 .950
o.ooo
0.770
1.250
1 .500
1 .800
2.300
2.400
2.700
2.900
2.900
3.300
2.900
89.
93.
93.
94.
94.
100.
102.
102.
102.
102.
102.
100.
100.
94.
94.
93.
94.
94.
96.
96.
100.
100.
100.
100.
84.
85.
85.
84.
84.
86.
86.
86.
88.
88.
88.
88.
88.
86.
88.
88.
86.
86.
86.
86.
88.
88.
88.
88.
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.1.95
0.195
0.195
0.195
0.195
0.195
0.195
STACK
TEMP
(DE)
55.
55.
55.
55.
50.
50.
50.
50.
50.
50.
50.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55,
STACK
VEL
(EPS)
77.152
78.680
78.680
81.650
81.253
84.105
84.105
86.863
89.536
89.536
89.536
69.007
0.000
43.644
55.635
61.335
66.905
75.593
77.152
81 .650
84.516
84.516
89.974
84.516
%T.
«• w
•» «•
98.3
99.3
100.0
99.7
99.2
98.3
93.1
98.6
98.2
98.2
98.2
104.5
0.0
128.4
99.3
100.2
99.5
99.3
99.7
99.6
99.4
99.1
99.0
100.3
-------
OME
YORK RESEARCH CORPORATION
RESEARCH DRIVE', STAMFORD, CONNECTICUT 0690ft
JOB NLIM8ER: 9517-17
CLIENT: EPA
PLANT LOCATION; CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER TP3
DUCT NUMBER: TP3
DUCT AREA: 33. 18SO.FT.,6.5' 1.0.
DUCT LOCATION: SCRUBBER OUTLET
FILTER NUMBERS: 02580
TEST NUMBER: TP3-5
DAT*;: AUG 28,79
TEST
BAR.
PITOT
TIME
SAMPLE ELAP
POINT TIME
START 0
A-l
2
3
4
5
6
7
8
9
1 0
1 1
12
1 3
1 4
15
16
17
1 8
19
20
21
22
23
24
3
6
9
12
15
18
21
24
27
30
33
36
39
42
45
48
51
54
57
60
63
66
69
72
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
SAMPLE
V 0 L U M P1
(DCF)
0
2
5
8
1 1
14
17
20
23
27
30
33
36
39
41
43
46
48
51
54
57
60
64
67
70
.000
.670
.540
.430
.350
.370
.420
.640
.810
.070
.425
.790
.865
.610
.660
.800
.240
.800
.670
.600
.730
.830
.200
.620
.974
PITOT
RDG
(INH20)
1 .
1.
1 .
1 .
1 .
1 .
1.
1 .
1 .
1.
1 .
1 .
1 .
0.
o.
0.
0.
1 .
1 .
1.
1 .
1 .
1 .
1.
300
300
300
300
400
400
600
500
600
700
700
400
100
400
670
860
950
200
300
400
400
700
700
600
ORIFICE WETERTEMP NOZ
RDG (DEG.F) DIA
(INH20) IM OUT (IN)
2.
2.
2.
2.
2.
2.
3.
2.
3.
3.
3.
2.
2.
0.
1 ,
1.
t .
2.
2.
2.
2.
3.
3.
3.
500
500
500
500
700
700
100
900
100
300
300
700
100
770
300
650
850
300
500
700
700
300
300
100
70.
74.
80.
84.
97.
88.
92.
94.
94.
98.
100.
100.
97.
94.
92.
93.
93.
95.
97.
98.
98.
.100.
100.
too.
70.
70.
70.
70.
72.
72.
74.
76.
76.
78.
80.
80.
82.
84.
84.
84.
84.
84.
85.
86.
86.
86.
86.
86.
0.195
0.195
0.195
0. 195
0. 195
0.195
0.195
0.195
0.195
0. 195
0.195
0.195
0.195
0. 195
0.195
0.195
0. 195
0. 195
0.195
0.195
0.195
0.195
0.195
0.195
0^0: SPRAYS OFF
RESS-
TUBE
IN HG: 21
FACTOR: 0
EST STARTED: 1
STACK
TEMP
CDF)
50.
50.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
STACK
VEL
(EPS)
73.193
78.193
78.575
78.575
81.541
81.541
87.172
84.403
87.172
89.854
89.854
81.541
72.279
43.586
56.409
63.909
67.170
75.493
78.575
81 .541
81 .541
89.854
89.854
87.172
.60
.880
223
%I
«w •
«•*
91 .4
97.9
98.5
99.2
98 .5
99.4
97.7
98.9
98.6
98.0
97.9
98.4
99.0
122.2
98.9
99.5
99.4
99.2
97.1
99.8
98.8
97.5
99.0
100.0
-------
YOPK RESEARCH CORPORATION
ONE RESEARCH DRIVE, STAMFORD, CONNECTICUT 06906
JOB NUMBER: 95.17-17
LTENT: EPA
PLAMT LOCATION: CLI«AX
UNIT TESTED: PRIMARY CRUSHER
TEST NUMBER: TP3-5
TP3
SAMPLE ELAP SAMPLE
POINT
TIME VOLUME
(MIN) (DCF1
START
R-1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
72.0
75.0
78.0
81 .0
84.0
87.0
90.0
93.0
96.0
99.0
102.0
1 05.0
108.0
111.0
1 14.0
1 17.0
120.0
123.0
1 26.0
129.0
1 32.0
135.0
1 38.0
141.0
1 44.0
70.
73.
76.
79.
83.
86.
89.
93.
96.
99.
102.
104.
107.
109.
1 11.
114.
116.
119.
122.
125.
128.
131.
134.
138.
141.
974
820
710
890
200
410
800
090
120
120
120
910
340
440
630
190
9.30
360
240
230
240
400
860
400
928
PT.TOT
RDG
(INH20)
1 .200
1 .200
1.500
1.600
1 .600
1.600
1 .600
1 .300
1 .300
1 .300
1 .100
0.800
0.550
0.770
0.900
1 .100
0.750
1.300
1 .300
1 .300
1 .500
1.800
1 .800
1 .800
ORIEICE METERTEMP NOZ
RDG
(INH20
2.300
2.300
2.900
3.100
3.100
3.100
3.100
2.500
2.500
2.500
2.100
1 .550
1.050
1 .500
1 .750
2.100
1.450
2.500
2.500
2.500
2.900
3.500
3.500
3.500
(DEC,
) IN
94.
97.
98.
98.
98.
100.
100.
102.
102.
100.
100.
100.
96.
95.
97.
98.
100.
100.
100.
100.
100.
100.
106.
106.
.F)
OUT
86.
87.
88.
88.
88.
86.
86.
86.
86.
84.
86.
86.
87.
86.
87.
88.
90.
90.
90.
90.
90.
88.
90.
90.
DTA
(IN)
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.1.95
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
STACK
TEMP
(OE)
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
STACK
VEL
(EPS)
75.493
75.493
84.403
87.172
87.172
87.172
37.172
78.575
78.575
78.575
72.279
61.640
51.109
60.473
65.379
72.279
59.682
73.575
78.575
78.575
84.403
92.459
92.459
92.459
%I
«• <•
«• ^
98.2
99.4
97.9
98.7
95.7
101. 1
98.1
99.8
98.9
99.2
100.0
101.9
106.3
96.2
99.5
98.2
104.9
94.7
98.4
99.0
96.9
97.2
98.8
98.4
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE1, STAMFORD, CONNECTICUT 06906
JOB NUMBER: 951.7-17
CLIENT: EPA
PLANT LOCATION: CLTVAX vn^Y
UNIT TESTED: PRIMARY CRUSHER TP3
DUCT NUMBER: TP3
DUCT AREA: 3.3. 18SO.FT. ,6.5" I.D.
DUCT LOCATION; SCRUBBER OUTLET
FILTER NUMBERS: 03000
TEST NUMBER: TP3-6
DATE: AUG 28,79
TEST COND: SPRAYS OFF
BAR. PRESS-IN HG: 21.60
PITOT TUBE FACTOR: 0.880
TIME TEST STARTED: 1528
SAMPLE ELAP SAMPLE
POINT TIME VOLUME
fMIN) (DCF)
START 0.0
B-1
2
3
4
5
6
7
8
9
10
1 1
12
13
1 4
15
16
17
1 8
19
20
21
22
2 J
24
3.0
6.0
9.0
12.0
15.0
18.0
21.0
24.0
27.0
30.0
31.0
36.0
19.0
42.0
45.0
48.0
51. .0
54.0
57.0
60.0
6.3.0
66.0
69.0
72.0
42
45
48
51
54
57
61
64
67
70
73
76
79
81
83
86
88
91
94
97
100
103
107
1 10
113
.500
.300
.300
.460
.700
.820
.030
.300
..530
.620
.700
.780
.260
.320
.580
.120
.850
.740
.640
.530
.420
.630
.030
.460
.897
PITOT
RDG
CINH20)
1 .200
1.400
1.500
1 .600
1 .400
1 .600
1 .600
1 .600
1 .400
1 .400
1 .400
0.800
0.600
0.720
0.950
1.100
1 .200
1 .200
1.200
1.200
1 .500
1.700
1 .700
1.700
ORIFICE METERTEMP NO?.
RDG (DEG.F) DlA
(INH20) IN OUT (IM)
2.300
2.700
2.900
3.100
2.700
3.100
3.100
3.100
2.700
2.700
2.700
1.550
1.150
1 .400
1 .850
2.100
2.300
2.300
2.300
2.300
2.900
3.300
3.300
3.300
75.
82.
90.
92.
94.
95.
96.
98.
100.
101.
102.
100.
96.
94.
94.
95.
96.
97.
97.
100.
100.
1 04.
104.
108.
75.
76.
76.
76.
78.
76.
76.
78.
80.
81.
83,
84.
84.
84.
84.
85.
86.
86.
86.
86.
86.
87.
87.
90.
0.195
0. 195
0.195
0.195
0.195
0.195
0.195
0. 195
0.195
0.195
0.195
0.195
0.195
0. 195
0.195
0.195
0.195
0. 195
0.195
0.195
0.195
0.195
0.195
0.195
STACK
TEMP
(DF)
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
STACK
VEL
(EPS)
75.494
81.543
84.405
87.173
81.543
87.173
87.173
87.173
81 .543
81 .543
81 .543
61.641
53.382
58.477
67.171
72.280
75.494
75,494
75.494
75.494
84.405
89.856
89.856
89.856
4V «•
99.3
97.9
99.0
98. 1
100.5
97.0
98.7
97.1
98.9
98.4
98.1
104.2
100.2
100.6
98.6
98.3
99.6
99.8
99.5
99.2
98.8
98.0
98.8
98.4
-------
YORK RESEARCH CORPORATION
RESEARCH DRIVE. STAMEORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
LIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PRIMARY CRUSHER
TEST NUMBER: TP3-6
TP3
SAMPLE ELAP
POINT TIME
(MIN)
START 72.0
A-1
7
3
4
5
6
7 .
8
9
1.0
l.t
12
13
1 4
15
16
1.7
18
1.9
20
21
22
23
24
75.0
7fl.O
SI .0
84.0
87.0
90.0
93.0
96.0
99.0
102.0
105.0
108.0
111.0
1 1. 4 . 0
117.0
120.0
123.0
1 26.0
129.0
132.0
1. 3 5 . 0
138.0
141 .0
144.0
SAMPLE
VOLUME
(DCE)
13.897
16.780
19.870
23.070
26.280
29.720
33. 160
36.630
40.090
43.120
45.740
47.890
47.890
47.890
49.935
52.300
54.780
57.390
60.280
63.195
66.330
69.485
72.620
76.050
79.243
PITOT
RDG
(INH20)
1 .200
1.400
1 .500
1 .500
1.700
1.700
1 .700
1.700
1 .200
0.900
0.600
0.000
0.000
0.500
O.ROO
0.850
0.950
1 .200
1.200
1.400
1 .400
1 .400
1.700
1.400
ORIEICE METERTEMP NQZ
RDG (DEG.F) DIA
(INH20) IN OUT (IN)
2.300
2.700
2.900
2.900
3.300
3.300
3.300
3.300
2.300
1 .750
1 . 150
o.ooo
0.000
0.960
1 .550
1.650
1.850
2.300
2.300
2.700
2.700
2.700
3.300
2.700
95.
1 00.
105.
108.
100.
110.
112.
U4.
114.
108.
104.
104.
104.
104.
110.
110.
1.10.
110.
105.
105.
106.
106.
110.
114.
88.
90.
90.
91.
92.
92.
94.
96.
96.
98.
76.
76.
76.
76.
96.
96.
96.
94.
95.
95.
96.
96.
96.
98.
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0. 195
0.195
0.195
0.195
0. 195
0.195
0.195
0.195
0.195
0. 195
0.195
0.195
0.195
0.195
STACK
TEMP
(DE)
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
STACK
VEL
(EPS)
75
81
84
84
89
89
89
89
75
65
5J
0
0
48
61
63
67
75
75
81
81
81
89
81
.494
,543
.405
.405
.856
.856
.856
.856
.494
.380
. 3 8 2
.000
.000
.7.31
.641
.538
.171
.494
.494
.543
.543
.543
.856
.54.3
%T
99.2
98.0
97.7
97.6
99.0
98.2
98.7
98.1
101 .9
101 .9
104.5
0.0
0.0
108.9
97.5
99.2
98.8
97.7
98.9
98.6
99.0
98.4
97.5
99.3
-------
YORK PFSEARCH .CORPORATION
ONE RESEARCH DRIVE. STAMEORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION; CLIMAX MO^Y
UNIT TESTED: PRIMARY CRUSHER
i STACK
| STACK
1
NUMBER: TP3
LOCATION: SCRUBBER OUTLET
JOS NUMBER
TEST "MJMRER: 2
DATE: AUG 29,79
CONDITIONS: SPfM
AMBIENT TEiMP-OF.G
.BAR., :PRESS - 1^
: 9517-17
Y OF*
F: 65
HG : 21.60-
ANDERSEN PARTICLE SIZING
STAGE
t
2
3
4
5
6
7
8
.. FILTER
ST&CK
STACK
G&S AN
1 '
DIAMETER
C MICRONS) fM
> 14.62
14.62-9.12
9.12-6.18
6. 18-4.21
4.21-2.70
2.70-1.35
1 .3-5-0.83
0.83-0.54
< 0.54
TEMP.(DEG.E).
WEIGHT
TLLIGRAMS)
1.18
0.60
1.01
0.66
0.48
0.51
0.78
0.57
0.80
. . . 55.0
PRESSURECIN.HG) . . 21.55
ALYSIS (DRY PERCENT)
C02 .... . 0.00
CO . .
N2 . .
02 . .
H20 . .
. . . 0.00
. . . 79.10
. . . 20.90
. . . 3.00
% PER CUM?; GR/SCFD
STAGE
-------
Pebble Screening and Milling
-------
TP-1 Screen Exhaust
-------
YORK RESEARCH CORPORATION JOB
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PEBBLE SCREEN TP1
9517-17
PARTICULATE SUMMARY IN ENGLISH UNITS
DESCRIPTION
UNITS
TP1-1
TP1-2
TP1-3
AVERAGE
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE
STACK PRESSURE. ABS.
STACK AREA
NET TIME OF RUM
PERCENT ISO
GAS DATA
AVG STACK GAS
AVG STACK TEMPERATURE
ACTUAL STACK FLO*RATE
STK FLOWRATE,DRY ,
MOLECULAR WT-ORY
MOLECULAR WT-STK
MOLE FRACTION DRY \3
GAS ANALYSIS CDRY
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION D
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD
VOL DRY GAS-METER
VOL DRY GAS-STD CQND
AVG GAS METER TEMP
AVG ORTF PRES DROP
PARTICIPATE WEIGHT
NET WEIGHT PARTIAL
NET HEIGHT TOTAL
PARTICIPATE EMISSIONS
PARTIAL
SCFD
SCFD 012%C02
ACF
HOUR
PROCESS UNIT
AUG
TN.HG
IN.HG
SO. FT
WIN
TTY FPS 7
PE DFG.F
TE ACFM
D DSCFM
K GAS
S
AS
EPCENT BASIS)
\ T \
A 1 A
ML
ON0 SCF
OND DEF
D DSCF
DEG.F
IM.H20
DATA
MG
MG
29,79
21 .60
21.48
0.47
80.0
97.7
1 .394
74.1
2014.
1435.
28.81
28.81
1.000
0.0
20.3
0.0
79.7
0.0
0.0
0.00
72.69
50.51
94.3
1.981
0.00
23.75
AUG 29,79
21 .60
21.48
0.47
90.0
101. 1
65.465
80.0
1834.
1278.
28.82
28.70
0.989
0.0
20.5
o.o
79.5
l.l
11.3
0.54
68.18
46.35
105.8
1, , 5 8 5
0.00
23.16
.AUG 30,79
21 .60
21.48
0.47
80.0
106. 1
64,182
70.0
1798.
1273.
28.82
28.67
0.986
0.0
20.5
0.0
79.5
1.4
14.3
0.68
69.24
48.46
89.6
1 .588
0.00
25,62
101.6
67.180
74.7
1882.
1329.
0.0
20.4
0.0
79.6
0.8
0.00
24.18
GRAINS
GRAINS
GRAINS
POUNDS
POUNDS
TOTAL
GRAINS
GRAINS
GRAINS
POUNDS
POUNDS
PER
PER
PER
PER
PER
PER SCFD
PER SCFD ai2%C02
PER flCF
PER HOUR
PER PROCESS UNIT
0.00000
0.00000
0.00000
0.00
0.00000
0.00724
o.ooooo
0.00516
0.09
0.00000
0.00000
o.ooooo
o.ooooo
0.00
o.ooooo
0.00770
o.ooooo
0.00536
0.03
0.00000
0.00000
0.00000
0.00000
0.00
0.00000
0.00814
0.00000
0.00576
0.09
0.00000
o.ooooo
0.00000
0.00000
0.00
o.ooooo
0.00769
0.00000
0.00543
0.09
o.ooooo
-------
ONE
YORK RESEARCH CORPORATION
RESEARCH DRIVE, STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT; EPA
PLANT LOCATION; CLIMAX MOLY
UNIT TESTED: PEBBLE SCREEN TP1
PARTICULATE SUMMARY IN METRIC UNITS
DESCRIPTION UNITS
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE
STACK PRESSURE. ARS
STACK AREA
NET TIME OF RUN
PERCENT ISOKINETIC
GAS DATA
AVG STACK GAS VELOC
AVG STACK TEMPERATURE
ACTUAL STACK FLOWRATE
STK FLOWRATE,DRY,STD
MOLECULAR WT-DRY
MOLECULAR rfT-STK GA,<
MOLE FRACTION DRY
GAS ANALYSIS (DRY
CARRON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION D
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD C
VOL DRY GAS-METER c
VOL DRY GAS-STD COND
AVG GAS METER TEMP
AVG ORIF PRES DROP
PARTICULATE WEIGHT
NET WEIGHT PARTIAL
NET WEIGHT TOTAL
PARTICIPATE EMISSIONS
PARTIAL
MG/NORMALIZED cu.METERS
MG/NORM. CU.M 912% C02
MG/ACTUAL CU. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
TOTAL
MG/NORMALIZED cu.METERS
MG/NORM. CU.M 012% C02
MG/ACTUAL cu. METERS
KILOGRAMS/HOUR
KTLOGM PER PROCESS UNIT
TP1-1
TP1-2
TP1-3
AVERAGE
MM.HG
MM.HG
M2
MTN
ITY M/S
RE DEG.C
TE AM3/M
D DNM3/M
K GAS
s
AS
ERCENT. 8AS
ATA
A I A
ML
0 N D N M 3
OND DM3
D D N M 3
DEG.C
MM.H20
DATA
MG
MG
AUG 29,79
548.64
545.65
0.043
80.0
97.7
21.913
23.4
57.
41.
28.81
28.81
1 .000
IS)
0.0
20.3
o.o
79.7
0.0
0.0
0.00
2.06
1.43
34.6
50.324
0.00
23.75
AUG 29,79
548.64
545.65
0.043
80.0
101. 1
19.954
26.7
52.
36.
28.82
28.70
0.989
0.0
20.5
0.0
79.5
1.1
11.3
0.02
1.93
1.31
41.0
40.259
0.00
23.16
AUG 30,79
548.64
545.65
0.043
80.0
106. 1
19.563
21.1
51.
36.
28.82
28.67
0.986
0.0
20.5
0.0
79.5
1.4
14.3
0.02
1.96
1.37
32.0
40.333
0.00
25.62
101 .6
20.477
23.7
53.
38.
0.0
20.4
0.0
79.6
0.8
0.00
24.18
0
0
0.00
0.00
0.00
0.00
.00000
16.57
0.00
11 .80
0.04
.00000
0.00
0.00
0.00
0.00
o.ooooo
17.61
0.00
12.26
0.04
o.ooooo
0.00
0.00
0.00
o.oo
0.00000
18.63
0.00
13.19
0.04
0.00000
0.00
0.00
0.00
0.00
o.ooooo
17.60
0.00
12.42
0.04
0.00000
-------
ONE
YOKK RESEARCH CORPORATION
RESEARCH DRIVE:1. STAMFORD, CONNECTICUT
JOB NUMBER: 9517-}?
06906
CLIENT: EPA
PLANT LOCATION: CLIMAX
UNIT TESTED; PEBBLE SCREEN
TP1
TEST NUMBER: TPl-l
DATE: AUG 29,79
TEST coND: NORM 4 r,
DUCT NUMBER: TP1
DUCT AREA: 0 . 47SO . FT . ,
-------
YORK RESEARCH CORPORATIOM
ONE RESEARCH DRIVE1, STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLAMT LOCATION: CLIMAX
UNIT TESTED: PEBBLE SCREEN TP1
OUCT NUMBER: TPl
DUCT AREA; 0.47SQ.FT. .9.25"
OUCT LOCATION: SCREEN EXHAUST
FILTER NUMBERS: 02850
I.D.
TEST NUMBER: TP1-2
DATE: AUG 29,79
TEST COND: NORMAL
BAR. PRESS-IN HG: 21.60
PITOT TUBE FACTOR: 0.930
TIME TEST STARTED: 1549
SAMPLE FLAP SAMPLE
POINT
TIME VOLUME
(MIN) (DCF)
START
3-1
2
3
4
5
6
7
8
START
A-l
2
3
4
5
6
7
8
0.0
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
40.0
45.0
50.0
55.0
60.0
65.0
70.0
75.0
80.0
238.
242.
246.
250.
255.
259.
264.
267.
271.
271.
275.
280.
284.
288.
293.
296.
301.
306.
001
490
950
370
510
860
250
490
244
244
810
600
790
950
300
200
860
182
PITOT
RDG
(IMH20)
0.840
0.850
0.760
0.770
0.820
0.820
0.420
0.600
1.000
0.980
0.670
0.830
0.820
0.800
0.710
0.800
ORIFICE
RDG
(IMH20)
1.750 '
1 .750
1.600
1.600
1.700
1 .700
0.820
1.200
2.000
1 .990
1.350
1.650
1.650
1.600
1.400
1 .600
METERTEMP NOZ
(DEG.F)
IN
92.
100.
104.
1 08.
110.
112.
114.
114.
113.
116.
118.
118.
1 18.
118.
119.
119.
OUT
92.
92.
94.
96.
96.
98.
98.
100.
100.
102.
102.
102.
104.
104.
105.
106.
DIA
( I M )
0.196
0.196
0.146
0.196
0.196
0.196
0.196
0.196
0.196
0.196
0.196
0.196
0.196
0.196
0.196
0.196
STACK
TEMP
(DF)
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
STACK
VEL
(EPS)
68.191
68.596
64.863
65.288
67.375
67.375
48.219
57.632
74.403
73.655
60.901
67.784
67.375
66.548
62.693
66.548
%I
--
--
104.8
102.8
82.9
123.1
100.8
101 .4
104.0
100.8
95.3
100.6
106.0
94.6
99.4
67.1
138.6
99.7
-------
YORK RESEARCH CORPORATION
RESEARCH DRIVE1. STAMFORD, CONNECTICUT
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
(JMIT TESTED: PEBBLE SCREEN TPl
DUCT NUMBER: TPI
DUCT AREA: 0.47SO.FT. ,9.25" I.D.
DUCT LOCATION: SCREEN EXHAUST
FILTER NUMBERS: 02750
JOB NUMBER: 9517-17
06906
TEST NUMBER: TPI-3
DATF: AUG 30,79
TEST COND: NORMAL
BAR. PRESS-IN HG: 21.60
PITOT TUBE FACTOR: 0.930
TIME TEST STARTED: 854
POINT
START
A-l
2
3
4
5
6
7
g
START
8-1
2
3
4
5
6
7
8
! ELAP SAMPLE
TIME VOLUME
fMIN) (OCF)
0.
5.
10.
15.
20.
25.
30.
35.
40.
40.
45.
50.
55.
60.
65.
70,
75,
80.
.0
.0
.0
,0
,0
,0
.0
,0
,0
.0
,0
,0
,0
,0
.0
,0
.0
.0
306
310
315
320
324
329
334
338
342
342
346
350
354
359
363
367
371
375
.583
.890
.290
.680
.990
.420
.160
.100
.060
.06°
.750
.800
.990
.470
.700
.110
.860
.828
PITOT
RDG
( INH20)
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
.820
.960
.950
.800
.900
.640
.680
.620
.700
.700
.740
.880
.750
.740
.640
.660
ORIFICE METERTEMP NOZ
RDG (DEG.F) DIA
(INH20) IN OUT (IN)
1
2
1
1
1
1
1
1
1
1
1
t
1
1
1
1
.700
.000
.950
.650
.850
.350
.400
.380
.450
.450
.550
.850
.550
.550
.330
.400
74.
80.
86.
92.
96.
96.
92.
96.
94.
98.
100.
102.
104.
106.
106.
106.
74.
76.
76.
78.
80.
82.
82.
84.
84.
86.
86.
88.
90.
90.
90.
92.
0.196
0.196
0.196
0.196
0. 196
0.1,96
0.196
0.196
0.196
0.196
0.196
0.196
0.196
0.196
0.196
0. 196
STACK
TEMP
CDF)
70.
70.
70.
70.
70.
70.
70.
70.
70.
70.
70.
70.
70.
70.
70.
70.
STACK
VEL
(FPS)
66.778
72.254
71.876
65.958
69.959
58.995
60.811
58.066
61.698
61.698
63.437
69. 178
63.864
63.437
58.995
59.910
%I
-* «
•
-------
YORK RESEARCH CORPORATION
JOB NUMBER! 9517-17
ONE RESEARCH DRIVE, STAMFORD, CONNECTICUT 06906
CLTENT; EPA TEST NUMBER; 1
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PEBBLE SCREEN
ST ACK JiU MEJER :.._.TP1
STACK LOCATION: SCREEN EXHAUST
DATE: AIJG 29,79
CONDITIONS: NORMAL
RAR. PRESS - IN HG:21.60
ANDERSEN PARTICLE SIZING
DIAMETER
STAGE fMICRONS)
WEIGHT
fMTLLIGRAMS)
% PER CU.M% GR/SCFD MG/NCMD
STAGE 11.59
11 .59-7.23
. 2. 30
5.01
13.95
30.38
86.05
0.001173
0.002556
2.69
5.85
7.23-4.89
2.16
13.10
55.67
0.001102
2.52
4
5
f>
4.89-3.32
3.32-2.12
2.12-1.05
.. 1.57 -: -
1.45
1 .10
9.52
8.79
6.67
42.57
33.05
24.26
0.000801
0.000740
0.000561
1.8 3
1.69
1 .28
7 1 .05-0.64
8 0.64-0.40
FILTER < 0.40
,; °-6 6 -.;.-
0.46
1.78
4.00
2.79
10.79
17.59
13.38
10.79
0.000337
0.000235
0.000908
0.77
0.54
2.08
STACK TEMP. (DEG.F).
65.0
GAS ANALYSIS (DRY PERCENT)
C02 0.00
CO 0.00..
N2 ... .. . . . 79.10
02 . . . . . 20.90
H2Q . .... 2.00
SAMPLING RATE(ACFM) . . .
________ , ____ _( S C F M q ) . . _...
IMPACTOR TEMP. (DEC. E) .
_P ARTLCLFLJDEN5..r T Y.( GM./C.C )
TEST TIME (MIN)
TOTAL WEIGHT CMG) . . .
0.710
_0...3..Q4.
0.014
65.0
1 . .00
60.00
16.49
TOTAL MG/NCMD
19.25
-------
YORK 'RESEARCH CORPORATION
JOB NUMBERi_9L5LLlill-
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA TEST NUMBER: 2
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PEBBLE SCREEN
STACK NUMBER: TPI
STACK
LOCATION: SCREEN EXHAUST
DATE: AUG 29,79
CONDITIONS: NORMAL
AMBIENT TEMP-OEG F: 65
BAR.
PRESS - TM
HG:21 .60
AMOERSEN PARTICLE SIZING
STAGE
1
2
3
4
5
6
7
8
FILTER
STACK
STACK
GAS AN
DIAMETER
(MICRONS)
> 11.80
1 1 .80-7.36
7.36-4.98
4.93-3.38
3.38-2.16
7.16-1.07
1.07-0.65
0.65-0.41
< 0.41
TEMP. (DEG.E
PRESSURE(TN
flLYSIS (DRY
C02 .
CO .
N2 .
02 .
H20 .
WEIGHT
(MILLIGRAMS)
5.61
0.96
1.37
1.08
0.94
0.46
0.56
0.1.6
0.01
). . . . 70.0
.HG) . . 21.48
PERCENT)
.... 0.00
.... o.oo
. . . . 79.10
.... 20.90
.... 2.00
% PER CUM% GR/SCEO
STAGE OIPPER DIAM PER STAGE
50.31
8.61 49.69
12.29 41.08
9.69 28.79
8.43 19.10
4.13 10.67
5.02 6.55
1.43 1.52
0.09 0.09
SAMPLING RATE
IMPACTOR TE*P
PARTICLE DENS
TEST TIME (MI
TOTAL WEIGHT
TOTAL GR/SCFD
TOTAL MG/NCMQ
0.002505
0.000429
0.000612
0.000482
0.000420
0.00020S
0.000250
0.000071
0.000004
. (OEG.F) .
ITY(GMXCC)
N )
(MG) . . .
MG/NCMD
PER STAGE
5.73
0.98
1 .40
1.10
0.96
0.47
0.57
0.16
0.01
0.690
0.485
0.014
70.0
1 .00
7 t . 2 0
11.15
. 0.00498
11.40
-------
YORK RES EARCH CORPORAT10N
JOQ NUMnER; 9517-17
ONE RESEARCH DRIVE, STAMFORD, CONNECTICUT 06906
CLIENT: EPA TEST NUMBER: 3
j: PLANT LOCATION: CLIMAX .VOLY
'4! UNtT TESTED: PEBBLE. SCREEM
; STACK NUMBER: TPI
STACK
;>; •
STAGE
1.
2
3
;;, *..
: 5
6
-" 7 ;
8
FILTER
111 STACK
..STACK
GAS AN
.J '
LOCATION: SCREEN EXHAUST
DIAMETER
(MICRONS)
> 11.24
It. 24-7.00
7.00-4.74
4.74-3.22:
3.22-2.05
2.05-1.01
1 .01-0.61
< 0.38
TEMP.CDEG.E
PRESSURE (.IN
ALYSIS (DRY
C02 .
CO .
N2 .
02 .
H20 .
ANDERSEN
WEIGHT
(MILLIGRAMS)
2.39
0.66
0.97
>•'•••/. .0^.49 . •• .'.,
0.57
0.30
0.09
O.OR
0.04
). . . . 70.0
PERCENT)
.... 0.00
. . . . 0.00
. . . . 79. 10
. . . . 20.90
.... 2.00
DATE: AUG 29,79
.CONDITIONS: NORMAL
AMBIENT TEMP-DEG E: 65
8AR. PRESS - IN
PARTICLE SIZING
% PER C!.IM% GR/SCED
STAGE
-------
TP-2 Bucket Elevator Hood Exhaust
-------
YORK RESEARCH CORPORATION
RESEARCH DRIVF. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PEBBLE SCREEN TP2
PARTICIPATE SUMMARY IN ENGLISH UNITS
JOB NUMBER: 9517-1.7
DESCRIPTION .
UNITS
TP2-1
TP2-2
TP2-3
AVERAGE
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE TN.HG
STACK PRESSURE, APS. TN.HG
STACK AREA SO. FT
NET TIME OF RUN MTN
PERCENT ISOKINETIC
GAS DATA
<\VG STACK GAS VELOCITY FPS
AVG STACK TEMPERATURE DEG.F
ACTUAL STACK FLOWRATF ACFM
STK FLOWRATE.DRY.STO DSCFM
MOLECULAR WT-DRY STK GAS
•MOLECULAR XT-STK GAS
MOLE FRACTION DRY GAS
GAS ANALYSIS (DRY PERCENT BAS
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION DATA
TOTAL H20 COLLECTED ML
VOL H20 VAPOH-STD COND SCF
VOL DRY GAS-METER COND DFF
VOL DRY GAS-STD COND DSCF
AVG GAS METER TEMP DEG.F
AVG OPIF PRES DROP IN.H20
PARTICIPATE ^EIGHT DATA
NET WEIGHT PARTIAL MG
NET WEIGHT TOTAL MG
PARTTCULATE EMISSIONS
PARTIAL
GRAINS PER SCFD
GRAINS PER SCFD 012%C02
GRAINS PER ftCF
POUNDS PER HOUR
POUNDS PER PROCESS UNIT
TOTAL
GRAINS PER SCFD
GRAINS PER SCFD iai2%C02
GRAINS PER ACF
POUNDS PER HOUR
POUNDS PEW PROCESS UNIT
AUG 29,79
21 .60
2t .33
0.28
80.0
102. 8
67.109
65.6
1115.
796.
28.82
28.75
0.993
IS)
0.0
20.5
0.0
79.5
0.7
7.0
0.33
72.61
50.03
98.5
1.754
0.00
145.92
0.00000
0.00000
0.00000
0.00
o.ooooo
0.04492
0.00000
0.03207
0.31
0.00000
AUG 29,79
21.60
21.33
0.28
80.0
106.0
64.485
6Q. 1
1072.
741 .
28.82
28.48
0.969
0.0
20.5
0.0
79.5
3.1
32.4
1 .54
70.74
48.04
106.3
1.581
o.oo
262.00
0.00000
O.OOnQO
0.00000
0.00
0.00000
0.08399
0.00000
0.0581 1
0.53
0.00000
AUG 30,79
21.60
21 .33
0.28
80.0
109.4
62.652
65.0
1041.
738.
28.82
28.66
0.985
0.0
20.5
0.0
79.5
1.5
15.9
0.75
70.99
49.33
93.3
1 .509
0.00
201.90
0.00000
0.00000
0.00000
0.00
o.ooooo
0.06303
o.ooooo
0.04466
0.40
0.00000
106. 1
64.749
66.6
1076.
759.
0.0
20.5
0.0
79.5
1.8
0.00
203.27
o.ooooo
o.ooooo
0 . 0 0000
0.00
0.00000
(1
0.06398
o.ooooo
0.04495
0.41
0.00000
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION; CLIMAX MOLY
UNIT TESTED: PEBBLE SCREEN TP2
JOB NUMBER: 9517-17
PARTICULATE SUMMARY IN METRIC UNITS
DESCRIPTION
UNITS
TP2-1
TP2-2
TP2-3
AVERAGE
GENERAL DATA
DATE OE RUN
BAROMETRIC PRESSURE
STACK PRESSURE. ABS
STACK AREA
NET TIME OE RUN
PERCENT ISOKINETIC
GAS DATA
AVG STACK GAS VELOC
AVG STACK TEMPERATU
ACTUAL STACK ELOWRA
STK" FLOWRATE.DRY.STD
MOLECULAR ^T-DRY s
MOLECULAR WT-STK G
MOLE FRACTION DRY
GAS ANALYSIS (DRY
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD
VOL DRY GAS-METER
VOL DRY GAS-STD COND
AVG GAS METER TEMP
AVG ORIF PRES DROP
PARTICULATE HEIGHT
MET WFTGHT PARTIAL
NET WEIGHT TOTAL
PARTICIPATE EMISSIONS
PARTIAL
MG/NORMALIZED cu.METERS
MG/NORM. CU.M 012% C02
MG/ACTUAL CU. METERS
KILOGRAMS/HOUR
KILOGMnP£R PROCESS UNIT
TOTAL
MG/MORMALIZED CU.METERS
MG/NORM. CU.M 012% C02
MG/ACTUAL cu. METERS
KILOGRAMS/HOUR
KTLOGM PER PROCESS UNIT-
MM.HG
MM.HG
M2
MTN
ITY M/S
RE DEG.C
TE AM3/M
D DNM3/M
K GAS
S
as
ERCENT RAS
ATA
A t A
ML
OND NM3
OND DM3
D DNM3
DEG.C
MM.H20
DATA
MG
MG
AIIG 29,79
548.64
541.73
0.026
80.0
102.8
20.455
18.7
32.
23.
28.82
28.75
0.993
IS)
0.0
20.5
0.0
79.5
0.7
7.0
0.01
2.06
1.42
36.9
44.545
0.00
145.92
AUG 29,79
548.64
541.73
0.026
80.0
106.0
19.655
20.6
30.
21.
28.82
28.48
0.969
0.0
20.5
0.0
79.5
3.1
32.4
0.04
2.00
1.36
41.3
40.148
0.00
262.00
AUG 30,79
548.64
541.73
0.026
80.0
109.4
19.096
18.3
29.
21.
28.82
28.66
0.985
0.0
20.5
0.0
79.5
1.5
15.9
0.02
2.01
1.40
34.0
38.322
0.00
201.90
106.1
19.735
19.2
30.
21.
0.0
20.5
0,0
79.5
1.8
0.00
203.27
0.
1
0.
0.00
0.00
0.00
0.00
00000
02.79
0.00
73.38
0. 14
ooooo
0.00
0.00
0.00
0.00
0.00000
192.20
o.oo
132.97
0.24
0.00000
0.00
0.00
0.00
0.00
0.00000
144.23
0.00
102.21
0.18
0.00000
0.00
0.00
o.oo
0.00
0.00000
146.41
0.00
102.85
0. 19
0.00000
-------
ONE
YORK RESEARCH CORPORATION
RESEARCH DRIVE1, STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MOf.Y
UNIT TESTED: PEBBLE SCREEM T?2
TEST NUMBER: TP2-1
DATE: AUG 29,79
TEST COND: NORMAL
DUCT NUMBER: TP2
DUCT AREA: 0.28SQ.FT. ,7. 125" I.D.
DUCT LOCATION: BUCKET ELEVATOR EXHAUST
FILTER NUMBERS; 02700
SAMPLE ELAP
POINT
--
START
A-l
7
3
4
5
6
7
8
START
B-1
2
3
4
5
6
7
8
TIME
C M I N )
0.0
5.0
10.0
1 5.0
20.0
?5.0
30.0
35.0
40.0
0.0
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
SAMPLE
VOLUME
(OCF)
134.307
138.330
141 .940
146.350
150. 120
154.220
158.540
163.690
169.297
169.297
173. 190
178.560
183.040
187.510
192. 130
196.500
201.550
206.915
PITOT
RDG
(INH20)
0.680
0.680
0.670
0.660
0.980
0.880
1 .600
1 .800
0.980
1 .000
0.930
0.920
0.940
0.93"
1 .250
1.100
ORIFICE
ROC
(INH2Q)
1
1
1
1
1
1
2
3
1
1
1
1
1
1
2
1
.200
.200
.150
.150
.550
.550
.850
.200
.750
.750
.630
.610
.650
.650
.200
.950
BAR. PRESS-IN HG: 21
PITOT TUBE FACTOR: o
TIME TEST STARTED: 1
METERTEMP NO?.
(OEG
IN
82.
87.
87.
91.
96.
102.
107.
112.
112.
11 3.
114.
1 14.
1 15.
1 15.
119.
1 20.
.F)
OUT
79.
80.
82.
83.
85.
87.
89.
91.
94.
95.
96.
98.
100.
101 .
102.
104.
DIA
(IN)
0.197
0.197
0.197
0.197
0.197
0. 197
0.197
0.197
0.197
0. 197
0.197
0.197
0.197
0.197
0.197
0. 197
STACK
TEMP
(DF)
70.
70.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
STACK
VEL
(EPS)
56.360
56.360
55.680
55.263
63.812
63.812
86.044
91.263
67.340
68.023
65.599
65.246
65.951
65.599
76.053
71 .344
.60
.860
218
%I
--
--
112.8
100.7
123.1
105.5
98.9
103.5
91.3
93.2
87.1
118.7
102.5
102.6
104.7
99.4
98.9
111.6
-------
ONE
YORK RESEARCH CORPORATION
RESEARCH DRIVE'. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX
UNIT TESTED: PEBBLE SCREEN TP2
OUCT NUMBER: TP2
DUCT AREA: 0.28SO.FT..7.125" I
D.
DUCT LOCATION: BUCKET ELEVATOR EXHAUST
ETLTER NUMBERS: 02430
TEST NUMBER: TP2-2
DATE: AUG 29,79
TEST COND: NORMAL
BAR. PRESS-IN HG: 21.60
PITOT TUBE FACTOR: 0.860
TIME TEST STARTED: 1542
SAMPLE
POINT
--
START
B-1
2
3
4
5
6
7
8
START
A-l
2
3
4
5
6
7
8
ELAP SAMPLE
TIME VOLUME
("IN) CDCF)
0.0 207.344
5.0 212.020
10.0 216.490
15.0 221.050
20.0 225.170
25.0 229.380
30.0 233. 480
35.0 238.210
40.0 243.186
0.0 243.186
5.0 247.290
10.0 251.070
15.0 254.750
20.0 258.570
25.0 263.000
30.0 267.640
35.0 272.710
40.0 278.081
PITOT
ROG
INH2Cn
0.930
0.940
0.910
0.920
0.750
0.760
1.100
1.100
0.620
0.620
0.550
0.640
0.970
0.950
1.300
1.300
ORIFICE METERTEMP NOZ
ROG (DEG.F) DIA
(I
1
1
1
1
1
1
I
1
I
1
0
1
I
1
2
2
NH20;
.650
.650
.550
.600
.350
.350
.950
.950
. 100
.100
.990
.150
.700
.630
.300
.270
1 IN
104.
104.
109.
110.
1 12.
112.
115.
117.
115.
115.
115.
115.
118.
120.
122.
124.
OUT
0.
104.
105.
105.
104.
104.
105.
105.
103.
104.
104.
105.
106.
106.
107.
108.
(IN)
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
o.
0.
0.
0.
197
197
197
197
197
197
197
197
197
197
197
197
197
197
197
197
STACK
(DF)
100.
65.
65.
65.
65.
65.
65.
65.
65.
65.
70.
70.
70.
70.
70.
70.
STACK %I
VEL
(EPS)
68.
66.
65.
65.
59.
59.
71.
71.
53.
53.
50.
54.
67.
66.
73.
78.
064
256
190
547
182
576
673
673
809
809
921
930
625
924
287
287
124
103
107
96
108
105
100
105
116
107
111
106
100
106
99
104
.0
.9
.2
.2
.7
.2
.7
.8
.3
.0
.1
.9
.5
.2
.2
.8
-------
O.ME
YORK RESEARCH CORPORATION
RESEARCH DRIVE'. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 951.7-17
CLIENT: EPA
Pf.,ANT LOCATION: CLIMAX MOt.(Y
(PITT TESTED: PEBBLE SCREEN
DUCT NUMBER: TP2
TEST NUMBER: TP2-3
DATE: AUG 30,79
TEST CQNf): NORMAL
BAR. PRESS-IN HG: 21.60
DUCT AREA: 0 . 28SO . FT . . 7 . 1 25 " I.D. PITOT TUBE FACTOR: 0
DUCT LOCATION: BUCKET ELEVATOR EXHAUST TIME TEST STARTED:
FILLER NUMBERS; 02400
SAMPLE ELAP SAMPLE PTTOT ORIFICE METEPTEMP Nf)Z STACK STACK
POINT
TIM'E VOLUME
(MIN) (DCF)
START
A-l
2
3
4
5
6
7
8
START
0-1
2
}
4
5
6
7
9
0.0
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
0.0
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
278.
282.
286.
290.
29.3.
297.
303.
308.
313.
313.
318.
322.
327.
331.
335.
339.
344.
349.
693
620
410
150
860
990
7QO
480
364
364
750
9^0
4.1 0
860
810
680
620
680
RDG
(INH20)
0.680
0.680
0.660
0.650
0.850
0.770
1 .100
1 .050
0.870
0.960
0.920
0.910
0.660
0.700
1 .100
1 .100
RDG
(INH20)
1 .200
1.200
1.130
1.130
1.450
1.350
1.950
1.930
1 .550
1.700
1 .600
1.630
1 .170
1.250
1.950
1.950
(DEG
IN
79.
84.
89.
92.
96.
93.
98.
103.
101 .
103.
105.
107.
1 07.
107.
110.
11.2.
.F)
OUT
76.
78.
79.
80.
83.
86.
87.
88.
89.
90.
92.
92.
94.
94.
95.
96.
DIA
fTN)
0. 197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0.197
0. 197
0.197
0.197
0.197
TEMP
(DF)
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
65.
VEL
(FPS)
56. 183
56.183
55.351
54.930
62.815
59.786
71.457
69.815
63.549
66.755
65.350
64.994
55. 351
57.003
71.457
71.457
.860
854
--
«• M
111.0
106.4
1.06.0
105.6
102.2
150.8
101.7
107.8
130.5
97.6
103.5
104.6
108.7
103.4
105.2
107.5
-------
- YORK RESEARCH CORPORATION JOB NUMBER: 9517-17
i ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION; CLIMAX MOLY
UNIT TESTED: PER8LE SCREEN
I STACK
i STACK
t ' •
NUMBER: TP2 -.'•.. -i*;:, ;.: : .
LOCATION:: BUCKET ELEVATOR
TEST NUMBER: i
DATE: AUG 29,79
CONDITIONS: NDP
MAL
: . AMBIENT. TEMP-DEGE:. 70
EXHAUST BAR. .PRESS - IN HG:21.60
ANDERSEN PARTICLE SIZING
STAGE
1
2
3
4
5 .. •
6
7
8
_FJLTER
STACK
DIAMETER WEIGHT
(MICRONS) fMILLIGRAMS)
> 13.48 3.25
13. 48-8. 41 2.15
•:;>..'-.-.-:'-:--::.'--'-'-.-^.; :,:/•.•.";.:.
ft. 4 1-5. 69 2.32
5.69-3.87 1.42
3. .87-2.48 ;;,;.;;•:;•,;. 1 .71 •, ,. •
2.48-1.23 1.57
1.23-0.75 0.84
0.75-0.49: :v :. 0.65
< 0.49 0.92
TEMP.CDEG.E) . . . . 70.0
STACK PRESSURE(JN.HG) . . 21.33
GAS ANALYSIS (DRY PERCENT)
C02 ..... 0.00
CO 0.00
N2 . . .- . . 79.10
02 20.90
H2(); . ... . 2.00
% PER CUM% GR/SCFD
STAGE
-------
YORK RESEARCH CORPORATION JOB NUMBER
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT. 06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MQLY
UNIT TESTED: PEBBLE SCREEN
STACK NUMBER: TP2
: STACK LOCATION: BUCKET ELEVATOR
: 9517-17
TEST NUMBER: 3
DATE: AUG 29,79
CONDITIONS: NORMAL
AMBIENT TEMP-OEG
EXHAUST BAR. PRESS - IN
Fi 70
HG:21.60
ANDERSEN PARTICLE SIZING
DIAMETER WEIGHT
. S T A GE . _ . JLMjLCRQrt 5) f MILLIGRAMS)
1 > 13.23 8.50
7 13.23-8.75 2.66
3 B. 25-5. 59 3.73
4 5.59-3.80 2.15
5 3.80-2.43 2.24
6 2.43-1.21 1 .65
7 1.21-0.74 1.03
fl 0.74-0.48 0.37
FILTER < 0.48 0.27
STACK TEMP. ( DEC. F }. . . . 70.0
STACK PRESSUREf IM.HG) . .21.33
GAS ANALYSIS (DRY PERCENT)
C02 0.00
CO 0.00
ivi 2 79.10
02 20.90
H20 ..... 2.00
• •••'•'. •••.;•• .• ••• "••.-. '
% PER CUM% GR/SCFO MG/NCMD
STAGE
-------
: ONE
YORK RESEARCH CORPORATION
RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MflLY
UNIT TESTED: PEBBLE SCREEN
JOB NUMBER:.
9517-17
TEST NUMBER: 2
DATE: AUG 29,79
CONDITIONS: NORMAL
: STACK NUMBER: TP2 AMRT
j STACK LOCATION: Ri.iCK.ET ELEVATOR EXHAUST BAP.
i ; ' • •• . .:> . ,.;• ' .... .. . ••-..•••.. ••"• -;•.•.'•
ENT TEMP-DEG F: 70
; PRESS - IN HG:21 .60
ANDERSEN PARTICLE SIZING
: , DIAMETER
STAGE (MICRONS) 1
1
2
3__
4
5
6
7
> 14.48
14.48-9.03
9.03-6.12
6.12-4. ifi
4.16-2.67
2.67-1.33
1.33-0.81
•;••,- ..;..:••..••• : , . : ••'•'; . •-••• ,;. •- .... . . . ••:/••< ;':. ,'. ' •••
WEIGHT % PER CUH% GR/SCFD MG/NCMD
fMTLLlGPAMS) STAGE
-------
TP-2A Total Scrubber Inlet
-------
YORK RESEARCH CORPORATION
ONE: RESEARCH DRIVE. STAFFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLAMT LOCATION: CLIMAX
U'VTT TESTED: PEBBLE SCREEN
TP2A
PARTICIPATE SUMMARY IN ENGLISH UNITS
DESCRIPTION
UNITS
TP2A-1
TP2A-2
TP2A-3
AVERAGE
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE TN.HG
STACK PRESSURE. A«?S. TN.HG
STACK AREA SO. FT
NFT TIME OF RUN M.TN
PERCENT ISOKINETTC
GAS DATA
AVG STACK GAS VELOCITY EPS
AVG STACK TEMPERATURE DEG.F
ACTUAL STACK FLOWRATE ACFM
STK FLOWRATE.ORY.STD OSCFM
MOLECULAR WT-DRY STK GAS
MOLECULAR WT-STK GAS
MOLE FRACTION DRY GAS
GAS ANALYSIS (DRY PERCENT BAS
CARBON OIOXIDF
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE 6Y VOL
SAMPLE COLLECTION DATA
TOTAL H20 COLLECTED ML
VOL H20 VAPOR-STD COND SCF
VOL DRY GAS-METER COND DEF
VOL DRY GAS-STD COND DSCF
AVG GAS METER TEMP DEG.F
AVG ORIF PRES DROP IN.H20
PARTICIPATE HEIGHT DATA
NET WEIGHT PARTIAL MG
MET WEIGHT TOTAL «G
PARTICULATE EMISSIONS
PARTIAL
GRAINS PER SCFD
GRAINS PER SCFD iai2%C02
GRAINS PER ACF
POUNDS PER HOUR
POUNDS PER PROCESS UNIT
TOTAL
GRAINS PER SCFO
GRAINS PER STFO 012%C02
GRAINS PER ACF
POUNDS PER H.OLIR
POUNDS PER PROCESS UNIT
AUG 29,79
21 .60
21 .29
1.23
96.0
104.1
81.242
79.6
5981 .
4120.
28.82
28.67
0.986
IS)
0.0
20.5
0.0
79.5
1.4
10.1
0.48
48.24
33.37
94.2
0.592
0.00
78.63
o.ooooo
0.00000
0.00000
0.00
0.00000
0.03629
0.00000
0.02500
1.28
0.00000
AUG 29,79
21 .60
21.29
1 .23
96.0
106.5
76.375
80.0
5623.
3843.
28.82
28.59
0.979
0.0
20.5
0.0
79.5
2.1
14.6
O.fe9
47.08
31.81
107.2
0.508
0.00
117.98
0.00000
0.00000
0.00000
0.00
0.00000
0.0571 1
o.ooooo
0.03903
1.88
0.00000
AUG 30,79
21 .60
21.29
1.23
96.0
102.0
75.975
74.0
5593.
3916.
28.92
28.73
0.991
0.0
20.5
0.0
79.5
0.9
5.7
0.27
44.35
31.07
87.1
0.508
0.00
174.52
0.00000
0.00000
0.00000
0.00
0.00000
0.08651
0.00000
0.06057
2.90
0.00000
104.2
77.864
77.8
5732.
3960.
0.0
20.5
0.0
79.5
1.5
0.00
123.71
o.ooooo
o.ooooo
o.ooooo
0.00
0.00000
0.05997
o.ooooo
0.04153
2.02
0.00000
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE, STAMEORO, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PEBBLE SCREEN TP2A
JOB NUMBER: 9517-17
PARTICIPATE SUMMARY IN METRIC UNITS
DESCRIPTION
UNITS
TP2A-1
TP2A-2
TP2A-3
AVERAGE
GENERAL DATA
DATE OE RUN
BAROMETRIC PRESSURE
STACK PRESSURE. ABS
STACK AREA
NET TIME OF RUN
PERCENT ISOKINETTC
GAS DATA
AVG STACK GAS VELOC
AVG STACK TEMPERATURE
ACTUAL STACK ELOV
STK FLOWRATE,DRY,STD
MOLECULAR -/IT-OR/, s
MOLECULAR ^T-STK G
MOLE FRACTION DRY
GAS ANSLYSIS (D.RY
CAPBQN DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD
VOL DRY GAS-METER
VOL DRY GAS-STD COMD
AVG GAS METER TEMP
AVG ORIF PRES DROP
PARTICIPATE WEIGHT
NET WEIGHT PARTIAL
NET WEIGHT TOTAL
PARTICIPATE EMISSIONS
PARTIAL
MG/NORMALIZED CU.METERS
MG/NORM. CU.M ai2% C02
MG/ACTUAL cu. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
TOTAL
MG/NORMALIZEO CU.METERS
MG/NORM. CU.M 012% C02
MG/ACTUAL cu. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
AUG
MM.HG
MM.HG
M2
MIN
ITY M/S
RE DEG.C
TE AM3/M
D DNM3/M
K GAS
S
AS
ERCENT BASIS)
A T A
A J A
ML
OMD MM3
OND DM3
D DNM3
DEG.C
MM .H20
DATA
MG
MG
29.79
548.64
540.80
0.1 14
96.0
104.1
24.762
26.4
169.
117.
28.82
28.67
0.986
0.0
20.5
0.0
79.5
1.4
1.0.1
0.01
1.37
0.94
34.5
15.039
0.00
78.63
AUG 29,79
548.64
540.80
0.114
96.0
106.5
23.279
26.7
159.
109.
28.82
28.59
0.979
0.0
20.5
0.0
79.5
2.1
14.6
0.02
1.33
0.90
41.8
12.912
0.00
117.98
AUG 30,79
548.64
540.90
0.114
96.0
102.0
23.157
23.3
158.
Ill .
28.82
28.73
0.991
0.0
20.5
0.0
79.5
0.9
5.7
o.ot
1.26
0.88
30.6
12.901
o.oo
174.52
104.2
23.733
25.5
162.
112.
0.0
20.5
o.o
79.5
1.5
0.00
123.71
0.00
0.00
0.00
0.00
.00000
83.05
0.00
57.22
0.58
.00000
0.00
0.00
o.oo
0.00
o.ooooo
130.70
0.00
89.32
0.85
0.00000
0.00
0.00
0.00
o.oo
0.00000
197.97
0.00
1 38.60
1.32
0.00000
0.00
0.00
0.00
o.oo
0.00000
137.24
a. oo
95.04
0.92
0.00000
-------
ONE
YORK RESEARCH CORPORATION
RESEARCH DRIVE', STAFFORD, CONNECTICUT
JOB NUMBER: 9517-17
Ofi906
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
LIMIT TESTED: PEBBLE SCREEN TP2A
TEST NUMBER: TP2A-1
DATE: AUG 29,79
TEST COND: NORMAL
DUCT NUMBER: TP2A BAR. PRESS-IN HG: 21
DUCT AREA: 1.23SQ.FT. ,15" 1.0. PITOT TUBF, FACTOR: 0
DUCT LOCATION: TOTAL SCRUBBER INLET TIME TEST STARTED: i
FILTER NUMBERS: 02880
SAMPLE ELAP SAMPLE PITOT ORIFICE MRTERTEMP NOZ STACK STACK
POINT TIME VOLUME RQG RDG (DEG.F) DIA TEMP VEL
(MIN) (DCF) CINH20MINH20) IN OUT (IN) (OF) (FPS)
START
1
2
3
4
5
f>
7
8
9
10
1 1
12
START
1
2
3
4
5
f>
7
R
9
10
1 1
12
0.0
4.0
8.0
12.0
16.0
20.0
24.0
28.0
32.0
36.0
40.0
44.0
48.0
48.0
52.0
56.0
60.0
64.0
68.0
72.0
76.0
80.0
84.0
88.0
92.0
96.0
845
847
849
851
853
855
857
859
861
862
863
865
867
867
869
871
874
876
879
881
883
885
887
889
891
893
.254
.490
.860
.360
.530
.770
.000
.500
.020
.470
.080
.500
.032
.032
.540
.990
.470
.900
.310
.500
.530
.450
.370
.350
.420
.494
1 .900
1 .900
2.500
1 .800
1.700
1 .300
0.820
0.620
0.620
0.700
0.620
0.670
2.000
2.000
2.000
1.900
1 .800
1.600
1 .300
1 .1 00
1.100
1 .200
1 .300
1.300
0.810
0.800
1.100
0.770
0.670
0.550
0.340
0.260
0.260
0.290
0.270
0.280
0.840
0.840
0.840
0.800
0.780
0.640
0.550
0.460
0.460
0.500
0.550
0.550
78.
84.
88.
80.
84.
88.
92.
93.
94.
96.
98.
99.
100.
103.
106.
1 08.
109.
1 10.
1 10.
110.
110.
110.
111.
112.
79.
79.
79.
81.
81 .
81.
83.
83.
85.
86.
88.
89.
90.
91.
93.
94.
95.
96.
97.
98.
99.
100.
100.
101.
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0. 135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
80.
75.
75.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
96.420
95.973
110.088
93.848
91.204
79.756
63.343
55.079
55.079
58.525
55.079
57.257
98.925
98.925
98.925
96.420
93.848
88.481
79.756
73.365
73.365
76.627
79.756
79.756
.60
.870
220
%t
100.6
105.5
58.1
99.9
105.7
66.1
163.1
117.4
111 .7
44.1
185.3
112.6
106.7
103.9
104.7
105.0
106.8
102.7
105.5
108.3
108.2
106.8
107.2
107.2
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE*. STAMFORD, CONNECTICUT
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UMIT TESTED: PEBBLE SCREEN TP2A
JOB NUMBER: 9517-17
06906
TEST NUMBER: TP2A-2
DATE: AUG 29,79
TEST COMD: NORMAL
DUCT NUMBER: TP2& BAR. PRESS-IN HG: 21
DUCT AREA: 1 .23SO.FT. , IS" I.D. PITOT TUBE FACTOR: 0
DUCT LOCATION: TOTAL SCRUBBER INLET TIME TEST STARTED: 1
FILTER NUMBERS: 02370
SAMPLE ELAP SAMPLE PTTOT ORIEICE METERTEMP NOZ STACK STACK
POINT TIME VOLUME RDG RDG (DEG.F) DIA TEMP VEL
(MIN) (QCF) (IMH20) (INH20) IN OUT (IN) (DF) (FPS)
START
1
7.
3
4
S
6
7
8
9
10
11
12
START
8-1
7
3
4
5
6
7
8
9
10
It
12
0.0
4.0
8.0
12.0
16.0
20.0
24.0
28.0
32.0
36.0
40.0
44.0
48.0
48.0
52.0
56.0
60.0
64.0
68.0
72.0
76.0
80.0
84.0
88.0
92.0
96.0
894.
896.
898.
901.
903.
905.
907.
909.
910.
912.
913.
915.
916.
917.
919.
921.
923.
925.
928.
929.
931.
933.
935.
937.
939.
941.
038
410
840
100
320
500
480
120
660
140
670
180
728
000
020
240
490
760
900
900
700
540
390
250
200
394
1 .900
1 .900
1.700
1 .600
1.500
1 .200
0.770
0.660
0.630
0.650
0.640
0.700
1.500
1 .600
1 .600
1 .600
1 .400
1.200
0.970
1.000
1 .000
1.000
1 .100
1 .600
0.800
0.800
0.660
0.640
0.620
0.500
0.330
0.280
0.260
0.270
0.270
0.290
0.620
0.670
0.670
0.670
0.590
0.500
0.400
0.420
0.420
0.420
0.460
0.640
96.
104.
110.
111.
113.
113.
113.
111.
111.
11 I.
111.
111.
110.
t 12.
114.
115.
115.
116.
115.
115.
115.
115.
115.
115.
96.
96.
97.
98.
99.
100.
101.
101 .
101.
102.
102.
103.
104.
104.
104.
105.
105.
105.
105.
105.
106.
106.
106.
106.
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
0.135
80.
80.
80.
80.
80.
80.
80.
HO.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
80.
96.550
96.550
91.327
88.601
85.787
76.730
61.464
56.905
55.596
56.472
56.036
58.604
85.787
88.601
88.601
88.601
82.878
76.730
68.986
70.045
70.045
70.045
73.464
88.601
.60
.870
548
%I
«• «•
103.9
105.7
103.3
104.4
105.6
107.1
110.6
112.3
110.5
112.3
111.7
109.4
97.7
103.8
105.0
105.7
156.3
53.7
107.6
108.3
108.8
109.4
109.4
102.1
-------
ONE
YORK RESEARCH CORPORATION
RESEARCH DRIVE'. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT! EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PEBBLE SCREEN TP2A
DUCT NUMBER: TP2A
DUCT AREA: 1 .23SO.FT..15" T.D.
DUCT LOCATION: TOTAL SCRUBBER INLET
EILTER NUMBERS: 02590
TEST NUMBER: TP2A-3
DATE: AUG 30,79
TEST CQND: NORMAL
BAR. f
PTTOT
TIME 1
SAMPLE ELAP SAMPLE PITOT ORIFICE METERTEMP NQZ
POINT TIME VOLUME RDG RDG (DEG.F) OIA
fMIN) CDCF) (INH20)(INH20) IN OUT (IN)
START
A-l
2
3
4
5
6
7
8
q
10
11
12
START
fl-1
2
3
4
5
6
7
8
9
10
1 1
12
0.0
4.0
9.0
12.0
16.0
20.0
24.0
28.0
32.0
36.0
40.0
44.0
48.0
48.0
52.0
56.0
60.0
64.0
68.0
72.0
76.0
80.0
84.0
88.0
92.0
96.0
941 ,
944
946,
948,
903
100
460
650
950.690
952.850
954,
955
957,
958
960
961
,930
,741
,230
,790
,260
,710
962.134
963.660
965.620
967.800
969.970
972,
974,
976,
978,
979,
981,
983,
985,
140
220
110
000
,880
830
700
850
987.683
1.900
1 .900
1 .800
1.600
1 .400
1.400
0.820
0.680
0.690
0.620
0.620
0.550
1 .600
1.600
1 .600
1.600
1.400
1.100
1 .100
1.100
1 .200
1.100
1 .100
1.100
0.800
0.800
0.680
0.640
0.590
0.590
0.340
0.280
0.290
0.270
0.270
0.230
0.640
0.640
0.640
0.640
0.590
0.460
0.460
0.460
0.500
0.460
0.460
0.460
73.
75.
80.
83.
86.
89.
90.
92.
85.
88.
90.
90.
93.
94.
98.
99.
100.
101.
101.
101.
102.
102.
96.
98.
72.
72.
72.
73.
74.
75.
77.
79.
80.
80.
81.
82.
85.
85.
86.
87.
88.
8<».
90.
91.
91.
92.
92.
92.
135
135
135
135
135
135
135
1 35
135
135
135
0.135
135
135
135
135
135
135
135
135
135
135
135
0.135
RESS-
TUBE
IN HG: 21
FACTOR: 0
EST STARTED:
STACK
TEMP
(DF)
80.
80.
80.
70.
70.
70.
70.
70.
75.
75.
75.
75.
75.
75.
70.
75.
70.
70.
75.
75.
75.
75.
75.
75.
STACK
VEL
(FPS)
96.320
96.320
93.751
87.567
81.911
81.911
62.688
57.086
57.775
54.766
54.766
51.582
97.979
87.979
87.567
87.979
81.911
72.606
72.948
72.948
76.192
72.948
72.948
72.948
.60
.870
858
%I
--
"•
104.0
106.7
101 .2
98.7
111.3
106.7
54.2
109.8
114.3
113.4
111.5
34.6
93.4
103.7
102.3
102.6
104.4
106.8
107.2
106.6
105.8
105.8
122.3
104.1
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
JOB NUMBER:: 9517-17
CLIENT: EPA
PLANT LOCATION: CLT«AX MQLY
...UN I T_T ES.T ED..: _._P E.B 6.LE_SCfi£EJi
STACK NUMBER: TP2A :
STACK;:: LOCATION r ;TO;TAL SCRUBBER-INLET
TEST NUMBER: i
DATE: AUG 30,79
J1Q.N.Q.ITI.QN.S :, .NORM A L .
AMBIENT TEMP-DEC. F: 70
- INv HG:21.60
ANDERSEN PARTICLE SIZING
DIAMETER WEIGHT % PER CUM% GR/SCFO MG/NCMD
STAGE (Nl.T.CRpN5.I__(LM.TL.L.TGRAMS>_. ST AGE__ 11.47
?. It. 47 -7. 15
3 7.15-4.83
4 4.83-3.29
5 3.29-2.10
6 . 2..10-1.04_
7 1.04-0.63
2.60
X 0.72 .,
0.62
0.01
0.15
0.20
0.05
59.77
16.55
14.25
0.23
3.45
4...60:
1.15
40.23
23.68
9.43
9.20
5.75
1.15
0.001314
0.000364
0.000313
0.000005
0.000076
0.000101
0.000025
3.01
0.83
0.72
0.01
0.17
0.23
0.06
8 0..63:-0.37: ;;>: - 0.00 I ; : >0.00;r ^^ -0:.00 0.000000 0.0.0
FILTER < 0.37 0.00 0.00 -0.00 0.000000 0_._0.0_
STACK TEMP.(OEG.F).
70.0
' STACK PRESSURECI^f.HG). . . 21.29
i\ GAS ANALYSIS (DRY;; PERCENT)
: • C02 . . . . . 0.00
CO 0.00
N2 79.10
02 20.90
H20
SAMPLING RATECACFM) . .
CSCFMO) . .
_0_. JJ _0_
0.509
0.014
TMPACTOR. 'TEMP. (PEG. F) . . _ 10..Jl_
PARTICLE DENSTTY(GM/CC) . 1.00
TEST TIME (WIN.) ..... 60.00
TOTAL WEIGHT (MG) . . . . _ 4_..33__
2.00 : TOTAL GR/SCFD . . ...... . . 0.00220
TOTAL MG/NCMD
5.03
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
; CLIENT: EPA
PLANT LOCATION: CLIMAX
' . UNIT TESTED; PERRLE SCREEN
'. STACK NUMBER: TP2A
J| STACK LOCATION; TOTAL SCRUBBER INLET
91 . • '
TEST NUMBER: 2
DATE: A!!G 30,79
.t ._N 0 R_«LA, L
AMBIENT TEMP-OEG E: 70
8AR. PRESS -.IN HG:21.6Q
ANDERSEN PARTICLE SIZING
DIAMETER WEIGHT % PER CUM% GR/SCFD MG/NCMD
STAGE ..( M_I C RONS) fMIL L_I G.RA JiS I S T_A G E 11 .47
1 1.47-7.15
7.15-4.83
4.83-3.29
3.29-2.10
2.10-1.04
1.04-0.63
15
1
1
0
0
0
0
.86
.09
.24
.54
.89
.52
.23
76
5
6
2
4
2
1
.99
.29
.02
.62
.32
.52
.12
23.
17,
11 .
9.
. 4.
2.
01
72
70
08
76
23
0.
0.
0.
o.
0.
0.
0.
006245
000429
000488
000213
000350
000205
000091
14.
0.
1..
0.
0.
0.
0.
29
98.
12
49
80
47
21
8 0.63-0.37
FILTER <_o.37
0.14 0.68 1.12
JL.PJ A..44 .0._44_
0.000055 0.13
_0 . 0 0 0 0 3 5. .0. .08..
STACK TEHP.(DEG.F).
STACK PRESSURE(IN.HG) . . 21.29
'••< GAS ANALYSIS (DRY PERCENT)
_CO_2
CO .
N2 .
02 .
..»_*_. CL..PP_
. . . 0.00
. . . 79.10
. . . 20.90
H20 ....... 2.00
LNG_JLA TE.LA .C_F *L)._ ._._ .
(SCFVD). . .
(NCMMD). . .
_.. IMPACT O.R_ T E JSJ P ...( 0 E G . F. ) . . . ..
PARTICLE D5NSITYCGM/CC) .
TEST TIME (MIN) .....
___TO_T AJL_1V£.I.GJ±T__(^ G I_ .__. _^_. .
0.509
0.014
..... _. 7 0. . D
1.00
77.00
2.Q...6 0_
TOTAL GR/SCFD ....... 0.00811
TOTAL MG/NCMD ....... 18.57
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MQLY
LIMIT, TESTED: .PEBBt,F!._SCRE_EN
STACK NUMBER: TP2A . .. :.:
STACK LOCATION::TOTAL SCRUBBER INLET
TEST NUMBER: 3
DATE: AUG 30,79
CONQ.T.TIQNS :. .NORMAL
•AMBIENT TEMP-QEG F: 70
B A R . : P R ESS .-•', IN H G : 21 .60
ANDERSEN PARTICLE SIZING
DIAMETER WEIGHT % PEP CUM% GR/SCED MG/MCMD
STAGE (M_ICROrtS_l .(.•ULLJ.GR AMS )_ . ST. AGE__ 10.95
10.95-6.82
..._.._ 3....
4
4.61-3.13
5 3.13-2.00
6 2_.jn_Oj^ Q...OLQ. 0..QO.OOO_Q Q. 00
STACK TEMP. COKG.F) .._. . . 70.0
•'•'• STACK PRESSU«ECIM.HG) . .,21.29
;" GAS ANALYSIS (DRY PERCENT) ; :
G02 . . . . . 0.00
CO
02
0.00
79.10
-20.90
H20 .;-. . ... .2.00
SAMPLING RATE(ACFM) . . . 0_.8_0_Q
:,:• ••-'../ . (SCFMO). . ... 0.558
v': : ;. (NCMMD). . . 0.016
TMPACTOR TEMP.fDEG.FL_c._. 7..0..D
PARTICLE DENSITYCGM/CC) . 1.00
TEST TIME (MIN) 46.00
TOTAL GR/SCFD .., . ., . .... . 0.00191
TOTAL MG/NCMD . . . . .. . 4.38
-------
TP-3 Scrubber Outlet
-------
YORK RESEARCH CORPORATION
ONE: RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION; CLIMAX MQLY
UNIT TESTED: PEBBLE SCREEN TP3
JOB NUMBER: 9517-17
PARTICULATE SUMMARY IN METRIC UNITS
UNITS
DESCRIPTION
GENERAL DATA
DATE Of RUN
BAROMETRIC PRESSURE
STACK PRESSURE. ABS
STACK AREA
NET TIME OF RUN
PERCENT ISOKINETIC
GAS DATA
AVG STACK GAS VELOC
AVG STACK TEMPERATURE
ACTUAL STACK FLOWRATF.
STK FLOWRATE»DRY,STD
MOLECULAR WT-DRY S
MOLECULAR WT-STK G
MOLE FRACTION DRY
GAS ANALYSIS (DRY
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION
TOTAL H20 COLLECTED
VOL H20 VAPOR-STD
VOL DRY GAS-METER
VOL DRY GAS-STD CO
AVG GAS METER TEMP
AVG ORTF PRES DROP
PARTTCULATE WEIGHT
NET WEIGHT PARTIAL
MET WEIGHT TOTAL
PARTICULATE EMISSIONS
PARTIAL
MG/NORMALIZED CU.METERS
MG/NORM. CU.M 012% C02
MG/ACTUAL cu. METERS
KILOGRAMS/HOUR
KILOGM PER PROCESS UNIT
TOTAL
MG/NORMALlZED CU.METERS
MG/NORM. CU.M (312% C02
MG/ACTUAL cu. METERS
KILOGRAMS/HOUR
K.TLOGM PEK PROCESS UNIT
TP3-1
TP3-2
TP3-3
AVERAGE
AUG
MM.HG
M M . H G
M2
MIN
TTY M/S
RE DEG.C
TE AM3/M
D DNM3/M
K GAS
S
AS
EPCENT BASIS)
ATA
A J A
ML
OND NM3
OND DM1
D DNM3
DEG.C
MM.H20
DATA
MG
MG
29,79
548.64
543.97
0.271
1 12.0
96.5
1 2.287
12.8
200.
1 44.
28.82
28.61
0.981
0.0
20.5
0.0
79.5
1.9
16.3
0.02
1.62
l.ll
38.0
20.665
0.00
24.31
AUG 29,79
548.64
547.39
0.271
112.0
96.7
14.069
12.7
229.
166.
28.82
28.60
0.980
0.0
20.5
0.0
79.5
2.0
19.7
0.03
1.90
1.28
43.4
25.223
0.00
14.54
AUG 30,79
548.64
547.67
0.271
112.0
97.6
15.025
10.6
244.
177.
28.82
28.50
0.971
0.0
20.5
0.0
79.5
2.9
30.9
0.04
1.96
1.38
30.8
26.661
0.00
18.36
96.9
13.794
12.0
224.
163.
0.0
20.5
0.0
79.5
2.3
0.00
19.07
o.oo
0.00
0.00
0.00
00000
21.88
0.00
15. SI
0.19
00000
0.00
0.00
0.00
o.oo
0.00000
11.35
0.00
8.24
0.11
o.ooooo
0.00
0.00
0.00
0.00
0.00000
13.31
0.00
9.66
0.14
0.00000
0.00
0.00
1 0.00
0.00
0.00000
15.51
0.00
11.23
0.15
0.0^000
-------
YORK RESEARCH CORPORATION
OMF RESEARCH DRIVE. STAMFORD. CONNECTICUT 06906
CLIENT: EPA
PLANT LOCATION: CLIMAX MOLY
UNIT TESTED: PEBBLE SCREE" TP3
JOB NUMBER: 9517-17
PARTICULATE SUMMARY IN ENGLISH UNITS
DESCRIPTION
UNITS
TP3-1
TP3-2
TP3-3
AVERAGE
GENERAL DATA
DATE OF RUN
BAROMETRIC PRESSURE IN.HG
STACK PRESSURE. ARS. IN.HG
STACK AREA SO. FT
NET TIME OF RUN MIM
PERCENT ISOKINETIC
GAS DATA
AVG STACK GAS VELOCITY EPS
AVG STACK TEMPERATURE DEG.F
ACTUAL STACK FLOWRATE ACFM
STK FLOWRATE, DRY ,STD DSCFM
MOLECULAR WT-DRY STK GAS
MOLECULAR HT-STK GAS
MOLE FRACTION DRY GAS
GAS ANALYSIS (DRY PERCENT BAS
CARBON DIOXIDE
OXYGEN
CARBON MONOXIDE
NITROGEN
MOISTURE BY VOL
SAMPLE COLLECTION DATA
TOTAL H20 COLLECTED ML
VOL H20 VAPOR-STD COND SCF
VOL DRY GAS-METER CONO DEF
VOL DRY GAS-STD COND DSCF
AVG GAS METER TEMp DEG.F
AVG ORIF PRES DROP TN.H20
PARTTCULATE HEIGHT DATA
NET WEIGHT PARTIAL MG
NET WEIGHT TOTAL MG
PARTICULATE EMISSIONS
PARTIAL
GRAINS PER SCFD
GRAINS PER SCFD 812%C02
GRAINS PE.R ACF
POUNDS PER HOUR
POUNDS PER PROCESS UNIT
TOTAL
GRAINS PER SCFD
GRAINS PER SCFD P12%C02
GRAINS PER ACF
POUNDS PER HOUR
POUNDS PER PROCESS UNIT
AUG 29,79
21.60
21 .42
2.92
112.0
96.5
40.31 1
55.0
7055.
5095.
28.82
28.61
0.981
IS)
0.0
20.5
0.0
79.5
1.9
16.3
0.77
57.19
39.15
100.4
0.814
0.00
24.31
0.00000
o.ooooo
0.00000
o.oo
0.00000
0.00956
o.ooooo
0.00691
0.42
o.ooooo
AUG 29,79
21.60
21.55
2.92
112.0
96.7
46.158
54.8
8078.
5868.
28.82
28.60
0.980
0.0
20.5
0.0
79.5
2.0
19.7
0.93
67.08
45.15
110.2
0.993
0.00
14.54
0.00000
0.00000
0.00000
0.00
o.ooooo
0.00496
o.ooooo
0.00360
0.25
0.00000
AUG 30,79
21.60
21.56
2.92
112.0
97.6
49.296
51.1
8628.
6253.
28.82
28.50
0.971
0.0
20.5
0.0
79.5
2.9
30.9
1.46
69.32
48.60
87.5
1.050
0.00
18.36
0.00000
0.00000
0.00000
0.00
0.00000
0.00582
o.ooooo
0.00422
0.31
0.00000
96,9
45.255
53.6
7921.
5740.
0.0
20.5
0.0
79.5
2.3
0.00
19.07
0.00000
0.00000
0.00000
0.00
o.ooooo
0.00678
o.ooooo
0.00491
0.33
0.00000
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE', STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION; CLIMAX MQLY
UNIT TESTED: PEBBLE SCREEN Tp-3
DUCT NUMBER: Tp-3
DUCT AREA: 2.92SO.FT.,23.125" I.D.
DUCT LOCATION: .SCRUBBER OUTLET
FILTER NUMBERS: 02770
TEST NUMBER: TP3-1
DATE: AUG 29,79
TEST COVD: NORMAL
BAR. PRESS-IN MCI: 21.eo
PITOT TUBE FACTOR: 0.910
TIME TEST STARTED: 1220
SAMPLE ELAP SAMPLE PTTOT ORIFICE METERTEMP NQZ
POINT TIME VOLUME RDG RDG (DEG.F) DIA
(DCF) (INH20)(INH20) IN OUT (IN)
START
A-l
2
3
4
5
6
7
S
9
10
1 1
12
1 3
14
START
B-t
2
3
4
5
6
7
8
9
10
11
12
1 3
14
0.0
4.0
fl.O
12.0
16.0
20.0
24.0
78.0
32.0
36.0
40.0
44.0
48.0
52.0
56.0
56.0
60.0
64.0
68.0
72.0
76.0
90.0
84.0
88.0
92.0
96.0
100.0
104.0
108.0
112.0
79.630
82.780
85.990
89.120
92.240
95.230
98.275
99.440
99.440
99.440
100.920
102.815
104.745
106.800
108.852
8.852
12.010
15.255
18.570
22.050
25.500
28.740'
30.920
30.920
30.920
30.920
30.920
32.910
34.930
36.819
0.840
0.890
0.820
0.820
0.7/lQ
0.740
0.1 00
0.000
0.000
0.170
0.260
0.260
0.300
0.300
0.760
0.810
0.850
0.960
0.930
0.770
0.300
0.000
0.000
0.000
0.000
0.260
0.280
0.240
1,
1,
1 ,
1,
1 ,
1,
0,
0,
0,
0,
0,
0,
0,
650
750
600
600
450
450
190
000
000
330
510
510
580
0.580
1.500
0.160
1 .670
1 .850
1 .800
1.500
0.580
0.000
0.000
0.000
0.000
0.500
0.550
0.470
76.
80.
87.
92.
96.
98.
92.
94.
94.
94.
98.
101.
104.
105.
106.
1 10.
114.
1 16.
116.
118.
116.
1 16.
112.
112.
112.
1 12.
112.
112.
74.
74.
76.
76.
78.
80.
94.
96.
96.
96.
96.
98.
100.
102.
101 .
102.
104.
106.
106.
108.
108.
108.
108.
108.
108.
108.
108.
108.
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
195
195
195
195
195
195
195
195
195
1«5
195
195
195
195
STACK
TEMP
(DF)
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
STACK
VEL
(FPS)
65.360
67.278
64.578
64.578
61.347
61.347
22.551
0.000
0.000
29.404
36.36.3
36.363
39.060
39.060
62.170
64.183
65.748
69.873
69.773
62.573
39.060
0.000
0.000
0.000
0.000
36.363
37.736
34.937
%I
--
— —
96.3
95.0
95.7
95.0
95.3
96.7
99.5
0.0
0.0
96.6
99.7
101 . I
99.8
99.4
96.4
95.1
94.9
93.4
94.1
96.7
104.1
0.0
0.0
0.0
0.0
102.4
100.2
101.2
-------
ONE
YORK RESEARCH CORPORATION
RESEARCH DRIVE'. STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MQLY
UNIT TESTED: PEBBLE SCREEN TP3
DUCT NUMBER: TP3
DUCT AREA: 2.92SO.FT.,23.125" ID
DUCT LOCATION: SCRUBBER OUTLET
FILTER NUMBERS: 02340
TEST NUMBER: TP3-2
DATE: AUG 29.79
TEST COND: NORMAL
BAR. PRESS-IN HG: 21.60
PITOT TUBE FACTOR: 0.910
TIME TEST STARTED: 1546
SAMPLE
POINT
--
START
A-l
2
3
4
5
6
7
8
9
10
11
12
13
14
START
8-1
2
3
4
5
6
7
8
9
10
11 1
12 1
13 1
14 1
ELAP
TIME
fMIN)
o.o
4.0
8.0
12.0
16.0
20.0
24.0
28.0
32.0
36.0
40.0
44.0
48.0
52.0
56.0
56.0
60.0
64.0
68.0
72.0
76.0
80.0
84.0
88.0
92.0
96.0
00.0
04.0
08.0
12.0
SAMPLE
VOLUME
(DCF)
41.668
45.060
48.4^0
52.090
55.600
58.790
61.530
61.530
61.530
63.300
65.290
67.515
69.795
71.870
73.939
73.940
77.170
80.520
83.870
87.400
90.950
93.980
96.120
96.120
97.650
99.475
101.510
103.930
106.340
108.745
PITOT
RDG
(TNH20)
0.950
0.920
1 .000
0.940
0.780
0.550
0.000
0.000
0.150
0.290
0.370
0.370
0.300
0.290
0.850
0.850
0.900
0.950
0.950
0.700
0.300
• o.ooo
0.1 30
0.230
0.280
0.420
0.420
0.400
ORIFICE
RDC
CIMH20)
1.850
1 .800
1 .950
1.850
1.500
1.075
0.000
0.000
0.290
0.570
0.720
0.720
0.580
0.570
1.650
1 .650
1.750
1.850
1.850
1.350
0.580
0.000
0.250
0.450
0.550
0.810
0.810
0.780
METERTEMP NOZ
(DEG.F)
IN
98.
104.
1 10.
113.
116.
116.
1 1.4.
114.
114.
112.
112.
112.
1 12.
1 12.
Ill .
114.
116.
1 16.
118.
118.
118.
118.
114.
11.4.
U4.
114.
1 14.
114.
OUT
102.
102.
102.
102.
104.
104.
1^4.
104.
104.
106.
106.
106.
106.
108.
109.
109.
1 10.
110.
110.
110.
no.
110.
110.
1 10.
110.
110.
110.
110.
DTA
(IN)
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
0.195
STACK
TEMP
(DF)
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
50.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
55.
STACK %I
VEL
(EPS)
69.
68.
71.
68.
62.
52.
0.
0.
27.
38.
43.
43.
38.
38.
65.
65.
67.
69.
69.
59.
38.
0.
25.
34.
37.
46.
46.
44.
303
200
103
937
797
732
ooo
000
538
290
250
250
945
290
554
235
454
303
.303
489
945
000
637
100
624
080
080
970
93.1
95.1
95.3
95.6
94.5
97.2
0.0
0.0
119.7
96.9
95.9
98.3
99.3
100.6
92.0
94.7
92.3
94.7
95.1
94.4
101.6
0.0
110.6
99.2
100.3
97.5
97.1
99.3
-------
YORK RESEARCH CORPORATION
ONE RESEARCH DRIVE1, STAMFORD, CONNECTICUT 06906
JOB NUMBER: 9517-17
CLIENT: EPA
PLANT LOCATION; CLIMAX MOLY
UNIT TESTED: PEBBLE SCREEN TP3
OUCT NUMBER: TP3
DUCT AREA: 2.92SO.FT. ,23.125"
DUCT LOCATION: SCRUBBER OUTLET
FILTER NUMBERS: 02730
I.D.
TEST NUMBER: TP3-3
DATE: AUG 30,79
TEST COND: NORMAL
BAR. PRESS-IN HG: 21.60
PITOT TUBE FACTOR: 0.910
TIME TEST STARTED: 903
SAMPLE
POINT
START
B-1
2
3
4
5
6
7
8
9
10
tl
12
13
1.4
START
A-1
2
3
4
5
6
7
8
9
10
11 1
12 1
13 1
14 1
FLAP
TIME
(MIN)
0.0
4.0
a.o
.12.0
16.0
20.0
24.0
28.0
32.0
34.0
40.0
44.0
48.0
52.0
56.0
56.0
60.0
64.0
68.0
77.0
76.0
80.0
84.0
88.0
92.0
96.0
00.0
04.0
08.0
12.0
SAMPLE
VOLUME
(DCF)
9.138
12.180
15.430
18.750
22.150
25.720
28.980
31.240
33.055
34.970
36.860
38.660
40.240
41 .810
43.721
43.721
47.295
50.300
53.350
56.130
58.300
60.520
60.520
62.050
64.500
67.300
70.170
72.960
75.740
78.454
PTTOT
RDG
CINH20)
0.810
0.920
0.980
1..000
1 .100
0.900
0.370
0.230
0.270
0.270
0.230
0.170
O.J70
0.290
1.050
0.720
0.750
0.600
0.490
0.190
0.000
0.190
0.470
0.610
0.650
0.600
0.600
0.530
ORIFICE METERTEMP NOZ
ROG (DEG.F) OTA
CINH20) IN OUT (IN)
1.550
1.800
1.850
1 .950
2.150
1.750
0.720
0.450
0.530
0.530
0.450
0.3.30
0.330
0.540
2.050
1.400
1.450
1.150
0.960
0.370
o.ooo
0.370
0.910
1.200
1.250
1.150
1.150
1.050
70.
74.
80.
84.
90.
94.
84.
86.
87.
90.
88.
90.
90.
90.
92.
97.
100.
100.
100.
100.
100.
100.
94.
96.
100.
100.
102.
102.
65.
66.
66.
68.
70.
72.
76.
78.
78.
80.
81.
82.
84.
84.
86.
87.
90.
90.
90.
90.
90.
90.
92.
92.
92.
93.
94.
94.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
o.
0.
0.
0.
195
195
195
195
195
195
195
195
195
195
195
195
195
195
195
195
195
195
195
195
195
195
195
195
195
195
195
195
STACK
TEMP
(OF)
50.
55.
55.
55.
55.
55.
55.
50.
50.
50.
50.
50.
50.
50.
50.
50.
50.
50.
50.
50.
50.
50.
50. .
50.
50.
50.
50.
50.
STACK
VEL
(FPS)
63.774
68.299
70.491
71 .206
74.682
67.552
4 } . 3 1 3
33.983
36.820
36.820
33.983
29.216
29.216
38.159
72.610
60.127
6t .366
54.888
49.602
30.887
0.000
30.887
48.579
55.343
57.129
54.888
54.888
51.587
%I
«•
-------
.:;::YORfC RESEARCH CORPORATION
ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT 06906
JOB NUMBER; 9517-17
CLIENT: EPA
PLANT LOCATION: CLIMAX MQLY
(INTT TESTED; PEBBLE
;i STACK NUMBER: .TP3 ; , :
3 .STACK LOCATION ^SCRUBBER ; OUTLET
TEST NUMBER: 1
DATE: AUG 30,79
COMDIT IONS; NORM AL
AMBIENT TEMP-DEG F: 70
BAR., PRESS - I;V HG:21.60
ANDERSEN PARTICLE SIZING
DIAMETER WEIGHT % PER CUM% GR/SCFO MG/NCMO
1
.2 . .
3
4
5
6
7
8 ,'
FILTER
STACK
, STACK
> 11.72
11.72-7.30
7.30-4.94
4.94-3.36
3.36-2.15
2.15-1.06
1 .06-0.64
0.64-0.43
< 0.43
TEMP.fDEG.F
PPESSURECIN
i GAS ANALYSIS (DRY
!
r :
C02 .
CO .
N? .
02 .
H20 .
0.46
.;• > 0.00
0.50
0.07
; ; 0.30
0.65
0.66
;:-'•;:,:- 0*38"...
0.96
). . . . 70
.HG) . . 21 .
PERCENT)
.... 0 .
.... 0.
.... 79.
.... 20.
. . . . 2.
11.56 0.000070
0.00 B 8. 4 4 0.000000
12.56 88.44 0.000077
1.76 75. 88 O.OOOOU
7.54 74.12 0.000046
16.33 66.58 0.000100
16.58 50.25 0.000101
9.55 33.67 0.000059
24.12 24.12 0.000147
.0 SAMPLING RATE(ACFM) . . .
64 (SCFMQ). . .
CNCMMO). . .
00 IMP.ACTOR TEMP.(DEG.F) . .
00 PARTICLE DEMSITYCGM/CC) .
10 TEST TIME (MT*J)
90 TOTAL WEIGHT (MG) ....
00 TOTAL GR/SCFD . . . ...
TOTAL MG/NCMD
0.16
0.00
0.18
0.02
0.11
0.23
0.23
0.13
0.34
0.700
0.496
0..014
_ ..70.0
1 . 00
203 .2
3.9«
0.00061
1.39
-------
6.2 Field Data Sheets
-------
Molybdenum Dryer
-------
TP-1 Scrubber Inlet
-------
Particulate
-------
'. FIELD DATA
PLANT
DATF
SAMPLING LOCATION
SAMPLE TYPE • (Sftd
RUN NUMBER ±
OPERATOR
PROBE LENGTH AND TYPE.
NOZZLE I.D.__Joi-*
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P.,)
, FILTER NUMBER (s)
ASSUMED MOISTURE. % .jgV
SAMPLE BOX NUMBER —
METER BOX NUMBER -S-j
METER AHg P.O/ I
C FACTOR - '.»'•'
'"'•^'2 "
~R£e: .w&i\
PROBE HEATER SETTING
HEATER BOX SETTING_
REFERENCE Ap.
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA EVERY
MINUTES
TRAVERSE
POINT
NUMBER
7
CLOCK TIME
a
/-SI'S
GAS METER READING
VELOCITY
HEAD
(Aps), in. H20
.or
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
STACK
TEMPERATURE
(TS).°F
DRY GAS METER
TEMPERATURE
INLET
(Tmin),°F
ft 3
OUTLET
PUMP
VACUUM,
in. Hg
1,0
SAMPLE BOX
TEMPERATURE,
°F
2^0
•zso
2 To
IMPINGER
TEMPERATURE,
°F
To
0
'.*?,
!??',.•%*
9
U-
13
57
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COMMENTS:
M
7:0
B
70
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9Z0.92.
92
, t(
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GO
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13 C
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Bs
32.
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38004,'j
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~&iif**-•-., ..-.
ES-041...
j-'-^ ••;
-------
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
lVmi. II3
VELOCITY
HEAD
^pl. in. H0
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjOl
DESIRED
ACTUAL
STACK
TEMPERATURE
ITSI.°F
DRY GAS METER
TEMPERATURE
INLET
«Tmin.."F
OUTLET
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
,2
Icrl
Go
71
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A
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ES-042
-------
nf2>/i-^<. (IP,-(I/LT,. ,.
FIELD DATA
PLANT
DATE
PROBE LENGTH AND TYPE 3G>
NOZZLE I.D.
SAMPLING LOCATION
SANIPLE TYPE G.PA
RUN NUMBER ?
OPERATOR E-.
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE, (Ps)_
FILTER NUMBER (s)
ASSUMED MOISTURE, H
SAMPLE BOX NUMBER
METER BOX NUMBER.
METER AHg <
C FACTOR ±=
-3
SCHEMATIC OF TRAVERSE POINT LAYOUT
PROBE HEATER SETTING
HEATER BOX SETTING
REFERENCE AP
07(77
READ AND RECORD ALL DATA EVERY.
MINUTES
v', '.. -
' * ,' '-' ,.,: .
• -V"
TRAVERSE
i POINT
NUMBER .
CLOCK TIME
GAS METER READING
'••- (VJ.lt3
VELOCITY
HEAD
(Aps), in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
STACK
TEMPERATURE
(TS),°F
DRYGASHETER.
TEMPERATURE
INLET
(Tmin).°F
OUTLET
(Traout).°F
PUMP
VACUUM.
in. Kg
SAMPLE BOX
TEMPERATURE,
°F
IMPINGER
TEMPERATURE,
°F
?56.
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ES-041
-------
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
'V- «3
VELOCITY
HEAD
iApl. In. H0
ORIFICE PRESSURE
DIFFERENTIAL
IAH). in. H?0l
DESIRED ACTUAL
STACK
TEMPERATURE
ITSI.°F
DRY GAS METER
TEMPERATURE
INLET
OUTLET
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
9
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70
Ul£
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ES-042
-------
PLANT.
DATE_
FIELD DATA
/
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
en - Sc-'i-obLgy~
< = ^A ' g"
-H
-V/y/
PROBE LENGTH AND
NOZZLE I.D. ('2*
3'
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AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE, (Ps)_
FILTER NUMBER (s)
7 O6 ^
ASSUMED MOISTURE, %.
SAMPLE BOX NUMBER _
METER BOX NUMBER _
METER AHB cL
C FACTOR.
I -
PROBE HEATER SETTING 90 ?i
HEATER BOX SETTING
REFERENCE AP . V<
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA FVFRY 3 MINUTES
PlIDT . 96
$i7~ 1 7
TRAVERSE
POINT
NUMBER
SAMPLING
TIUC •
TIME, mm
CLOCK TIKIE
r!2nrhu,
CLOCK)
GAS METER READING
/V. 77^
VELOCITY
HEAD
(Aps), in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
STACK
TEMPERATURE
(TS).°F
DRY GAS METER
TEMPERATURE
INLET
(Tmin),°F
OUTLET
PUMP
VACUUM,
in. Hg
SAMPLE BOX
TEMPERATURE,
°F
IMPINGER
TEMPERATURE,
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COMMENTS:
ES-041
-------
TRAVERSE
POINT
- NUMBER
CLOCK TIME
GAS METER READING
'V- »3
VELOCITY
HEAD
{Apsl. in. HpO
ORIFICE PRESSURE
DIFFERENTIAL
IAH). in. HjOl .
DESIRED
ACTUAL
STACK
TEMPERATURE
(TSI.°F
DRY GAS METER
TEMPERATURE
INLET
«Tm).°F
OUTLET
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
^SJ_
SD
/o
72
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3
HO
3
12-
7?
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150
13
37
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<•/£>
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97
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53.
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/so
97
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38028
ES-042
-------
Particle Size Distribution
-------
PARTICLE SIZE DATA SHEET
1.
2.
3.
4..
5.
6..
7.
8.
9.
ih 3 f / / - / / (A
f P /9- ' (A
'. ,• . ~ ^>,t/»AV xw . /
^— - ' — — "^ ,. / ' **' f \ *^
'''.-, .'1 ;,.,„ ^~ .tttr S v. (A
•r ) 23 / 73'' (A
-.Af?i°^,:J '."'"" ' ";(A,8) ' •' 7f:'" '•••'••••"••' """(A
- •;::.£>;;:.:: (Av7^/^«=^-V^^>,p;
. . • . •*.•./ ..... .. ..;
1. *;*.•• 3 (R,8> '-'-.-••'• x/" (R,s): -• - i-?-d&-
,8)
,24
,24
,16
,16
,8)
,8)
,24
t. "-'" ' '
Type of Test
Job Number
Client •
(A,24} Plant Location
Test Condition
.Ambient Temp.
Test No., Stack No.
(A,24) Test Location
(R/8) 'I . (R,8)
Bar. Press: Pj.,
(in.Hg)
And,-Impactor Press. Inpactdr" Temp. Part.
Drop (Brink Impactor) Tj (deg F) - Density
Static (in.Hg) .. (gm/cc)
10.
11.
(R/8)
C0
(R,8)
(R,8) --r
.
(R,8)
(R,8)
% CO
.
(R,8)
%H20
(R,8)
12. And. /. •) * ./,/.;
Stage 1 2
(mg)
13.
Brinks Filter 5
Stage
(mg)
(R,8)
Filter
1 Cyclone
Probe
(R,8)
Sample Rate:Qn Stack Temp.: Tst '.Static Press. Test Time:
(ACFM) (Deg F) -" ... ; ' Duct: Pst .. . t (min)
.. . ' ' • •:•-. 1:^ '- "'••-;•••:•- (in.H20),,r.<; . '•„
-------
"38386 1
y
PARTICLE SIZE DATA SHEET
'7 -,-, .-I, t -,'.(
1.
2.
3.
4.
5.
6.
7.
8.
9.
) -• £j C / > - ^ /
y /T
1 1
i
0.-, j ..__ ^^-L
/
Type of-Test
(A,8) Job Number
_(A,24) Client
(A, 24) Plant Location
_(A,16) Unit Tested
(A,16) Date
(A, 8)
•• (A, 8)
_(A,8) Test Condition
- - Ambient Temp.
,(A,8) -;;Test No., Stack No.
Location
(R,8
Bar. Press: PJ-,
(in.Hg)
(R/8)
(R,8)
And ,-Impactor Press. Inpactor Temp.
Drop (Brink Impactor) Tj (deg F)
Static (in.Hg)
Part.
Density
(gm/cc)
(R,8)
C0
CO
%H20
11.
(R,8)
Sample Rate:Qn
(ACFM)
(R,8)
(R,8)
Stack Temp.
(Deg F)
"
st .
Static Press.
Duct: Pst
.- (in.H20) .-.- .-
'" '
12. And."
Stage
1 Cyclone
Probe
Test Time:
t (min)
.,> »!..^^ (R/8)
8 Filter
(R,8)
(R/8)
-------
Operator
Duct Dimensions
Iraactor I.D.
Nozzle Size:dn(in)
Pitot Factor: F
Clock Time
Meter Temp: Tm (deg F
Meter Rate: Rm(cfm)
1) Stack Pressure: Ps = Pb +
•
t
2. ) , 3 ^ inHg
' -
2) Mole Fraction Dry Gas: MJ = 1 - %H2° = 1 - - j_L = (>.2
^ - '-*•
.,100
100
3) Mol Wt. Dry Flue Gas: MWd = (.44 x %C02)+(.32 x %02) + (.28 x %CO)+(.28 x %N2)
= (.44 x _ _ ) + (.32 x _ ) + (.28 x __) + (. 28 x "_j _) = ' ^ ,f . <
4) Mol Wt. Flue' Gas: MW = (MWd) x (M^) + Fl8 x (l-Md)l ';
5) Stack Gas Velocity: Vst = 85.35 x (Fs) x.
i/ AP x (Tst + 4
6Q)
x MW
» 85-35
460) ,'
.2.;.
6)" ^Sample Rate: Qn = .327 x (Vst) x (dn2) , .
= -327 x ? 3, $C, x ( .25^)2 , C$7
ACFM
p
7) Meter Rate: Rm = (Qn) x jL x
Md
46°
x
C't
; SO
cfm
V
-------
TP-2 Scrubber Outlet
-------
Particulate
-------
FIELD DATA
TRAVERSE
POINT
NUMBER
K> '
3
3
c/
S~TiA{^~
/i (
2,
3
H
PLANT C-t-lf~tA y rtt>t-t'i3C>c?i£• /vjs
73. /<-/ 17
gy / T(-G-r -&£!.»<= fZ.
E S"*J>} - S~
yl^gy r>Y V &l_J ajTOl^
WPFRATURE <2 0
PRFSSIIRF
.SURF (P )
RFR(t) J*" <936^ O
PROBE LENGTH AND TYPE 3 c/^ (Sc/4«5<>
^--^ N07?IEID ^S
/V PROBE HEATER SETTING
HEATER BOX SETTING
/00 "7,
REFERENCE An . V?
7vi/?.t= -vv^V? SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA FVFRY /A MINUTES
GAS METER READING
(Vm).»3
?£.37 X
9 */ . 0 6 b"
/^ .(Oo
(01. ^
//c .00
/Ho -03
/ ~)~2 & • C?-^ C,
f3f. 7/5
/V.2 - C/<5"'T
VELOCITY
HEAD
(Aps), in. H20
, 3°
. 3^
• J. ^
. ^ ^
t^±/><^
, 30
, 2 /
- / 7
,/r
\V^CXV><5w^
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED
/./£
/-3b
. •%<-!
.37
/>C>0
/- /s
y ^
(iV
•^"6
\^^
ACTUAL
/./£
/, 5s"
. %q
• % 7
o^c
A/s"
. 5?
.< ^
. ^6
^^^
)*
, STACK
TEMPERATURE
(TS).°F
// X
//Y
/J*^^-^
//£
ltd
u a
^S"
^-> A^H
ficr&fc
3G
<%<%
8<2
93^
^V^xf
—
—
—
1 ~^o
OUTLET
7Z>
6^
70
7<5
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76
71?
-72
g1-/
^^<^^
380.
3
-"" 3
1L-<>
PUMP
VACUUM,
in. Hg
O
^, 0
c/.
4*0
3. e>
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^-^
3xf> o
S^c^
-^^^^ri
3^' /
.1
^ 3>S^/ S
) -
IMPINGER
TEMPERATURE,
"F
^g'
^S"
7?
7S
^crr=~==-
66^
6C>
G.O
6 0
^v^^11^—
^YfZ-1 ' G^>
^o^ o. o
COMMENTS:
ES-041
-------
7 - / 7
FIELD DATA
TRAVERSE
POINT
NUMBER
A ,
9
-3
V
Sr/t/^.
/? /
3,
J
c,
PLANT c^ <— ' n>4 V" A?c»c ~ff$L> 'BsUL'Y-^
DATE £ ~^ 3 ' 7 /&3.I
^ ^33.
Vg . /'& 5 £
G>0 /£'V7
72. /£, £1
5V /7//
% / 7 ^ 3
£/vz> 7~e£r
ICATION /7<*C '. £>&>'&'&- &U. L.^ I
F ^/?/i - o°7a
'ZOO
An / '/'?'
V-C ,/
VJ. 7
f
7^X25 - „ V s"<93 G SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA EVERY_/_2__ MINUTES
GAS METER READING
og. ir3
V^. 7£7
,<^. 7/
C7. 7^?
<£><-/. YS^"
7/. /J.2^
7/. /;*. C
7^
5. S
•PJX
•^20
L^O^-
.3V N
3 L/
5V
/Cs^/VPx-F
.
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED
/ 2,
•"SC
8 V
s~76>
•>^><\.
/• 3
/.yC
. 9V
• ?^
\^fv/x
ACTUAL
/. ;x
g>5^
. 51/
7^
^-=<>
/-3
;. s2-
51 Lie ^ CeL
IfTP.
DRY GAS METER
TEMPERATURE
INLET
V-'
•x"?
72.
76/
TA
V-^K^i
—
—
—
OUTLET
7S"~
7 "2
s- t£xL--
PUMP
VACUUM.
in. Hg
£". <9
V. 0
LI.O
V. 0
V<(£»&£
38017
38018
38019
/^i
rtLS
SAMPLE BOX
.TEMPERATURE,
°F
^ so
.^ 76
375-
,275
ii^^^KV^
n 7 ^
,727 <"
•3 <£ s^
^^ •r
<6i^v>v^
-i
.-'
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r
1
)
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IMPINGER
TtmrtKAIUKti
"F
6 <"
ST
s s".
v
6 o
C?o
£>o
C-,r>
f^SttyU^^.
f'Vft.it c:.5
^ C<5A
—
COfflENTS:
ES-041
-------
?
FIELD DATA
PLANT
DATE
- ~T*\
SAMPLING LOCATION /-7*«-r: - Zv£t-<£/2-
SAMPLE TYPE gp/3 - £~
RUN NUMBER J£
OPERATOR X-&I Tt'l V
AMBIENT TEMPERATURE Vt> ' F
BAROMETRIC PRESSURE
STATIC PRESSURE, (P$).
FILTER NUMBER (s) ** °
PROBE LENGTH AND TYPf "2
NOZZLE I.D. ,;a<3
ASSUMED MOISTURE, %
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AH@ /•
C FACTOR =
7-
PROBE HEATER SETTING
HEATER BOX SETTING
REFERENCE Ap
• J *1
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA EVERY
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
og. ft3
VELOCITY
HEAD
(Aps), in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED (ACTUAL
STACK
TEMPERATURE
(TS),UF
DRYGASKETER
TEMPERATURE
INLET
(Tmjn).°F
OUTLET
-------
Particle Size Distribution
-------
PARTICLE SIZE DATA-SHEET
1.
2.
3.
4.
5.
6.
7.
8.
9,
£t/r»/l?t
Type of-Test
_(A,8) Job Number
_(A,24) Client
_(A,24) Plant Location
_(A,16) Unit Tested
(A,16) Date
(A, 8)
(A,8) Test Condition
Ambient Temp.
(A,8) •£
gH _(A,8) Test.No., Stack No.
'/ (A, 24) Test Location
(R,8)
Bar. Press: Pj_,
(in.Hg)
(R,8)
(R,8)
And , -Impactor Press. Inpactor Temp.
Drop (Brink Impactor) ' Tj (deg F)
Static (in. Hg)
Part.
Density
(gm/cc)
10.
11.
(R,8)
C02
(Rr8)
(R,8)
02
(R/8)
% CO
..'• M'~ -i?~^
(R,8)
%H20
(R,8)
(R,8)
Sample Rate:Qn Stack Temp.: Tst
(ACFM) (Deg F)
Static Press.
Duct: Pst
(in.H20) ,,,••
Test Time:
t (min)
(R,8)
12. And.
Stage
(mg)
13.
Brinks
Stage
(mgj
Filter
?,36
^
(R,8)
Filter
Cyclone
Probe
-------
Visible Emissions
-------
REPORT HO.
PAGE.
VISIBLE EMISSIONS FIELD DATA /9/^c- / ^ -^
Date fi K^Yr2*/ Job Number /~~ ^57 "*-•/?•
Obser
. • Obser
Stack
Obser
."
. * . *
Cornmei
ver LAJ w>3.3>e,e tf£ —
vation. Point \P-
: Distance from
Plant & Location Orv^r- c.r/j^"
iro P" Wind -S Speed *^'/e -z-o ^/jf
2 3"' Hei^it ^ Direction N) U1^
nation Be~gan l^l-o
^
o
/
2.
3
4
4"
6
7
8
<}
/<3
//
/2,
/3
/A
/5"
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/s
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its:
O
3<2
I/
/^
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/^
f£
14
if.
>$
2o
£0
r°
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2-0
£.0
£0
2-0
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/f
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[2-0
2»
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'lo
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4^
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J&-.
IS \
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7,5
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/5 )I3 /^| >55"^ |zo /5^
2-P z^o 2,0 5~o 1/5^1-.;^ /y
37 \ia l/c- h?> \£.\ •lj'7b». 1/5" 2o
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;„.
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•'..'••. ' ' '••-•;•
-------
REPORT NO.
PAGE
Date
Obser
. • Obser
Stack
Obser
i t
Commai
ver
VISIBLE EMISSIONS FIELD DATA ' - #~ - •
Job Number /*?$"/ 7 -f 7
Plant & Location
vation. Point
: Distance from
vation Be~gan
^
o
/
2.
3
O
/^T
•z-o
^-o
)X-
4 fc>
^ ho
6 \u .
7 \lf
a
/^^
9 i/5" .
/o j»T
// ~'iV
/2
/,<
/-3 I/iff
/•* t^-o.
/r
/£
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/3
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its:
IS
^°
^6
,^0
1°
/J
te'
t»
•1.O
"l&
1.4
to
Wind & Speed
Hei^it Direction
•• Ended Skv Condition
% Opacity O^-^-c^ i-&-jf 2_
30
-^
:^
•^o
t£"
Zc?
2^
io bxp
if
If
i5
if
If
i£
j.
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to
i$
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t~ ,
/£
32
3.3
3f
35"
36
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if IK'
if if
2* IS
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/ . 2&
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/£/ j,f
if fS'
/o | c<^ yo
4.T '%\ O A5~ 30
/< • 40 •
/< 41
/< 4Z i
/4"l 43 1
/•^')/J44j
/^ 45- 1
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4f
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Z^., 491
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2o;|- 5"/ i • ••
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53 if-
3°,
\f . /ff /f 1.5-7) I
if \ is \ ^° «fs
ill! iv5^?! i
• , • - '
' - ,
-------
REPORT NO.
PAGE
Date
(> e
VISIBLE EMISSIONS FIELD DATA
' . Job Niiiriber f-
Observer
i> t/
Observation. Point
Stack: Distance from
Observation Be"gan
/
_Height_
Ended
Plant & Location
Wind 5-Speed °"
Direction
Sky Condition/
&
Opacity
1.0
8
/a
17
18
O
/Jb
30.
20
16
2.2
23
2.0
Zo
30 4
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30 4
2o 2o
241^
X5"
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2.1
2-%
23
30
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A;
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31 ^ P
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141 1^
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b>«> I Is-/
34
.30
36
?° Uol2o
37
3S
3^
/r
il^ ii-
Comments:
&*-
-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA 0 f&JU 2-u$Z_ '
Date 6 /^3/>? Job Number
Obser
Obser
Stack
Obser
Ccmmei
-- ~x &^&£££,
ver LA->o<5C^£eC- . Plant & Loca-tian^^ ^T'^f
vation Point V>cro^ Wind & Speed
: Distance from Height Direction
vation Be~gan
^
^
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/
2.
3
«$
4-
6
7
8
J5
(-4
jtf
(^/^«A-Ended / 7 (v Sky Condition
'{' "?> —.-" /TooLy b'y*'^ °^-^T
. % Opacity . :
30,
^5^
l^
(^
/£"
l?f
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1 ^\ if
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60
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2,0
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2°
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^
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a^ ^ 2^ so, !4ri
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7bx ?-ri?s^ 7^ — 9 i
?.< ?/ -z< o" ^o! i
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32
• 3,3
34
35"
^
2c '2o -2-i> |t^ ,5-^
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33
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39 1 vS^?'
- 1r- •"*"
• ' -s"1^-" -
. -
•• " -•' ' .
. ' -.
-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA Pn^tr /^j~2^
• Date ^/^/-h Job Nuinber 1- ?C?2--/-2
Obser-
. • Obser
Stack
Obser
.^A-.-V' •• '. •-- •
^,";*".V''. •;* •'•:" v : '*i''°*'-'
•"i3^°" -J-v . .- V-
,||:1 c
v^«. v;; • '»,-.;
.^•VCi. •••#"-.
•*-:i?z&:*.; •%•::;
llflKl-iv
C omraei
1 /
yer 1/0 U Q Q&E? ^Z__
/vi^)_y
Plant & Location iN^?/— i)^T/-ixT
vation. Point fibDi/p^ Wind .•SPSpeed
^-ZC?
: Distance fromo^o' Height (•; ' ' Direction
vation Be"gan
^
o
/
Zr.
3
•4
.r
6
7
8
^
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//
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/3
/4
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/7
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its:
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1$
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or
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15
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4£-
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2^?-
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/ 1 4! /Y
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/^ -0 /^ ~/3~ 43 /(9 ,
/O /5~ 16 1^ 144! u^
It) to \o IS', 14-^1^
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i
/^
/o
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m
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/o
Jo
/o j !b ft \jZ • !>5fl /(?
/O /Q /lj
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J^v
30
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1 6
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4r
/^"
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JO
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fi<^T~
/o
|/ (7 /o \of
/O e<
A
• . ' ''--•'
- - . -;'•••
' ' . • •>
-------
REPORT NO.
PAGE
Date
VISIBLE EMISSIONS FIELD DATA (>^<2 7 i.
Job Number 0 / - *? 5"/•? - /
Observer- J^ , \j\j: ;.
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TP-3 Dryer Area
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Visible Emissions
-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD
Date 08 - 3^-7^
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Job Number O/
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Wind & Speed
Direction
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD
Date 08 - 3. 3 -IS
Observer fcQu-bancx. T>Tgimnnoir> &
Observation Point f #•£?•. in TJWrf urc^~
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Wind & Speed
Direction
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41
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-------
REPORT NO.
PAGE
Praers - ' i^sf c|
VISIBLE EMISSIONS FIELD DATA
Date OS - ^ - T °[ Job Number 0 / - 9 £*/ '7 - / 7
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-------
Fugitive Emissions
-------
fvthrive. Time- Q
-------
bC*
06
o ,
0°/°
-------
Primary Crusher - Sprays On
-------
TP-1 Transfer Points Exhaust Duct
-------
Particulate
-------
FIELD DATA
PLANT i
DATE
SAMPLING LOCATION
SAMPLE TYPE
RUN .NUMBER _^
OPERATOR TV
-------
TRAVERSE
POINT
NUMBER
- (o
CLOCK TIME
TIME. mm
GAS METER READING
i 3
VELOCITY
HEAD
&3L
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. tOi
DESIRED ACTUAL
STACK
TEMPERATURE
IT.I.-F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in Hg
IT
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
y
ES-042
-------
PLANT
DATE
PROGE LENGTH AND TYPk'-5"
NOZZLE I.D. /^ i
ASSUMED MOISTURE, % ___
SAMPLE BOX MUMPER
METER BOX NUMBER _^3_r
METER AH
c
SAMPLING LOCATION.
SAMPLE TYPE
AMBIENT TEMPERATURE
BAHO;,1ETRIC PRESSURE
STATIC PRESSURE, (Ps
FILTER NUMbER (s)
PROBE HEATER SETTING - feO
HEATER BOX SETTING
REFERENCE i
COMlOTS:
38044
-------
TRAVERSE
POINT •
NUMBER
CLOCK TIME
SAMPLING
TIME, mm
GAS METER READING
3
VELOCITY
HEAD
ORIFICE PRESSURE
DIFFERENTIAL
iaH). in H0i
DESIRED ACTUAL
STACK
TEMPERATURE
lTs).°F
DRY GAS METER
TEMPERATURE
INLET
'Tmjn).»F
OUTLET
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
\ HtfoL
^u
(o/
ES-042
^£EOiO^/WL§
.
-------
FIELD DATA
PLANT_.':jreiVl(Lr;S9vv fAir
DATE **" ~ A. 7v - 7^
SAfilPLING LOCATION
SAMPLE TYPE _
RUN NUMBER _
OPERATOR •?). '
AHBIENT TE!.ii
BAROMETRIC PRESSURE
STATIC PRESSURE, (Hs) riii«^2-_
FILTER JiUr.iBER (s)
PROBE LENGTH AND TYPF
NOZZLE I.D. £P J_1 ?_> .__.^//U^
ASSUMED MOISTURE, "4
SAMPLE BOX NUMBER :
METEK BOX NUMBER .
MEIER iH J.J5L3
c *
- ( in
C FACTOR £2-4 ~2L<-
PROBE HEATER SETTING (aO
HEATER BUX SETTING -'JQQ
REFF.HENCE >,P £>.CI3.-
SCHEMATIC OF THAVERSt POINT LAYOUT
r^
READ AND RECORD ALL DATA EVERY :2. MINUTES
/O
SAMPLE BOX
TEMPERATURE,
°F
IMPINGER
TEMPERATURE,
"F
COIMEHTS:
' 38038 -
-------
CM\
TRAVERSE
POINT
NUMBER
CLOCK TIME
TIME, mm
GAS METER READING
•- "
VELOCITY
HEAD
lAp). in. H0
ORIFICE PRESSURE
DIFFERENTIAL
liHI. in H20l
DESIRED ACTUAL
STACK
TEMPERATURE
ITSI.°F
DRY GAS METER
TEMPERATURE
INLET
•Tn|B.."F
OUTLET
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
.ft-
JofL
3—&-
.M.—,
"
n
ES-042
-------
Particle Size Distribution
-------
PARTICLE SIZE DATA SHEET
Bar. Press: PJ
(in.Hg)
Type of-Test
(A,8) Job Number
(A,24) Client
(A,24) Plant Location
(A,16) Unit Tastad
(A,16) Date
(A,8) Test Condition
Ambient Temp.
(A,8) Test No., Stack No.
(A,24) Test Location
*~~ (R,8) / (R,8)
And ,-Iinpactor Press. Inpactor Temp. Part.
Drop (Brink Impactor) Tj (deg F) • Density
Static (in.Hg) (gm/ccj
10.
11.
(R,8)
2.0-
O -CD
(R,8)
% 02
(R,8)
% CO
%H20
(R,8)
(3.
Sample Rate:Qn Stack Temp.: Tst
(ACFM) (Deg F)
Static Press.
Duct: Pst
(in.H20)
Test Time :
t (min)
12. Arid. -•--/-•
Stage • 1
(nig)
13.
Brinks Filter
Stage
(rag)
1—J -' -V '!_£_;£- (R>Q'
7 8 Filter
(R,8)
1 Cvclons
Probe
O
03
oo
CO
-------
Operator
Duct Dimensions
Impactor I.D.
Nozzle Size:dn(in)
Pitot Factor: F
Clock Time
/ /
Meter Temp: Tm (deg Fl
Meter Rate: Rm (cfm)
1) Stack Pressure: Ps = Pb +
t
JL j . b
2) Mole Fraction Dry Gas: Md = 1 -
^^
J_ J . fa
100
= 1 -
100
inHg
3) Mol Wt. Dry Flue Gas: MWd = (.44 x %C02)+(.32 x %02)+(.28 x %CO)+(.28 x %N2)
= (-44 x ) + (.32 x )+{.28 x ) + (.28 x ___) -
-------
PARTICLE SIZE DATA SHEET
Type of-Test
1.
2.
3.
5.
6.
7.
8.
CUM.IX ,'i/cc. '/
£3.^^-3-
(A,a;
Bar. Press: P
(in.llg)
_(A,24) Client
_(A,24) Plant Location
(A,16) Unit Tested
(A,16) Date
(A,8) Test Condition
Ambient Temp.
_(A,8) Test Mo., Stack No.
_(A,24) Test Location
(R,S) /. (R,8)
Arid. ,-Impactor Press. Inpactor Temp.
Drop (Brink Impactor) Tj (dag F)
Static (in.Hg) ~ ' (grn/cc)
ar.
Densit-
10.
(R,8!
(R,8)
% co2 % o2
11. • ' ^> f^ (R,8) (£?-?" •
Sample Rate:Qn Stack Temo. :
(ACFM) (Deg F)
12 . And . 2. ! c - O C - 0
Stage 1234.
(mg)
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Brinks Filter 5 4 3
Stage ^ft-
(mgVf) "j? t^X^il
% CO %H20
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Tst Static Press. Test Time:
Duct: Pst t (rain)
• •;•-••• (in.H^O)
- n C-& -0 C. T±' :',''.- (R,S
5678 Filter
(R,8)
2 1 Cvclor.e
_ Probe
op-
(R,8)
t "Z.
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^Q^ti
-------
PARTICLE SIZE DATA SHEET
1.
2.
3.
4.
5.
6 . cs/fr
7.
8.
9. _Q
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,24)
,16)
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,8)
,24)
Type of -Test
Job Number
Client
Plant Location
Unit Tested
Date
Test Condition
Amb i e n t Temp .
Test Mo. , Stack Mo
Test Location
*,8) /, (R,8) •
Bar. Press: PJ-,
(in.IIg)
And,-Impactor Press. Inpactor Temp. Part.
Drop (Brink Irnpactor) Tj (deg F) Density
Static (in.Hg) (gm/cc)
10.
11.
(R,8)
-O
(R,8)
% CO-,
02
% CO
7-0
%H20
(R,8)
(R,8)
(R,8)
(R,8
(R,8)
Sample Rate:Qn Stack Temp.: Tst
(ACFM) . " (Deg F)
Static Press.
Duct: P
(in.H20)
St.
Test Time:
t (min)
12. And. ^-V-.-,
Stage 1
(mg)
13.
Brinks Filter
Stage
0
«r rt
131 . i o
2) 2. I
Cyclone
Probe
Filter
'/ (R,8)
CO
CO
-------
TP-2 Crusher Pit Exhaust Duct
-------
Particulate
-------
IT
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FIELD DATA
- t'AOt,^.
DATE_
SAMPLING LOCATION -'rnl-
SAMPLE TYPE PA-fH". _
PROBE LENGTH AND .TYPE J -
NOZZLE I.D. \l* ' i-13••'••>
P
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE, (PJ_
ASSUMED MOISTURE. % ^J>
SAMPLE BOX NUMBER ^
METER BOX NUMBER .
METER AHC,
C FACTOR ;
" ?-/& 7
PROBE HEATER SETTING.
HEATER BOX SETTING
REFERENCE AP V
SCHEMAT1C OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA EVERY^_
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(Vm). It3
VELOCITY
HEAD
(Aps), in. K20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
STACK
TEMPERATURE
(TS),UF
DRYGASKETER
TEMPERATURE
INLET
(Tmn),°F
OUTLET
PUMP
VACUUM,
in. Hg
SAMPLE BOX
TEMPERATURE,
°F
IMPINGER
TEMPERATURE,
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COMMENTS:
ES-041
\
-------
-------
FIELD DATA
PLANT.
DATE.
SAMPLING LOCATION ~t-JL)t-t I
SAMPLE TYPE .
RUN NUMBER _
OPERATOR ;
AMBIENT TEMPERATURE —M^.^L
BAROC.1ETRIC PRESSURE £>
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COi&iENTS:
ES-041
-------
TRAVERSE
POINT
NUMBER
SAMPLING
TIME.min
CLOCK TIME
|74-ht
CLOCK1
GAS METER READING
(Vml. It3
VELOCITY
HEAD
IApi. in. H0
ORIFICE PRESSURE
DIFFERENTIAL
IdHl. in H20)
DESIRED ACTUAL
STACK
TEMPERATURE
(TS1.°F
DRY GAS METER
TEMPERATURE
INLET
'Tm,,,>.0F
OUTLET
PUMP
VACUUM.
in Kg
SAMPLE BOX
TEMPERATURE.
°F
1MPINGER
TEMPERATURE.
°F
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-------
PLANT
DATE 4-A? 7/7^
SAMPLING LOCATION J7)^^T
SAMPLE TYPE "*' ' '
RUN' NUMBER 'TtiV£& fe)
OPERATOR
FIELD DATA
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6,0
CCMJI1EKTS:
ES-041
-------
TRAVERSE
POINT
NUMBER
CLOCK TIME
SAMPLING
T.i.r •
TIME, mm
GAS METER READING
'V ll3
VELOCITY
HEAD
li\pl. in. H0
ORIFICE PRESSURE
DIFFERENTIAL
DESIRED ACTUAL
STACK
TEMPERATURE
IT l.°F
DRY GAS METER
TEMPERATURE
INLET
(Tn,..«F
OUTLET
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
60
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Particle Size Distribution '
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PARTICLE SIZE DATA SHEET
/-.- ^••t-^-^t-^txLjS-c
i. f-r/7-/7
2. £/?s\
3. ^g^ C^/x
4 . ^i^^zfcz^e "/Sl^-
5. -r <£*&*•/ ^7, 9-
6 . '-'7 (R,8)
(A, 8)
(A, 24)
'2vf X /'^ ££-*<-/ ( A , 2 4 )
Type of Test
Job Number
Client
Plant Location
/•=>_/ -*. < / d'/^ \>-jrtL/~L'
~/^^>'i^€^'^0^< I /-V////7/.' v/ ( A , 1 6 ) Unit Te s ted
/
r (A, 16)
^r ' (A, 8)
// ^--^' ( A , 8 )
•f^-V Ls^tsts'-^l^i ( A , 2 4 )
/ '& (R,8) ,<^'^^' " (R,
Date '
Test Condition
Ambient Temp.
Test No. , Stack No
Test Location
8) /-O (R,8)
Bar. Press: P
(in.Hg)
___
J-, And , -Impactor Press. Inpactor Temp". Part.
Drop (Brink Impactor) Tj (dag F) Density
Static (in/Hg) (gm/cc)
10.
% C02 % 02
11. ;J ^ ^ (R,8) &^ '
Sample Rate:Qr Stack' Temp. :
(ACFM) .. ' (Deg F)
12. And. ••/- '"' !• t'-£ 1'', 7 ; •_ '••::'
Stage 1234
(rag)
13.
Brinks Filter 5 4 . 3
Stage ^
Q. p- jfl. ft (" 7 i (y(_A C~ "
% CO %H20
(R,8) /"^' — ' (R,8) ' ^ -'— : '
Tst Static Press. Test Time:
Duct: P3t t (min)
(in.H20) ' , .
i 1? '•• '; ^ r. / J" :, :-:; c-':- (R,S;
5678 Filter
(R,8) CO^"
2 1 Cyclone • ^
Probe ^
CO
, — - ^~ r— • •-- - - - ..-'-
(R,8
(R f 8 )
1 <-
••-•*• '
^,
3
s&ilS3?y
X/O'JAury
-------
Operator
Imactor I.D.
3 ^-
Pitot Factor: F
Clock Time
72—
1) Stack Pressure: Ps = Pb +
13.6
Duct Dimensions
Nozzle Size:dn(in)
Meter Temp: Tm (deg F]
Meter Rate: Rm(cfm)
13.5
inHg
2) Mole Fraction Dry Gas: MJ = 1
100
1 -
100
3) Mol Wt. Dry Flue Gas: MWd = (.44 x %C02)+(-32 x %02)-:-(.28 x %CO) + (.23 x
= (.44 x _ _) + {.32 x __ ) + (-28 x _ _) + (.28 x __) - 2 ^-^
4) Mol Wt. Flue Gas: MW = (MWjj) x (M^) +[~18 x (l-Md)|
x
+ 18 x (1 -
5) Stack Gas Velocity: Vst - 85.35 x (Fs) x
/AP x (Tst + 460]
Ps x MW
= 85.35 x
x
fps
6) Sample Rate: Qn
= .327 x
327 x (Vst) x (dn2)
x
)2 =
ACFM
Rate:
x
(Qn) x p£ x
J- m
m
•D U-
ITo
x
cfm
-------
PARTICLE SIZE DATA SHEET
1.
2.
3.
4.
5.
6.
^
Type of-Test
(A, 8) Job Number
(A,24) Client '
(A,24) Plant Location
(A,16) Unit Tested
(A,16) Date
(A,8) Test Condition
Ambient Temp.
(A, 8) Test No., Stack No.
(A, 24) Test Location'
(R/3)
(R,8)
(in.Hg)
And ,-jUTipactor Press. Inpactor Temp. Part.
Drop (Brink Impactor) Tj (deg F) Density
Static (in.Hg) (gm/cc)
10.
(R,8)
(R/8)
(R/8)
% co2
x " U-
11. •' ~> ' (R/e;
S amo le Rate : Qn
(ACFM)
12. And. •.; /• '. .] '<'"',
Stage 1 2
(mg)
13.
Brinks Filter 5
Stage
(mg)
% 02 % CO %H20
i ..'••--.-•. ~ ..••.-. • . • •
/" ' • ' '•/.<. T-? .'•-• . : , :>
)' &T~f~~ -
-------
PARTICLE SIZE DATA SHEET. .
1.
2.
3.
5.
6.
,1? CC V
2-7,7
*^ (A,8)
(A,8)
'•/ (R,8)
/•o
(R,8)
_ Type of Test
_(A,8) Job Number
_(A,24) Client
_(A,24) Plant Location
(A,16) Unit Tested
_JA,16) Date
(A, 8)
Test Condition
Ambient Temp.
(A78) Test Mo., Stack Nc
(A724) Test Location
(R,S)
Bar. Press; Pv,
(in.Hg)
And,-Impactor Press.
Drop (Brink Impactor)
Static (in.Hg)
{R/8)
Inpactor Temp.
Tj (deg F)
Part.
Density
(grn/cc)
10.
11.
(R,8)
(R,8)
'6-0
(R,8)
(R,8)
% CO-
02
% CO
(R,8)
Sample Rate:Qn Stack Temp.: Tst
(ACFM) • (Deg F)
Static Press.
Duct: Pst
(in.H20) •.••'•••..
Test Time:.
t (min)
12. And. :<,;-^
Stage 1
'(mg)
13.
Brinks Filter
Stage
(mg)
i' C: ") (R,8)
8 Filter
(R,8)
1 Cyclone
Probe
C'J
-------
TP-3 Scrubber Outlet
-------
Particulate
-------
/
FIELD DATA
PLAIST
DATE
PROBE LENGTH AND pPE
NOZZLE 1.0 -&J3
ASSUMED MOISTURE, % '3*7.
SAMPLE BOX NUMBER
METER BOX NUMBER
KETER
G
SAMPLING LOCATION
SAMPLE TYPE gP/4 - -S
RUN HUM3ER
PROBE HEATER SETTING '
-------
I - ft s / / - i /
-------
FiEU
PLANT
DATE
SAMPLING LOCATION
SAMPLE TYPE <*?/>/•! - ^
RUN NU.HBER ^~—Js±
OPERATOR
ATiiBIEMT TEMPERATURE feO
BAROKETSIC PRESSURE '3 £"•
STATIC PRESSURE, (P..) fj^l
FILTER NUiViBER (s) ff QJ^f^n
PROBE LENGTH AND
NOZZLE I.D. ' t'^f
ASSUMED MOISTURE, ft ....>
SAMPLE BOX NUMBER _O/
METER BOX NUMBER ^ - *
METER A!
•e-fftef err JL.
PROBE HEATER SETTING.
HEATER BOX SETTING__232±L
REFERENCE An /- <-,
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL OATA EVERY,
MINUTES
U2^7
TRAVERSE
POINT
NUMBER
CLOCK TIME
TIHE,«in
GAS METER REAOIfiG
(Vm), It3
VELOCITY
HEAD
(AP). in. H0
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED
ACTUAL
STACK
TEMPERATURE
(TS),°F
DRYGASCiETER
TEMPERATURE
INLET
(Tmin),"
OUTLET
PUMP
VACUUM,
SAMPLE BOX
TEMPERATURE,
°F
IMPINGER
TEMPERATURE,
"F
5" £>
64
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6 0
-------
ES-042
-------
FIELD DATA
PLANT
DATE
PROUE LENGTH AND TYPE /Q ' 5>.
NOZZLE I.O. .. /»'£
SAMPLING LOCATION <~
SAMPLE TYPE
RUN NUMBER ~t'.v- 3
OPERATOR k£i TH -f
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE, {Ps)_
FILTER NUMBER (s) _*f
-TAfLG ' .'
ASSUMED MOISTURE, % _2_
SftfilPLE BOX NUMBER f? f
METER BOX NUMBER j
METER AHfc /^gfe ^._
c- pac-iea— ?<;/>' ^ - . s"
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COIHMEHTS:
ES-041
-------
ES-042
-------
Particle Size Distribution
-------
PARTICLE SIZE DATA SHEET
1.
2.
3.
4.
5.
6.
7.
8.
9.
....-.— .
^97
Type of 'Test
_(A,8) Job Number
(A ,24} Client
(A, 24) Plant Location
(A, 16) Unit Tested
. ,
(A ,16) Date
'O ( A , S )
O
.-— 7--
V
• (A, 8 )
(A,8) Test Condition
Ambient Temp,
_(A,8) Test Mo., Stack No
(A,24) Test Location
f (R,8)
Bar. Press:
(in. Kg)
An
rr.pactor Press.
Drop (Brink Inpactor)
Static (in. Fig)
.(R ' 8) ^J
-------
Visible Emissions
-------
REPORT NO.
PAGE
jf — -k
VISIBLE EMISSIONS FIELD DATA /'fae* / <-~^-~ >
Date rVV?> / ~}-c) Job Number /- /V7 7--t >
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Observ
Stack:
Obsei^
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f er fjjA; 'J& i& ftr~ P—
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ration. Points-**. 6^c..fc c/-/_ S/v
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nation Be"gan c9/"3
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA /^^ ^^{f > '
Date S '?>•' '*•••"? Job Number t- /- ,
Observer U-A ^.^ B c? ^
Plant & Location W-T/t-^r
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Stack: Distance from Hei^at
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA fiff* ^^3
Date W~'/V>7 Job Number/- C1'S/ 7- -/?
Obsei^
Obser\
Stack,
Obser\
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD
Date $ tP/t. 7-/>*7
Ob sen
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Obsen
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA P/% t 2-c./?''
/ / ' i/1 **
Date '# ' - - / 1 1 • - - Job Number / - ? T/ - .- / ?
Ob sen
Obser\
Stack:
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REPORT NO.
PAGE
VISIBLE EMISSIONS PIELD DATA p*^ ' ^-'3 . '
Date 1% ' ? /'2<7 ' Job Number A "z?57 ^ "/ -~
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA f^^~^ ~Z-^'{\- 3
Date \2nW~n • Job Number /- ?5*/?~/' 3-
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA p0!^ *> ^pJ-
Date iY7?-/?---? Job Number 1 ~ ^SlT-'f ?*
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Visible Emissions
-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD
Date 8-2, 7 - 7 ?
Obsen
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA
Date 8-2*7-79 Job Number O t - 9 X/f-t ?
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA
Date 9 -27- 7?
Job Number
7
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-------
REPORT NO.
PAGE
Date S~Z7-~7tf
Observer
VISIBLE EMISSIONS FIELD DATA
Job Number /?/_
Plant & Location
Observation. Point
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Stack: Distance froi
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA
Date g -Z7- 77
Observer LAMEJ*
Job Number
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REPORT NO.
PAGE
Date
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VISIBLE EMISSIONS FIELD DATA
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Stack: Distance from /fffiHeight A
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TP-5 Rail Car Unloading
-------
Visible Emissions
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REPORT NO.
PAGE ../ ^-
VISIBLE EMISSIONS FIELD DATA
Date ? ~ x_. 7 - 7 *? . Job Number •' - "7 ^ / ? - / >
** ''' *•' '' ' i i
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-------
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-------
/7
REPORT NO. ' PAGE J ,.r<3
VISIBLE EMISSIONS FIELD DATA
Date >~- ~ ^ ? - 7 - Job Number / - r ^ / 7 -/ 7
Obsen
Obser^
"Stack;
Obsem
Comme]
fj/'-/-* ^/'j-L. 1
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-------
R£PORT NO.
PAGE
VISIBLE EMISSIONS FIELD
Date * - .,7 ?-?'?.
_. J^-M- *;/-J-f-~ 1 -,
Observer X. ^/2-- X/T/T-. ••'•-'?
Observation. Point ^/O^^
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-------
HEPORT NO.
PAGE /<-''.,
t
VISIBLE EMISSIONS FIZLD DATA . '
Date .'T ~-A ? - ~ "~ ,". Job Nuihber / ~ '"'' ' ^ ' / 7-/S
Observer /^C^" /'.."f^'.'J. 0 Plant & Location •••'•••••' /'•x>^,<--.~ ••
. • Observation Point X^X— ^> x- Wind & Soeed Y/<
"'r " 'Stsek: Distance from ^jTf He i sit •'>//• C •/ Direction-'///--'
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f- 1 ' ' / ' ~ ,', T 1 y«
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ft
REPORT' NO.
PAGE
VISIBLE EMISSIONS FIELD DATA
Date ^ -..";. 'r - /,'-?.•• Job Number / - -? <~/ ? -/ ?
Observer ./4/^r /^"c7^^» ^?
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c ,
REPORT NO. PAGE /.." '_
VISIBLE EMISSIONS FIELD DATA
Date rO. ,?-•?- /• Job Number /_ -"r/ -^ .../-
Ob sen
Obser^
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-------
REPORT" NO.
PAGE
Bate
Observer
Observation Point
. J
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VISIBLE EMISSIONS FIELD DATA
212 * Job Number •; - qc /-;.../ 7.
Plant & Location^. //r.gt.^v.<'
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so 45*1 TO o
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Fugitive Emissions
-------
-------
.,-.-...,.,.. .,_' :-. . „,._-» _, .;.*.. . '. . •' .....v •. J.
VtS' J-VlS ..(f6
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-------
TP-6 Crusher Building
-------
Visible Emissions
-------
REPORT NO.
PAGE
c
(j
VISIBLE EMISSIONS FIELD
Date OA- 3-t - 13
Observer R>£.r txxr-0~ 7^ru-mkvx<5^
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REPORT NO.
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VISIBLE EMISSIONS FIELD
Date 08 - 2*V - V}
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REPORT NO.
PAGE
Date 08 - y\
C- fusKi/^' - ~T£.Srf *1_ CorrH f\x^Jtdc. M? ."V
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REPORT NO.
PAGE
£rusKfl.r~' - .""fesf <2- (£J^
VISIBLE EMISSIONS FIELD
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REPORT NO.
PAGE
Date o#-
Ob s e rve r l^Cu^boAO^
Observation Point ^-
(IN-
VISIBLE EMISSIONS FIELD DATA
Job Number Q/ -
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REPORT NO.
PAGE
C/r^«*-S'r^< — '— l-£>S~f" 3- (iE-B^
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-------
PAGE
Date 08- Stl- -
VISIBLE EMISS
Observer DCXr^biir-iX- "DrurvMrvoo
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-------
REPORT NO.
PAGE
- -rest 3
Date
VISIBLE EMISSIONS FIELD DATA . *
Job Number H / - 9r<7<7 -/ 9
Observer
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-------
REPORT NO.
PAGE
Date D$-<21- - '
Observer "pjOuri
VISIBLE EMISSIONS FIELD DATA . *
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FIELD DATA
PLANT
DATE
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SAMPLE TYPE "rkH-i'o
RUN NUMBER '
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SCHEMATIC OF TRAVERSE POINT LAYOUT
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in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
({-
$£-
1^3.
- IP
toO
ES-042
-------
FIELD DATA
O
PLANT.
OATE_
SAMPLING LOCATION
SAMPLE TYPE '
RUN NUMBER^
OPERATOR
AMBIENT TFMPERATUREU
BAROMETRIC PRESSURE •?_/- ^ '
STATIC PRESSURE, (Ps).
FILTER NUMBER (s)
PROBE LENGTH AND TY
NOZZLE ID
ASSUMED MOISTURE, t.
SAMPLE BOX NUMBER _
METER BOX NUMBER _
METER AHfi
75"
"e-
C FACTOR.
PROBE HEATER SETTING
HEATER BOX SETTING
REFERENCE Ap
O . 1
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA FVFRY
MINUTES
TRAVERSE
POINT
NUMBER
~ t
- /
-^L
-Q.
-3
CLOCK TIME
10
\3L3i
30
jjJtt
50
COMMENTS:
M90
GAS METER READING
)."3
37s-
. ^^
^L
JJL
VELOCITY
HEAD
(APS). in. H20
0^0
o/?/
-U
I./
ORIFICE PRESSURE
DIFFERENTIAL
(aH), in. H20)
DESIRED ACTUAL
a.
l.r
..13
MT
L2
L3
3809Q -
LJ—f -^-*—rJ—L«t.
38091j
STACK
TEMPERATURE
(TS),°F
DRY GAS METER
TEMPERATURE
INLET
-------
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
VELOCITY
HEAD
IAps>. in. HjO
ORIFICE PRESSURE
DIFFERENTIAL
IAH). in. H;0>
DESIRED ACTUAL
STACK
TEMPERATURE
(Tsl.°F
DRY GAS METER
TEMPERATURE
INLET
'Tmin..'F
OUTLET
lT«o«l'-OF
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
J&=L
/ O
33:
C£
o
/01
\lfT
ES-042
-------
PLANT
DATE
PROBE LENGTH AND TYPE
NOZZLE 1.0.
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
OPERATOR
ASSUMED MOISTURE,
SAMPLE BOX NUMBER
METER BOX NUMBER
METER AH
C FACTOR
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
PROBE HEATER SETTING
HEATER BOX SETTING
REFERENCE AP
ST ATIC PRESSURE. (P)
FILTER NUMBER (s)
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA EVERY
ES-041
38095
-------
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
VELOCITY
HEAD
(Ap$l. in. HjO
ORIFICE PRESSURE
DIFFERENTIAL
IAHI. in. H^Oi
DESIRED ACTUAL
STACK
TEMPERATURE
lTs>.°F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
^&.
-L£.
____Z-±i__
V ub
ES-042
-------
Particle Size Distribution
-------
'PARTICLE SIZE DATA SHEET
Type of -Test
2.
3.
4.
_(A,8) Job Number
_(A,24) Client
_(A,24) Plant Location
__(A,16) Unit Tested
(A,16) Date
r=- (A, 8)
7.
8.
9.
. (A, 8}
ft A/OT
(A ,8) Test Condition
Ambient Temp.
(A, 8) Test. No., Stack No.
(A,24) Test Location
(R,8)
(R,3)
Bar. Press: PJ-, And, -Impactor Press. Inpactor Temp. Part.
(in.Hg) Drop (Brink Impactor) Tj (deg ?) Density
Static (in.Hg) (gm/ccj
(R,8)
10.
(R,8)
(R,8)
(R,8)
i
;
•
S
"_j^
% C02 % 02 . % CO %H20
11. O J (R,8) fafl, (R,8) — 3'J (R,8) &»C) (R,
Sample Rate:Qn Stack Temo. : Tst Static Press. Test Time:
(ACFiM) (Deg F) Duct: Pst t (min)
.. .- ' (in.H20) .
12. And. 17,7^ l/tf 1 icl i.C'J. 1*5 17? il/2 «.7r, ^-^3 (R,8)
Stage 1 23 4. 5 6 7 8 Filter
(rag)
13. . (R,8) -N
Brinks Filter 54321 Cvclone <>j i
Stage 'V ' Probe Ch
(rag) r\ , -
9; t
^^
- ctlTw
LI b ' ' M /
fel^
VtijT^3 )Kf *'
t^JW'lttl'To 76 - ,f .f%=?\
i ' / 1 1 ^»a L * 1 *. -i
/ H~ i (5 3 I "7 C? //O /" k 1 1 1 •««.-" y
' / j • ' "^ / ^ / f *) I • C^
, / "^ — / v^ , '
-------
PARTICLE SIZE DATA SHEET
Type of -Test
1. ^h
2. ,£•*/
3 . /' s* •'i 6<-<^"&*££-, ^> 'Co- »?g^Ng>- 'A/' (A, 8)
J-^f f £?*'£ f'fA(J$ f~ (A, 24)
^R,8) /-O (R,8) f^'f ' (R/
And ,-Impactor Press. Inpacl&or Temp.
Drop (Brink Impactor) Tj (deg F)
Static (in.Hg)
(R,8) c/<^- ^ (R,8) (^?- O (R,
% 02 . .... % CO
(R,8) &£> (R,8) — 3- S (R/
Stack Temo. : Tst Static Press.
(Deg F) Duct: Pst
:>•:=•,•:::'. (in.H-,0)
• • * ' . «
2 3 4. 5 6 7 8
(R,
54321 Cyclone
Probe
^i-t.--3,3
t<-1 «- . Bill3-*- ' .
» • - «?
Job Number
Client
Plant Location
Unit Tested
Date
Test Condition
Ambient Temp.
Test Mo. , Stack No
Test Location
8) ' /• V. (R,8)
Part. ->
Density
(gm/cc)
8) o^ ^: (R/8)
%H20
-7rV
8) /JO (R,8)
Test Time :
t (min)
5 ^/ (R,8)
Filter
8)
•\- ' ' • '
i Sjr <*•;••<•»••— 7\
ff
-------
PARTICLE SIZE DATA SHEET
1.
2.
3.
4.
5.
6.
7.
8.
9.
2 ^ 7*7
Type of -Test
_(A,8) Job Number
_(A,24) Client
^_(A,24) Plant Location
_(A,16) Unit Tested
(A,16) Date
(A,8)
(A,8)
Bar. Press:
(in.Hg)
_(A,8) Test Condition
Ambient Temp.
.(A,8) Test No., Stack No.
(A,24) Test Location
(R,8) / (R,8)
And , -Infpactor Press. inpactor Temp .
Drop (Brink Impactor) Tj (deg F)
Static (in.Hg)
Part..
Density
(gm/cc)
10.
11.
O-o-'
JR,8)
co
(R,8)
O -o
% 02
(R,8)
." % CO
%H20
(R,8)
Sample Rate:Qn
(ACFM)
(R,8)
(R,8) ~
(R,8)
Stack Temp. :
(Deg F)
st
Static Press.
Duct:
-.-..' ;•*'::::: (in.H20]
12. And.
Stage
(mg)
13.
Brinks
Stage
(mg)
Filter 5
i': (O
1,7$ ^$ *£'/ *44 /.
4. 5
3 2
6 7
1
1 Cyclone
Probe
Test Time:
t (min)
(R,8)
(R,8)
Filter
(R,8)
[6
-------
TP-2 Crusher Pit Exhaust
-------
Particulate
-------
FIELD DATA
PLANT.
DATE_
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
OPERATOR
-6;
rf i
PK
- /&/
- /6l
LENGTH AND TYPE '
Fl.D. .It \.J3oT
AMBIENT TEMPERATURE .
BAROMETRIC PRESSURE .
STATIC PRESSURE, (Ps)_
FILTER NUMBER (s) :
- O.
PROBE
NOZZLE
ASSUMED MOISTURE, %.
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AHg L
C FACTOR —
/-
-•Q_
33-
-ia
5? M-7
1.7
•05
Y/5
f/yfv
(JO
8-1
.TO
5?
1.3
8*1
(c
It
53
L^_
5
7
56,
/.a
35- -75
y.3
bO
7V
9
37-
(sO
7V
J5O
10
1.2
J7
^=TQ
7
II
33
OS1
3.0
7V
/Z-
9 ;/
t
1.7
ttO
3.&D
JL^_
•tol
$1
(
-------
(CO/IT.)
-i 7
TRAVERSE
POINT
NUMBER
GAS METER READING
IV.I. II
3
VELOCITY
HEAD
4pt. in. H0
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in H20l
DESIRED ACTUAL
STACK
TEMPERATURE
(TSI.°F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in Hg
SAMPLE ,BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
& 1
bfl
. 5V
100
5?-**
75-
GO
/oo
75
qq
9/
57
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loo
C&0
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9
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3(00
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bo
90 tO 07
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1-5
,57
93
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V
55-
10
1-7
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102
It
99 ®/l>
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10
,(o\
no
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1.5-
1)0
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in
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120 10 31
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10
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I/O
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jo
19
132-
U^
38058 r
38058
5.6
ES-042
-------
FIELD DATA
TRAVERSE
POINT
NUMBER
A V
2.
M-
5
10
n
IL
/3
/v
/s
n
it
°
AL
$o
33
PLANT
DATE.
^Ihr
SAMPLING LOCATION / r-2-
SAMPLE TYPE.
RUN NUMBER _
OPERATOR
nf#-/ -
LENGTH AND'
NOZZLE I _
ASSUMED MOISTURE, % /£>
SAMPLE BOX NUMBER
METER BOX NUMBER
/
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE **'
STATIC PRESSURE, (Ps).
FILTER NUMBER (s)
?/• (s&
e-
METER AH
CFACTOR.
PROBE HEATER SETTING.
HEATER BOX SETTING
REFERENCE Ap \
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA FVFRY 3 MINUTES
P/T&T
CLOCK TIME
CLOCK)
123^
ft^
1250
1305
H-S ($0%
7M
5V- A /
13
-£-
JJL
fab 133}
GAS METER READING
(VJ.lt3
135
.53
Tl.
lot. S5
70% -
. $5
7 1 1-53
. /so
VELOCITY
HEAD
(Aps), in. H20
/
1-5
/. 5"
o
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
,53
57
.(el
,51
t-W
3.5-
•57
•57
,57
.(*!
,57
,$0
STACK
TEMPERATURE
(T5).°F
laO_
(00
(sO
UO-
o
(pO
frf)
60
DRY GAS METER
TEMPERATURE
INLET
(TBia).«F
7M.
(Ob
/Of
*
OUTLET
to
12
i/
PUMP
VACUUM.
in. Hg
Z
SAMPLE BOX
TEMPERATURE.
°F
JSO
IMPINGER
TEMPERATURE,
°F
GO
jro
5D
50
51*
COMfilENTS:
ES-041
0.0
-------
~ /7
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
'V- »3
VELOCITY
HEAD
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20i
DESIRED
ACTUAL
STACK
TEMPERATURE
ITS».°F
DRY GAS METER
TEMPERATURE
INLET
«Tmjn.."F
OUTLET
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
-33
72,
1331
, r?
.17
1S_
(2,
Ji3.
UK
1
,35"
,35"
W
13
90
13 55
1-5
.51
102
l3 52
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•7
t-7
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ten
n
7-3V-53
5*1
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1-1
bo
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10
737-7/
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Lkl
AS
,51
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,5-3
,53
103
17
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,53
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(oO
20
JOLL
21
y?
/fib
32*
-75-I.OSD
j%.
W059
38061 r
Sj^_
ES-042
-------
FIELD DATA
TRAVERSE
POINT
NUMBER
2_
5_
1°.
^
w
if
n
^o_
(2L
9fr~t
Q.
<>o
i'3L
COMMENTS:
PLANT pun ft*—-
DATE
SAMPLING LOCATION
SAMPLE TYPE fiA g
0 ASSUMED MOISTURE, t /-5
SAMPLE BOX NUMBER ' '
METER BOX NUMBER _
^/^ METER AH@
CFACTOR
PROBE HEATER SETTING.
HEATER BOX SETTING
REFERENCE Ap
7070
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA FVFRY
MINUTES
CLOCK TIME
Ma?
GAS METER READING
(Vm). It3
•753.09
757 -
763.
76 ^. 03
77.3 .£3
77^ . 77
. 5o
. 7?
73g.
VELOCITY
HEAD
(Aps), in. H20
y.s*
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
So
.61
23,
JL?_
^C2_
JT?
.A\
.So
^Z.
..S'o
STACK
TEMPERATURE
(TS).°F
to
DRY GAS METER
TEMPERATURE
INLET
(Tmjfl).°F
,/^L
OUTLET
34
5J_
PUMP
VACUUM.
in. Hg
SAMPLE BOX
TEMPERATURE,
°F
3^5-
IMPINGER
TEMPERATURE,
"F
5*4
^(L
5-5-
5-4
5T
ES-041
-------
rf 6'
TRAVERSE
POINT
NUMBER
SAMPLING
TIME.min
CLOCK TIME
GAS METER READING
'V-'l3
VELOCITY
HEAD
IApsl. in. HjO
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20l
DESIRED ACTUAL
STACK
TEMPERATURE
(TS».°F
DRY GAS METER
TEMPERATURE
INLET
to
107
77
L7
/O
//o
Od I7&8
no
Si 60
U-
Z6.
flt
522
/to
6s-
//o
1*5
ito
.5-0
811.^7
o
X13-QC.
££.
j^L
U<2-
314.. 3?
t*a.
38064
38063
38062
ta:
ES-042
-------
Particle Size Distribution
-------
PARTICLE SIZE DATA SHEET
1. ty ff~? -V 7 '
y^~v^xi3
2 (— I fi
• f ' • ,- " f - /* ^///7J
3 . 3~T~L- U. *~ V?. //•/-& f£-**L> £ ;- fe*s^ -^-O— .-
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5. /^/6- ^n*!
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e. . (./— <^Xs^c;jr-
9. r) ( > (-0 (R/8) /<' ) (R,8) ^
(A, 8)
(A, 24)
?rt/r' ^/^
(A, 24)
(A, 16)
(A, 16)
(A, 8)
^- (A,8)
(A, 24)
5^" (R
Type of -Test
Job Number
Client
't^y
Plant Location
Unit Tested
Date
Test Condition
Ambient Temp.
Test No. , Stack No
Test Location
,8) / (R,8)
Bar. Press: PJ-,
(in.fig)
And,-Impactor Press. Inpactor Temp. Part.
Drop (Brink Impactor) Tj (deg F) Density
Static (in.Hg) ' (gm/cc)
10.
11.
(R,8)
C02
(R,8)
O-O (R,8)
02
.... % CO
(R/8)
%H20
(R,8)
(R,8) ""/ ' (R,8)
(R/8)
Sample Rate:Qn Stack Temp.: Tst Static" Press. Test Time:
(ACFiM) (Deg F) Duct: Pst t (min)
. . •: •;• •. •• •• '. :- :•".•;<••V(in.H20)
12. And
Stage
(mg)
6
(R/8)
1 Cyclone
Probe
8 Filter
(R,8)
-------
3 e 9
PARTICLE SIZE DATA SHEET .
1.
2.
3.
4.
5.
6.
(A, 8)
r/t/f
i J.
/
(R,8)
Bar. Press:
(in.Hg)
(H,8)
Type of-Test
_(A,8) Job Number
(A,24) Client
y
r,24) Plant Location
_(A,16) Unit Tested
_(A,16) Date
(A,8)
Test Condition
Ambient Temp.
(A,8) Test No., Stack
^(A/24) Test Location
(R,8) / (R78)
And,-Impactor Press. Inpactor Temp.
Drop (Brink Irnpactcr) Tj (deg F)
Static (in.Hg) . ...
Part .
Density
(gm/cc)
10.
11.
(R,8)
CO-
02
Sample Rate:Qn
(ACFiM)
(R,8)
Stack Temp.:
(Deg F)
(R,8)
(R,8)
... % CO
(R,8)
%H20
(R,8)
Static Press.
(R/8) (
Duct: Pst
: •••••'•• (in.Ho)
Test Time:
t (min)
(R,8
12. And
Stage
(mg)
13.
Brinks
Stage
(mg)
\.\
2
Filter
2
0.20
Filter
(R,8)
Cyclone
Probe
s>
\
,oS?V
or
7<
^
-------
333
PARTICLE SIZE DATA SHEET
Type of -Test
1.
2.
3.
4. ,
5.
6. ,
8.
9.
' ^JV7~,-7 . (A,8)
^^^ (A, 24)
/yXs&vj*«^ srr* » » ^O- — <-'•<-£>- <~L-//il,i/\ /sW-y(A,24)
/
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^Z^^f,^*/ ? °? (A, 16)
t_&&'4'y4f:.&^
-------
TP-3 Scrubber Outlet
-------
Particulate
-------
/
IFIELD DATAJ
PLANT
DATE
SAMPLING LOCATION
SAMPLE TYPE f E>X> -
RUN NUMBER V
OPERATOR >fc6/r<*
«3c/-rt-g T
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
ST ATIC PRESSURE, (Ps)_
FILTER NUMBER (s) _JS.
/,
>. Y Y«g ? MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
VELOCITY
HEAD
(AP$). in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
STACK
TEMPERATURE
(TS),°F
DRY GAS METER
TEMPERATURE
INLET
OUTLET
PUMP
VACUUM.
in. Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
Go
£.6
f .
5S
66
7-
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0
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do
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20
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70
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76
30
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COMMENTS:
ES-041
-------
A «TT S"/ 7 - / ~7
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(Vml. II3
VELOCITY
HEAD
(Apjl. in. HjO
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in H20l
DESIRED
ACTUAL
STACK
TEMPERATURE
IT$I.°F
DRY GAS METER
TEMPERATURE
INLET
«Traj..»F
OUTLET
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
.«? (2
/.7sr
S.o
7.X Q95/
A- -
74"
"?> 3 -
300
Z£_
r
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0
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s-
S'T
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38352
"38353"
38354
42
-------
FIELD DATA
PLANT
DATE
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
OPERATOR
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE, (P$)
FILTER NUMBER (s)
TAG-S -
/-
PROBE LENGTH AND TYPF J& ' ^ 5.
NOZZLE I.D
ASSUMED MOISTURE, %_2^
SAMPLE BOX NUMBER O/
METER BOX NUMBER S-^J
METER AHg /. o u»
C-EAGTOR-
PROBE HEATER SETTING /Oft
HEATER BOX SETTING 3<3g »
REFERENCE AP ,^ ^
SE POINT LAYOUT
HIIIIITFS
/
TRAVERSE
POINT
NUMBER
SAMPLING i
Vi»i- •
TIME, mm
CLOCK TIME
2*h'
GAS METER READING
(Vm). It3
o.
VELOCITY
HEAD
(Aps), in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED
ACTUAL
STACK
TEMPERATURE
(TS),°F
DRY GAS METER
TEMPERATURE
INLET
(Tai in).°
OUTLET
PUMP
VACUUM,
in. Hg
SAMPLE BOX
TEMPERATURE,
°F
IMPINGER
TEMPERATURE,
/."S
2-5
70
-TO
£.0
s. .
20
/a
Go
// 35-
70
"7(50
• 37
-t
/.
;?. 7
sr
7"
o
JM.
3^>o
/.r
76
"7S"
7.
7-5"
10
•53
-7*2
JL
JZ^.
/. 7
-5-3
/oo
<8o
CJ
JA.
^L
a. 7
/oo
l.o
1OO
n
Q.
/y
.77
77
55"
l(?. %0
A3
/ 3
"Sao
r^n
/"W
dS_
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16)0
cr
r?
2-5
^JL
-7.0
7,0
3.3
tso
/. -7
3-3
loo
c?
COMMENTS:
ES-041
-------
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
« II3
VELOCITY
HEAD
IAps>. in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH). in.'HjOi
DESIRED ACTUAL
STACK
TEMPERATURE
DRY GAS METER
TEMPERATURE
INLET
«Tmjnl.°F
OUTLET
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
./"X
a.
-7.6
'0
0
ii
nil
sr
too
C..O
•a
1 1/"/
. 5 y
100
cs—
I/I
/7/7
to*.
ICO
5s
113.0
III .
,77
0
m
A7S
5.0
jLJL
2J_
6.0
.112
CS"
'f
^ s"
loo
r
r
/O 0
"/7V/
106
30
7. 0
o
3. r
10 0
n^i
iW. 40
ioe>
JLJJ
/Ob
38357 >
38358
38359
-------
FIELD DATA
PLANT
DATE.
PROBE LENGTH AND TYPE/0X
NOZZLE I.D
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
OPERATOR
ASSUMED MOISTURE, % .
SAMPLE BOX NUMBER.
METER BOX NUMBER _J
METER AHC
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE, (Ps!
FILTER NUMBER (s)
V
/•
- /.
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA FVFRY 3 MINUTES
PROBE HEATER SETTING
HEATER BOX SETTING
REFERENCE Ap
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(VJ.lt3
VELOCITY
HEAD
(Aps), in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
STACK
TEMPERATURE
(TS),°F
DRY GAS METER
TEMPERATURE
INLET
7.S'
COMMENTS:
ES-041
-------
TRAVERSE
POINT
NUMBER
CLOCK TIME
SAMPLING
TIME.min
GAS METER READING
.¥„.. It
3
VELOCITY
HEAD
lApsi. in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. HjOl
DESIRED ACTUAL
STACK
TEMPERATURE
DRY GAS METER
TEMPERATURE
INLET
«Tmm>.°F
OUTLET
(T">ou.''°F
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
op
IMPINGER
TEMPERATURE.
°F
B-
75
. 78
rr
5 /
tf .
J4-
AS
7.7
10
$"7
(.02
It
3-3
116
0
CS"
(to
/. 7
3.?
C5"
, b
-2,00
no
^2L3L
X 7
96
«- > . /
//*/
s~s
It
//s
74
0
Q. 0
o.o
- 0
o.o .
56
/;/
/7A/
0. 0
. 0
. O
H
. go
x.sr
/to
/t,
y?
A6S
I/O
Ij
to
no
AX
/U
j3L
33-
Sb
10 G
T3i
/ V
76
^J7_
^3_
rr
Ho
^i.
_o
3-7
~7G$~T
3836Q
3 8361
38362
-------
Particle Size Distribution
-------
PARTICLE SIZE DATA SHEET
Type of -Test
1.
2.
3.
5.
6.
8.
9.
V
_(A,8) Job Number
(A,24) Client
(A,24) Plant Location
(A,16) Unit Tested
(A,16) Date
(A,8)
• (A,8>
(R,8)
(R,8)
(A,8) Test Condition
Ambient Temp.
~/t"'3 (A, 8) Test No., Stack No
: (A,24) Test Location
^ (R,8) ( (R,8)
Bar. Press: .Pj-,.:-..... And,-Impactor Press. Inpactor Temp. Part.
(in.Hg) ''•' :j- . o'^tfer.. Dr°P (Brink Impactor) Tj (dag F) Density
;fe.-v:..^t^St:-:Static (in.Hg) , . , ' (gm/cc)
'•'• •'••••?• *•?}?'•?*"&•.;;.•"•:•'.. . • .-. .•••'.
10.
11.
% CO-
(R,8)
% 02
(R,8)
f,: % CO
(R,8)
%H20
(R,8)
(R,8)
-. "' Sample Rate:Qn . Stack Temp.: Tst
:.^: (ACFM-),, . (Deg F)
Static Press.
Duct: Pst
(in.H20)
(R,8)
Test Time:
,.t (min)
tei-
^
Filter
, ,
BtinKs-'.?!! Filter
Stage v
(mg)
Cyclone
Probe
(Rr8)
-------
Visible Emissions
-------
REPORT NO.
PAGE
'-• . . VISIBLE EMISSIONS FIELD DATA ^ri-k(T A-^-3. •
Date P ^TfccVc Wind & Speed S e~
Stack: Distance from 3*0' Height $"0 ' Direction' O - •' 0 •*/';+ ^
Observation ]
Commej
^
o
/
2.
3
^
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6
7
8
^Jls5t<;»i"iri**fi»>
• ' •••" ' -j^--" '• •^;^^.-55tS?«r:- •-
- % Opacity . ' ••>'• . v^i^^If^'
- •'.'• ,' T#/Wiira5<#*vit i'"
•"."-•;• •?$&%£&%?£ ••
/^ 3O -^S ^( O /vTJ 3O ^<* |V^ O Xo" 3O 4anlf^
•(}p |A;" :^2il3'^ c-i !675";o/j i42!c?r by"! c/ior
<9^ • /o !/T? ' .23 ["O*? ^> iC^ ic1^1 43'^" .' <2^>" !C3'*' ef^""'
/i? /J I/O' 24lr7.5* o -•»'!£?;> ,0^,^ 44! ^r | /* to?" /j^ 1^. '"^v-'^i 'v>'.
/O JO Ja.\ S.S-\(}f O'f \cf ^ £-£\ /c \ Of '&f C^V^^^^j^
i f* i **. ' f\ i / .^ ^ ***^ 1 ^ "*T^ — . t*S A y ( >-^ I y o «*^ •** i -\ v"^^ rV'"li'T*a^-^*'^j*i?' '•• ' '• *
/O /O /° 2j# 0$ C$ \0^ 05 ^-0105 1 Oj O'j L'-> - r.'-"^^*^' ,•-.!«.-. '
cf\cf c*f\ 27-ic5' of \cf df\ 47\c'f\of of cf^'^ •" "'• -.v--;"-
of\G^"\cf-. 2.3\Q~* ^ *of o£ AS \of \of &1o>"\
0f\ 05
OS" \of Of i 3Q\ £>? C$ 1 (if ! O'/ 5-/|cri tJSXl«X Os-^
10 to^l/o i/'& ! ,2~ 10$" 05"! o./ior i.~-?!r)t^i^'^i c^o^
/p l/o !/o jo.\ 2^\c.f ofio^o^ -^r^ c>ri of o.^jorT
/(?
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/T-rbr irV" cr O<"
/O j/o / -€^\cf\0f 0< df
10 \af cf- 36 Chios' \c'f of sr£\of\*f o-' of
olios' \o£' i 37 IDS' &f\of ^f. ij— H^rkr ^ c^" •
C&.\o£ Of \ JS !o/ i 0> \cf £> ^SOflofio^Cf-'
QS cf\^\ \23\cf i/° i/« /o ,5*
-------
REPORT NO.
PAGE
. . . VISIBLE EMISSIONS FIELD DATA j>$b$ ^ ^o • '
Date ?/zP/-2<) - • ' Job Number J-ttfT-f 7-
Obser-A
. • Obser<
Stack.
Obser^
*
Commei
/er LOueB^enZ^ Plant •& Location o*r/cf *&
nation Point A=-£T(-f ,?p Cfocfc Wind & Speed £""-/ j*V»»//v
Distance from ^ *rt ' Height T2> ' Direction- ' lYl#ifth( ^
/ation Be~gan COioT: Ended Sky Condit-'cn ///£•/•/ &>?/?.<;
^
0
/
JL.
3
^
^~
6
7
8
^
/o
//
12
/3
/j-
x^
/£
/7
78
/?
its:
% Opacity
O }$ 3o -4£" **<& O /£~ ~>O\ ^-Si !/'V\i O /o" 3O|-4a'
ft'f Ch O'y' O^~ z.c> c^"t^ jiy \ /& i 1 4o f '-?/ c5" &f\i*'
Of of )0 I/ft i 1 2,' /c1 o< os'! o^l 141 I /o /o ,o i/o
yO !/o /O /° 1 U2 0^ 0 /o as'le^!^ fif\0^\ 145' ' /O /O i/o I/O
/O /o /a /o i 2.^\Q^ \f7i^ of\o<^\ 46i/0 /^ !/D I/O
/O j/ (3 /O /o 1 27 iO? /o \/o \C^\ 47 VO 10 0-f\ 7< .
10 Jo /° \O'T\ 2.% o=^ C"^1 O'Ti0^ 1 kgi(^<^'. £><" cy|j><'
^5" Of o<^ o^ 1 2s? . o** lob'' cs-" ! Oi''i |49ios^ic's' o^iCsT'
iJ'f OS' lOS"^ 05^- 2.O.O^ i. 05' ! e^! /o i i.f-^loS' of !tr i Dol;>
OsX (?5^ O/ *:f 0< | 0V
D<5" iof /O I/O , 3c~ ovx 0^ cfio^ !o>"'b<''
^^ O^T OS" '0 | 3
-------
REPORT NO.
PAGE
Date
Observer
Observation Point X3o i?7U
Stack: Distance from
Observation Be~gsn
VISIBLE EMISSIONS FIELD DATA
. * " ' Job Number /- f >"/ ? -/
Plant £ Location
Wind & Speed_
Direction- ^
_Height_
Ended
/)
Sky Condition.
Opacity
so
so
O'l"
20{0«T 0 O5\ 0 to} i ! ?-!
17
18
0
-------
REPORT NO.
PAGE
Date
Observer
VISIBLE EMISSIONS FIELD DATA/m^cT
. • ; ' Job Nunib e r_/- 957 ? "
_-__ Plant & Location^'
• Observation Point fOc/iTk c^
Stack; Distance frcra ^£2_Hsight_^
' Observation Ee~gsn 12'^ ? Ended
Wind & Speed /o -
Direction- A
Sky Condition PT/y 5>
Opacity
5_
T
8
/o
/jr
t /O I/O I /
/o \/0\/O\/o\ 1-s.f \Op i ob toj j°5 U
0 .
/Q I/O \ \23\03 1
o/1 o :>'.
fl^iaf oy-l .c'0 I Of
/O !
j 10 '-/o
0< Jfe'-) Os !
o>
0>
/«=...:
.! .f^f i /o i / o ;/o i
£"c Ix^' ! / O I j ,> j
l/c
LLof los
io
-------
• ,.;1£.£.&U^
'.'fttt£< >?"£3
REPOKT NO. PAGE'-'-^-vgr
•: '." ' . , "• '. . ;•'•/. ' ' . . . .; • . -:^v^-S
"1C^ -^ ' . • ' • ••"• VISIBLE EMI^^H^iLD DATA P*^ ^ . ,$g|^ ;
Date rP/Z*?/^? • ' Job Number /-^^^ -/ X'
Obser\
. • Gbserv
Stack:
Obsen
Commej
fsr LOtJtrBr^e?^*^-' Plant & Lccaticn^^-*'^ <^'fcf
/•ation Point /Vb/<7V 6xyiL ^Trf C_ ^- Wind & Soeed O"""/^ <*•»/*"//
1 * N
Distance from -> "° ' Height ^ Direction- N
/ation Be~g£n Co-o^e*^ Ended Sky Condition/^y S-^^y
^
o
/
2.
'. •-." ' % Opacity . '".•••••
*
I rv£>_, j i i>9>j i I i
o js 3oK£" lv\ o AT so 1^5"! f^\i o \ /s 3c\A£
O<) Oj' o5"|Q5^ Uo C< O^O'-J^O'yl Mo KT/I'^^I OS'iO^T'i
0 >x 0>" 0>"i?/ is,' 0 il ° ^ 0 / JO/' ! 1 4 M 0 '< \ 6 -/ ' o Si 0 yl
O/.'/O /-' 1 c?5l '2.2 i/^ -70 i /^ : 10 Ij-i2 1 0.^! C>' 05^1 °^'!
3 I/L''- /o /«?! /t>\ \23 !0\lc i/0 I/O ^-!^3!0 I/O 1 1 Arias' ! -^" io<~"iD<
^~
6
7
8
9
/o
//
/^
/3
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AT
/^
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78
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its:
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/D f'O /o | /c. j i? ? rO^ jO^J csrl O'^l !^Sl/Oj/'J> /^ t/o . r
/o I/O it??"^^- 12^ OSi ovios ! o' ^i? ! o^i- |- :? c ! 0 > i -0 b ; 0 •? i (j/ ! I -="5 i / o I /O : P i ' 0 !;>
n/ 10^ of i a*' • ! 3 ! &:» j o^J OS-7 i o /! ! - / I/O ! 65" i o/".i ^ !
^ lo/ !<0>^ ! o/ 1 ! 32 i c $ i 6^'. c/ !f <' i '.<•.?! of ! Qx OfltP/'.'CXf'. !2_? C^ OS !^3!CK J OS 1 ,-7^! i<~c b<'!c>^'n<1 ^>"'
O/IOT Gv'lO^i iSTlC1? 0*» 05!°^.! !5-7ii?Slc?^ io^ i t^
C^>xl O/l 0&\ C^ i^cO^ of Js! o^i !c*=!CS''i t>'' ;c' !fj;^0^ t>S °^ !/o ! ivT°:OS j fr'V>ri nsT " """'•
• • '• " ,~'""-
.
'
-:'\'' '*••'
-------
REPORT NO.
PAGE
;. . ;,'.' VISIBLE EMISSIONS FIELD DATA ' f$i*-G J" Y- > • "
Date F/7^/>1 ' ' • Job Number /' ! ''-i.3' ! !' 1
-T
^~
6
7
8
9
/o
//
/.?
/S
c? xo!c^!^5"i ! i
liO 0-3 OSX|C?< !2,
-------
REPORT NO.
PAGE
.- ,'. VISIBLE EMISSIONS FIELD DATA /'/46-tT /<•"£ > •
Date tfil.?/'^ .- •' Job Nuniber /~ ?'7?~~/7^ —
Observer (-A->^- ^7^ (f ^ Wind & Speed O-/c>
Stack: Distance from >oo' Height ^ ' Direction- ' /O^
nP ~>^P •••/•>'
Observation Ee"sanu^ <-(7^ Ended Skv Condition P "T/^ S,-~^v
.-
Commei
^
o
/
2.
.. . '.. '.' .' . '-' '... • j "^-' • ' ' :' ' . '~ • ' ... " .,. . ^OtlQ^j-i
.•••'•' • •• % Opacity . . '
O y^"x'3o ^£ rvU ° /-^ SO I -4^" P^\i O /S" 3o|4i"
CP^ ^^ C?>l/^ \2.O\Vy d'y\Q\G^\ \^\ IC'S o~6 c^\c^'\
/O !y^> /^ /«9 12.2 icy o^\ G<^\! //> i/O 1-15 lO.^'^ i x ^^.^f
•<}•
-T
6
7
8
9
/o
//
/2
/3
/A
/&
/&
17
IS
iy
its:
O^ 0^ 0^.^ I24!oi' o/i^/i^! \-i£~\c^ OJ oyic'/T
0^ o' 0")f ! 25!o/k5/ \vf\cb \\£-£\ rtf O/ o*'j o/1
o^ to^"nsx r^ (2.4b< O? o4\o*'\\At>\of oS orttftf
Q Si 0^ 0->^ c?^ I 2 7 UT^ ! Of? 0x !^>x! cvf
o^ -o^ c?S^ CP'^ ^2. ? 1 (i^l r^! o ^\o5 i \^-^\ ,^^\ f)^\ £o"( t?sr^
e?1? c?:/ c^ n/ 12s? Icr^i &•£ o:j\o3'\ !^--? ! "ic,^io$x': ! -^1 n^\ fjf '\r>^\ of^'
9< ty^\<0^\^ 13/io/le?/' ^i°^ ! j <"/ J5< tffjo^l 5^!
^9"T \cs\&4 ln? ! 3^ so^ !O->' iO^ ! CP J ' •*".?! c< ^> ;c? b"'- c?"'!^
C^ b^X |(?<<^")^' l3f!C?i jC-b G^1 ic:> I !vT-?!(9>'' (? ^' O <• d"1^}
0^ ob o* 06 !34!C-o o5 lob'ic1^! ! c~-'0^\^>^ 0^\°^
c$ of ^ of i 3-TlOef L-:f 0^\C^\ !.5£-| /o /c? /O i /n
/?/ o< c?^ c< \3~ los" ii?/ o^ I o^l l<"ci/o /'l ! 53 I/O /i /o 1 /^ i !c"S'/c i /c i/o !/s
&sx ^ ^l^ |f-i/°J^M/^ !/^ 1 ..5^:/c /o /c |/n j
» ' • . •
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.-•••' •' - • •'-•"%:' •
• . -'••••' • • •"'"'•''.•"'.
-" '''-ST..' '
-------
REPORT NO.
PAGE
.. ... VISIBLE EMISSIONS FIELD DATA ftiL ^ ? 6-^.5 '
_ 9 I ^ i) /3-'i- ' ,- ,^ ^ 1
Date * t i' f ' ' • job Number/-- y 7/ ^ -Y^ J
Observer CvOL~fcfc(r<£- • ; Plant & Lccaticn c-r/~f rfM
' . • Observation Point N>°/t7\ ^ <57^c,c Wind & Speed 0''^
Stack: Distance from 3^*0 Height <7~"Q Direction-' A^^— '
' Observation Be~g2n CcA'f;^^ Ended Sky Condition /is> ~V CV^-cXy
• .;
#
Commei
^
0
/
2.
-3
•^
,5"
6
7
8
«J
/o
; : -'..'• ' -•'/ . ' •• '•• % Opacity . •. : ' " . ".
•
|N?> 1 i !>C>- I
o ;s 30. -^r r^l o /s- so.Ur ,r^\l o /s BO 4r
o/ 0f |fl>' of , \ao\oZ d> /?/ 1 o;fl Ma f/^ 1 /0 ^J 1 7^ ' •
°> 'ic^JDl^j C1^ 1 £3 ^ l^x-'^i-^.xi' !— 3'r-;'"l cr 6'>5'Tc/T
j>3xib'5|C3 o/ !24l^-y' n-^ !OJ> l4-il/;>'"l^y^' '"
Ob 10-2 /)*) \0f^ ' ! ^5"!/^/ *i' nT'T^j «? ^ | <£-£* ! ^J^ 1 i/y c/y ojT
f- r i o i<^7X ^*> U ' 2. ~f*. \^-o i o^Tci" ^>'" ic7-?^
c>T \o^\o^ \O<> i 2 7 le^.l o>x '^>x 1 /- (4 7 ! c->" lc>.< '^ i c>->~"i
os<1 0?' ^ 0/x '2. S i O-^' id !/0 1 /6 k5 i 0'/"\ of of1, af\ .
O^ C*f \O~j &5\ ! 2^ i /O i / £' /^ ! /£>' 1—9 1 o r i o>" joy'' Q'J' \
C") 0? \Ovf fft \ ! -:- - • /^ 0 ^ ' O> ! c.y^ ! 5"3 iCV'' j c>$'"^rov> i <^> :'
// |&/x £/"l 0< /° ! -3 ! ' «.'^ ^ j?^.i 0>"^ ! 5"H cf !o's.x ie>'5^ c^"^
12
/3
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/r
/^
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/7JO< C>X^/ ^^ !ST!o> o^ W i c>" ;/•• 7i/o |/t ,t3 /o
7P
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its:
?7SX ^ IrJ1^' D1 !i-=i/'o I /toi/o /c?
c?/ h< 0"?X| 0-' lfai<3i iOr:/6J !/* i><-0:/o j /-a i .^ /o j
,•:...:..-.
» *
-------
REPORT NO.
PAGE
. • VISIBLE EMISSIONS FIELD DATA /^C-t $c^L.2>'
Date oT/2-P/TP ' ' Job Number/- £ rf 7—f Z-
Obser\
. • Obser\
Stack:
Obser\
Comraej
?er LA-"Jir1t?s^<'2^- Plant & Location o<-~rf <-f y^^y
t
nation Point /O otfTK (f^. <^7V4-tA_ Wind-S^Speed O - ^JMS/r
Distance from ^rt/;-- Height ^ ' Direction • ^^
/"* '' • <>x ' / -/
nation Be'gsn C-o/\-t(..\)v**XEnded Sky Condition fiT/ ^ C/ouJy
' ', •• •'.. '•'
^
o
1
2.
••^••••M*
3
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6
7
8
9
/o
O
o«>x
P^
• - •" . . % Opacity ^SEB^' '•.'••.
/<5 3O -^ £" ("c^,! O _ /j~ 1 3 0 1 -4 ^* r^^i O /,5" 3 o i 4i"
i.O5" O^ ^b" IsoJcJ/ 0'7^io^xi 5»/1 Mo f i
of n^ oyf \-z.i\Q4\,0'f\tri'\vf\ 141 I I ! !
^/j^ ^>Xlo<1 :2.2 i/P^'^^io.^! ^.<"! o/' 123! n<7^Qf\ °r\ is /TT^-3 ! ! i i
D-S"
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f
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78
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its:
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^
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TP-4 Transfer Points Hoods
-------
Visible Emissions
-------
REPORT NO.
PAGE
VISIBLE- EMISSIONS FIELD DATA . '
Date 9~28~79 - Job Number/^/— P.T'/T-/'?
Observer /^ £) A/£r Plant & Lo
Obser\
Stack:
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA
Date 8-2S-79
Observer
Job Number fl/—
Observation Point
Stack: Distance from A/A Height
Observation Be~gan 093fr Ended
& Location
Wind & Speed
Direction''
Ml
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Opacity
8
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA . '
Date P-2,3— 79 Job Number O/-~9*?/~7-/ ~7
Ob sen,
Observ
Stack:
Qbser\
Comraej
rev JL.AA/E Plant & Location H£"j\fag%. $(?/ '
ration Point 7?ftjMAf(y C^cAT/V^^ Wind & Sneed AfA
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA
Date 8 -ZS -79
Observer
Observation Point
Stack: Distance from _
Observation Be'gan J3
Heigfrt
Job Number ^/-/r/7.
Plant &
Wind & Speed
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Ended [4-3O Sky Condition,
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to
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io\
-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA
Date 8-Z8-79
Observer L. /\ A/£~
Observation Point
Job Number al~
Plant &
Stack: Distance from ^//) Height
Observation Be~gsn / S 2,S Ended
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-------
REPORT NO.
PAGE
. . . ..'.. .VISIBLE EMISSIONS FIELD DATA . ' ..
Date #-:Z#-79 • Job Number Oi-9Fi7-l 7
Obsen
. • Obser\
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nation Point PfiiMftRy Z-RuSH&Z. Wind & Speed A/tf
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Fugitive Emissions
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rfitfx- HcflfytfcoV ^QQ # « #/ . ^$77 - / 7
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TP-5 Rail Car Unloading
-------
Visible Emissions
-------
REPORT NO.
PAGE
1,
VISIBLE EMISSIONS FIELD DATA
Date /F-«?cf- 7*9 Job Number / -7^.^r h ££fj5ft£&
Stack: Distance from,-2.C Heig
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA
Date P-3-^-r^. Job Number /~'7^/7~/7
Observer /fc^c/ • Jft Z7^,/'.:,Je
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-------
REPORT NO.
PAGE
. • ' . .'. .VISIBLE EMISSIONS FIELD DATA • . *
Date ?r - £•£—•'??• • ' Job Nuniber •/- '? *~/?-/ 7~
Observer / 1 /? i 2 ,' ! ! i 4 1 I i
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-------
REPORT NO.
PAGE /-<;
VISIBLE EMISSIONS FIELD DATA
Date tP-<2.r-7f, Job Number /- f. r/7-/7-
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-------
REPORT NO.
PAGE
. • ,'. VISIBLE EMISSIONS FIELD DATA
Date
Observer /^C// /s6.3T~71,J' , Plant £ Lccaticn^'^^/^Tv^X^ /
. • Observation PoiiitX^-.aZ/v;' ffusdio /^-Aipf^^Wiiid & Speed fi//-£
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o ,-'•) o i f) 1 2^"i /'-> O \ O n '' ••=£"! 0 c? 0 ! /->
c- \o o\ :? ' ^= ' ^ j o t /> /? i 'r^i r> •- o !^
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./ - ' ^/ *^ y/
-------
REPORT NO.
PAGE
;i
: -..'• .- ,...'. . VISIBLE EMISSIONS FIELD DATA • . *
Date &-^%'~"*?J ,, • ' Job Number •/-<-?<";?-/?
Obser\
. • Cbser\
'-i^'i^-i/^ • x^
Sleeks
Gbsen
•* •
Ccmmei
fer >f>^X XxL^??]r^- 7 Plant £ Lccatlg^'^X^^V/r.^
nation Poinjj^^_yii^<"--x^o.<,, /2v<+2- Wind & Speed ///*
Distance frcm^c Height^/!//? <€? Direction-' //'/J-
/•aticn Ee~g5H /5 .&tfy Ended /X/^V Sky Condlt^'cnX/^.^-/'.
^
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5.
3
4
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6
7
8
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/7
VS
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its:
% Opacity . . . • .
o /s so -4s- "^1 o /^- so Ur! f%^| c /o~ sc(4ri .
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v? 1 ."> .^ 1 /? 2. ? i O i? ! /'^ i r- * \±%\ n n ^ ' .0 1
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y.y • ' i • / s s
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-------
IJ "2
REPORT N'O.
..";.'.' VISIBLE EMISSIONS FIELD DATA . *
Date /P~ J^- ?'9 / . • •' Job Nuniber • •/- 6?rV?--/ 7-
Observ
. • Obserx
•o;-. • JL /-
-Sfeack:
Obser\
' • *
Ccmmei
*=rs/Jj t^/jJL. /I
rer /fs^cs Ss.ttssM <-> Plant & Lccatica^" ^//^/XT/*^1
Cation Point^^-^vT - xyv.^r^ ./^y/^^^^Wind & Speed A, /^
Distance from ^ f Height^X/// ^ D^act^on- /f /^'
•aticn Begsn //.',7^
^
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2.
-3
•^
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6
7
8
9
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//
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X^"
/£
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78
/?
its:
.' - .: '. . ' . % Opacity . '".'••.' •'....:•
O J5 So -T£" *^\ O !/o"i So 1^5") !"^>\l O /.5" Sc|45"|
t^/ t- ^ • ^J j
O C' .;*> 1 J* 2 ,' ,O I .^ 1 O ! £ M 4- 1 ' JT ,-Z O ' r?' '
.-> 1 ,~ - 0 ! D '• 2.2 i ,-^ ! .--) i (? : {? i i -2 i O -1 ^ \ .9 •
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'^ ,,^/^J.:?~'-&i<^!L ~.,.^s:./s^ ~?_ ^f,: /*V
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Fugitive Emissions
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.
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n
u
; crp:0V_''2A
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TP-6 Crusher Building
-------
Visible Emissions
-------
REPORT NO.
PAGE
Date Oft- <3 8
1U5
sp
tic p>
e^o(s>
Of
557
^
VISIBLE EMISSIONS FIELD DATA
— rn Job Number Of
Observer BarbarTX- T>
• Obser\
trusH-er-
S^feeefe
9
C.JiVrux%, fYiclubc&nurn n^'dl
"UmnrxOr^C'l Plant & Location He/v^zr^on A?
ration Point ^ /£"$ '-flK IK! ~fr
in^of
Distance from^/57'-mIei^it-/
Observation Be'gan Q ' 3 3 Ended
t P-
,^"^ I
1
1
Comraej
^
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3
9-3
£
6
7
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12
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17
78
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its:
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-------
a<
cJ .
c—j
INl
-------
REPORT NO.
PAGE
V
VISIBLE EMISSIONS FIELD DATA
Date nfl-<3R -
Observer
Job Nuriber O[r9£V7-/7
X* • » ™*^™™^"™^^*^^™«™^™™™**Ji™ 9
Plant & Urn
Observation Point /WSZ^Q-- Uhritj
'' ~ - 4^ g ^~~~ —_____ s3T
T? nxx«d( A • —
£3
-------
REPORT NO.
. . .,.;. VISIBLE
Date Oft-£A--?9
Observer Fhftrbdr^ ~D<"U
^ • Observation Point ^/S i) -r/"-
(jru£hLr~ f6(Jd IdU. t\Q (
S*eek: Distance f rcm^/^Z)/)
Gbser\
II
Comrnei
C£>rnVuc£cl ;
/ation' Ee'gan /Q/ 3 3
"7T<5lfK* 'r
Or&S/\&/--'
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6
7
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0
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0
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0
0
0
0
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_£_
C£U5^6^ -TEST" W'l\ '
mrnondL Plant & Lccatacn/^^e^-^on (*5 ^
v P . /> j3£*T#j2. h^-suctjL 1
inirGnhor Wind & Speeded *j£j*j>^ -f*^ 1
l/"&S^u2T"~ felokt ' r
fWei^it -c/ y^*^- > Direction- ^(9tcfc^i
^ Ended //iCTD Sky Condition ^Lwruj fdb^a.c "
_ ^ ^-^^- ! !
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U- . . ; •
-------
REPORT NO.
PAGE
5- <£jj
Date DP -
VISIBLE EMISSIONS FIELD DATA
' ' Job briber 01-95H-/"7
Observer fiflrbortx
Observation Paint ^
- in
Distance fron
Observation Be~gen lot'
Plant & Location
Wind & Sneed
Height A; 7S"ffi. Direction •'
Ended /3-c3^ .§ky_Condition_
.••R'S~A
-------
REPORT NO.
PAGE
se&AJdSOFF-
VISIBLE EMISSIONS FIELD DAT
A
Date 06-^8-*^ • •
Observer feAr-bar-^: • "DriA.no rnorvril
. • Observation Point 'W5T?
Cruskor
m
Job Nunber,O/~9571-/7
Pla^it £ Lccaffc^'/JFn^r:^) , (°^,
Wind & Speed .xu /Gry^k^
Distance frc.i
Observation Be~gzn
-u&ter-/S»/rf3 - / 7/ j
.Heigjit_/^2£j&' Direction A/6 Q
0 !O i O
OOOO -3^! 0 0_ 0 ! 0
: 0 I O i O! O
Comments:,
LXx-^L^
' • ^ " * •
j/v-i^'S'' ^f affl/ax:
J;. g Do
&
-------
REPORT NO.
PAGE
Date Oft - ;
Obser\
. • Obser\
O/usKfi*--
Staek:
Obser\
mam
-» W
Commei
Or
rer fef
2B
A^fc
. VISIBLE
CLhC
ration Point A-
x% P i 1 «e it CT '& -^t^r^ ^"t "* )i!>_ IT***. 'r^L ]
C*x ^^ L/ w^ it' ^> ^^ "^ | C^ ^^ I ^^ [ & * j_j^ y
SpR_A^5 OFF
EMISSIONS FIELD DATA . *
Job Nuniber Ol-H^O-lT
*. f. ' • C/l'inncxy Prvol ubobi^cx^Vi f^\
X^, ur~(} iY)fY\Gr\dL Plant & Lccat^ en U^wWar-^^^ P,
'/67)-fr.
/ibu i IcU r\cj (
Distance from /W/51^
ration Be~gsn A/ji23k
"*>:£2
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;
2.
r^jn mm
3
^
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7
8
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-------
REPORT NO.
PAGE
Date
VISIBLE EMISSIONS FIELD DATA
• ' Job Number
Observer
.
Plant & Location Me/vi*rSc
Observation Point
S-fesek: Distance frc
Observation Ee~gsn
Wind & Speed
75>p-f. Direction A/LO
Ended (b: 98 Sky^Conciiticn SlUVUj
' ^-~" <~'
Opacity
-------
REPORT NO.
PAGE
Date
VISIBLE EMISSIONS FIELD DATA
.• • Job Nunfcer.
Observer
mr\oliA
Plant 5 Lccati'iA
Observation Point
Distance fre
Observation Ee~s
Wind & Speed_
Direction •'
Sky Condition^
cv\ p< 3>
^
c
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Comments:
c*<
/s
-------
REPORT NO.
PAGE
QFF
VISIBLE EMISSIONS FIELD DAT
Date D&-
Job Number
Observer &Q.rbar2<
0 O i O
0 I 0 i OIO
O i 0 i Q JO ' !26
0 IP I 0 JO I I27i
17
IZ
0 I Q Q {.Q.
Of 0 I 0 I 0 I I3g
0 in 10 10 i 137!
0 I Q I 0 I O M 3S I
141
S43i
!47
0 I O i 010!
Comments:
^f^-^
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/-es-r
j^J\>Qv'>
t^
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-------
Fugitive Emissions
-------
.. Gki> No. , Ol-9S~n ~J3- jyimx*.
_^
ttS ' firus Ka-*" lou^LcUnct
~" ..... " •-•.-— ....... -- ..... - J— - ..........
Period '•
8-L3.3
IT6ST
, PuM4>\K^ "6m'f5>s'iDAS (
iv ^J
-------
Train Processing Schedule
-------
ol»^^
l m g'S
mirL 30
(0
1Q_LIB_LOO
/01_£9 L^e LQjLfel
~hrcu.n
-------
/
-------
.fslo....Qir...-
Climax.. IfTifi^kdju/uLuvo
s OFF
-T&J&LUS.&&C-
J/n/Vi.
.13 8
]K._y^id-cl^i.._.dr/.j^cs
-------
Pebble Screening and Milling
-------
TP-1 Screen Exhaust Duct
-------
Particulate
-------
FIELD DATA
PLANT
DATF
SAMPLING LOCATION
SAMPLE TYPE A-i
RUN NUMBER L
OPERATOR L
Z/i./7-. / &P\
,
i, c
PROBE LENGTH AND TYPE _
NOZZLE ID 'I'i/-
AMBIENT TEMPERATURE .
BAROMETRIC PRESSURE .
STATIC PRESSURE. (Pj)_
FILTER NUMBER (s) _
ASSUMED MOISTURE, * -'7-
SAMPLE BOX NUMBER 2_
METER BOX NUMBER 5
METER AHj
C-F ACTOR _
•?.
//
}'
or
75
A-f
7 <;
?/:
loo
. c
107
1 '7
,"7
)&/-
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%
?0
2S^
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3L
Sf
fTs
3-
75
•7'
/&
.3.C/1
7$
&&
J4-
.?
^.
38116
COMMENTS:
ES-041
-------
FIELD DATA
- O
PLANT.
DATE_
SAMPLING LOCATION,
SAMPLE TYPE 2
RUN NUMBER
OPERATOR
PROBE LENGTH AND TYPE ...
NOZZLE I.D >. < *?
ASSUMED MOISTURE, %.
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AHn . y,
O_
*s —
AMBIENT TEMPERATURE _
BAROMETRIC PRESSURE _
STATIC PRESSURE, (Ps)_:
FILTER NUMBER (s)
PROBE HEATER !
HEATER BOX SETTING,
REFERENCE Ap
377
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA EVERY
MINUTES
VELOCITY
HEAD
(Aps), in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
iZ
'1,1
&
E
7.6
STACK
TEMPERATURE
(TS),°F
so
DRY GAS METER
TEMPERATURE
INLET
(Tm ),°
to
-1&-
&
OUTLET
(Tmoul).°F
1^-
jOO
0 2.
PUMP
VACUUM.
in. Hg
5*
C
-
SAMPLE BOX
TEMPERATURE,
°F
IMPINGER
TEMPERATURE.
°F
25
^
72.
ES-041
-------
cA
FIELD DATA
PLANT
DATE
PROBE LENGTH AND TYPE
NOZZLE ID ' / cl (
ASSUMED MOISTURE, * <2=
SAMPLE BOX NUMBER -2- ~ I D
METER BOX NUMBER
METER
SAMPLING LQCATi
SAMPLE TYPE
RUN NUMBER
OPERATOR /-
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
PROBE HEATER SETTIING
HEATER BOX SETTING
STATIC PRESSURE, (P )
FILTER NUMBER (s)
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA EVERY
-------
Particle Size Distribution
-------
- c •
PARTICLE SIZE DATA SHEET
Type of -Test
1.
2.
3.
4.
5.
6.
7
8
9
_(A,8) Job Number
(A,24) Client
2
_(A,8)
(A,8)
_(A,24) Plant Location
_(A,16) Unit Tested
^(A,16) Date
(A, 8)
Bar. Press:
(in.Hg)
(R,8)
(R,8)
Test Condition
Ambient Temp.
.(A,8) Test No., Stack 'To.
(A,24) Test Location
(R,8) / (R,.8)
And,-Impactor Press. Inpactor Temp.
Drop (Brink Impactor) TT (deg F)
. Static (in.Hg)
Part.
Density
(gm/cc)
10.
(R,8)
% C02 .
(R8)
% 02
(R,8)
CO
(R,8)
%H20
(R,8)
2""; ->'^-'Sample Rate:Qn Stack Temp.
*;..' v5.; (ACFM). (Deg F)
(Rf8)
(R,8)
Static Press.
Duct: Pst
';-.<:::".:,. (in.H20)
Test Time:
t (min)
(R,8)
Stage \ •. 1
(nig) .
13. '
Brinks Filter
Stage
(mg) .
8 Filter
(R,8)
1 Cyclone
Probe
• I
K.
i'*o °l
-------
PARTICLE SIZE DATA SHEET
Type of -Test
1.
2.
3.
4.
5.
6.
7-
8.
9-
_(A,8) Job Number
(A,24) Client
Plant Location
(A,16) Unit Tested
(A,16) Date
(A, 8)
. (A/8)
(A,8) Test Condition
Ambient Temp.
(A, 8) Test No., Stack
,2V Test Location
Bar. Press: Pj.,
(in.Hg)
(R,8)
(R,8)
And,-Impac'tor Press. Inpactor Temp. Part.
Drop (Brink Impactcr) Tj (deg F) Density
Static (in.Hg) (gm/cc)
10.
(R,8)
(R>8)
% co2
11. 'o-<£^ (R,g
Sample Rate:Qn
(ACFM)
12. And. C*,6J d.qC
Stage 1 2
(mg)
13.
Brinks Filter 5
Stage
% 02 .... % CO %H20
I) /& " - (R,8) -~^/'<^' (R,8) "~7/. 2_ (R/g
Stack Temp.: Ts^ Static Press. Test Time:
(Deg F) Duct: Pst t (min)
.-.._ •'•• •. • • • ••; :.;- :>:;•;::> (in.H20)
', . (.11 loZ '0-34' t.U '•'•O.St, d-!£ fi,b\ (R,S)
3 . 4. 5 67 8 Filter
: (R,8)
4 3 2 1 Cyclone
..; Probe
38385
/10
-------
PARTICLE SIZE DATA SHEET
1.
2.
3.
4.
5.
6.
7.
8.
9.
7?
(A,8)
• (A,8).
(R,8)
10.
Bar. Press:
(in.Hg)
% cd-
(R,8)
Type of -Test
(A,8) Job Number
(A,24) Client
/Mfc-^
,24) Plant Location
(A,16) Unit Tested
(A,16) Date
(A,8) Test Condition
Ambient Temp.
_(A,8) Test. No., Stack No.
_(A,24) Test Location
m~.:_(R,8) _/_'_. (R/8)
And,-Impactor Press. Inpactor Temp. Part.
Drop (Brink Impactcr) Tj (deg F) Density
Static (in.Hg) '• (gm/cc)
(R,8)
% o2
(R,8)
..- % CO
(R,8)
%H20
11.
(R,!
Sample Rate:Qn Stack Temp.: Tst
. (ACFM) (Deg F) uuct: ^
.- ;-' ..' '• •• '. ';.;''. .-"- -..v.:; :£••.:•;: (in.H20) •
(R,8) gOJ (R,8)
Static Press. Test Time:
Duct: PC-+. t (min)
12. And. 2.37
Stage 1
(rug)
13.
Brinks Filter
Stage
(mg)
0.a
2
5
Filter
(Rr8)
1 Cyclone
Probe
//(? -
-------
TP-2 Bucket Elevator Exhaust Duct
-------
Particulate
-------
PLANT
DATE
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
OPERATOR
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE, (P;) ~ ^> 1.
FILTER NUMBER U) "~ "
-------
FIELD DATA
PLANT
DATE_
SAMPLING LOCA
SAMPLE TYPE
RUN NUMBER.
OPERATOR _
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE, (Ps» ri
FILTER NUMBER (s) _
W
^LTTJ
PROBE LENGTH
NOZZLE I.D. CO. I
3fit? "
ASSUMED MOISTURE. %.
SAMPLE BOX NUMBER _
METER BOX NUMBER
METER AHg L.
CFACTOR
PROBE HEATER SETTING
HEATER BOX SETTING
REFERENCE AP
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA EVERY.
MINUTES
TRAVERSE.
POINT
NUMBER
CLOCK TIME
"SAMPLING
TIME.min
GAS METER READING
(Vra). It3
VELOCITY
HEAD
(Ap$). in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED
ACTUAL
STACK
TEMPERATURE
(TS).°F
DRY GAS METER
TEMPERATURE
INLET
(Tmin)."F
OUTLET
PUMP
VACUUM.
in. Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE,
°F
TM
im
<2
-------
FIELD DATA
PLANT
OATE
PROBE LENGTH
NOZZLE I.D. f O.
ASSUMED MOISTURE, %
SAMPLE BOX NUMBER
METER BOX NUMBER
METER
c FACTOR
SAMPLING LOCAT
SAMPLE TYPE
RUN NUMBER
OPERATOR
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE. (P$)
FILTER NUMBER (s)
PROBE HEATER SETTING
HEATER BOX SETTING
REFF.RENCE AP
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA EVERY
COMMENTS:
3834 5"}- S
-------
Particle Size Distribution
-------
PARTICLE SIZE DATA SHEET
1.
2.
3.
4.
5.
6.
7.
8
9
* /*
i/J
-------
.
\; /(
PARTICLE SIZE DATA SHEET
Type of -Test
1.
2.
3.
4.
5.
6. /
7.
8.
9. ,
'^J~/7'/ ~7 . (A, 8)
^ '7&s1 (A, 24)
£*- > / ' / S" .•»
* 1 J M£ rf'' J J / f&t ^1 i* U "> t f
,/_j^C/L< ' .r /•%•'- y (A, 24)
c . .. /
X^^J-^/ ' •' •;.•'•'.!'• '' -i'-!.1-.- •' " " '
C^:;- (A, 8) / /^7- (A, 8)
^ ~i r>- ^ -'/=;-' -y ^ / ^ r^ r- &7ty/3 U3 .
v1 ><~^ «i- — (\)Lr£.'£(~ 1 i^L^£- ^ ft / £^~ \A,24)
^. /' ^ (R,8) /- 8)
02
(R/8)
CO
%H20
(R,8)
(R,8)
(R,8)
(R,8
Sample Rate:Qn Stack Temp.: Tsi; Static Press. Test Time:
(ACFM) (Deg F) Duct: Pst t (min)
..=•'•-•- •'• ••: •••'-.• v "-'• : :" -^"': (in.H20) - _ . . •
12. And.
Stage
13.
Brinks
Stage
_
Filter
-4
__
Cyclone
Probe
M7 (R,8)
Filter
-------
PARTICLE SIZE DATA SHEET
.-7/7si -
1.
2.
3.
4.
5.
6. X
7.
9^/?~/ ? (A, 8)
(^^^ (A, 24
Xs* -x ^ > ^ ^ /° /.//?? -? 7* «-f L\J
_^z, d*' .••-.;;. ^^2_£- .-.-.Boater tffgwni, &/tati&
9. _^
^ /- C- (R,8) X<^ (R,8) ' "7 £>•••'•""•
Type of -Test
(A>24) plant Location
Test Condition
Ambient Temp.
^(A,8) Test No., Stack No,
Test Location
(R,8) /
Bar. Press: PJ.J And,-Impactor Press. Inpactbr Temp. Part.
(in.Hg) Drop (Brink Lrnpactor) Tj (deg F)
. Static (in.Hg) .. ,
(R,8)
r, "«. -^W«-'---,-
Densitv -^^"^"^f'^s:
(gm/cc) »:«'
10.
11.
% CO-
(R,8)
02
(R,8)
% CO
%H20
(R,8) .
/•J^
(R,8)
(R,8) ~
. Saraple. Rate:Qn
•• ••' • fACPM'V" '••'-
• ^ .'f /.-. .V**^rC-*rA/J - ---^ "--. ..- ^
•Viv.S. ...>'V^i'>^;V!^-'irJ5:v-'; "
*:-^'.-«^i.'>!^^'-!- ••-.• -IJ.--.. . '
•f:*- ^,Vfc'^.v,-f-..i-v-;-: •.•-.:••.
:4jfr-;-^^r-:'"'-'V"^ :' .'
.^•: "Stage 1 2
13...
Brinks Filter 5
Stage
(mg) '<
Stack Temo. : Ts^-
(Deg F) .
3 4. 5
4 3 2
• .. .Vi , . . . . . ' .
Static Press.
Duct: Pst
(in.H20)
i.c£ ± '\,b3 (
6 7
1 Cyclone
Probe
Test Time :
t (min)
0-3 7 ft. .2-2- (*, 8
8 Filter
(R,8) _^,
go /'
(R,8)
-------
TP-2A Total Scrubber Inlet
-------
Particulate
-------
v*sri*»?i''s '*• •'
%i*fe,a*,v".-'*t"- -.
ES-041
-------
TRAVERSE
POINT
NUMBER
k2_
CLOCK TIME
13.
GAS METER READING
.vm..r.3
2
VELOCITY
HEAD
Apl. in. H0
JA
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in H20)
DESIRED ACTUAL
STACK
TEMPERATURE
(T$I.°F
Sa
fl\
DRY CAS METER
TEMPERATURE
INLET
us.
OUTLET
;oo
Joo
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
38141
,
1 (WINGER
TEMPERATURE.
«F
7?
-------
^^^^^^B
i
PLANT.
DATE_
SAMPLING LOCATION
SAMPiETYPE
RUN NUMBER.
OPERATOR
terra^f^
_£
PROBE LENGTH AND JY^E.
NOZZLE I.D. >y
75
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE .
STATIC PRESSURE, (PJ _ —
FILTER NUMBER (s).
ASSUMED MOISTURE, *
SAMPLE BOX NUMBER.
METER BOX NUMBER
METER AHe_
FACTOR_
ii.O
As-
?
PROBE HEATER SETTING.
HEATER BOX SETTING
REFERENCE Ap *L
!>~O f
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA EVERY —Jj— MINUTES
fe I'V^-fflfccOHMENTS:
rt-jifc.-;®^.:- •-.-• •
?••••?. ;••'_, .•."•-"•;.! ' ;
3;:.,1:.' *-;f".1,..'i' v' „
$'rS$r/:^'* ''•
GAS METER READING
(Vm), It3
. gy
Jo/ . O
m2
VELOCITY
HEAD
(dps), in. H20
^L
LI
A
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
.20
Z7_
,£0
STACK
TEMPERATURE
te-
^L
SO
fo
DRY GAS METER
TEMPERATURE
INLET
6
joj
IQI
lot
PUMP
VACUUM,
in. Hg
/
SAMPLE BOX
TEMPERATURE.
°F .
005"
IMPINGER
TEMPERATURE,
"F
75
ES-041
-------
TRAVERSE
POINT
NUMBER
t)
&•
• '•, ••'"'
\v CLOCK TIME
^"""NfSSi
TIME.min x^
' _
& )7 3?
^ J7 XJ^
-— — __
i
GAS METER READING
(Vm». It3
75?.aG
?H(-^^
/ ^W4J1
QA'. •
VELOCITY
HEAD
IAp$l. in. HjO
I.I
1 &
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in HjOl
DESIRED
*u
.M
r"
i •
r
/
ACTUAL
M
44
381^
"JJ
T?/
STACK
TEMPERATURE
(T$I.°F
^0
Pn
[R-l
/I
/
DRY GAS METER
TEMPERATURE
INLET
(Tmjn>.°F
^
lc>
OUTLET
.'F
7o^.
/o/$
3
J-.
r 0
y I /
PUMP
VACUUM.
in Hg
/
i
8148
Ml
SAMPLE BOX
TEMPERATURE.
°f
2*fo
^^
" i
) •
•**
IMPINGER
TEMPERATURE.
°F
^^5"
7^
ES-042
0,0
-------
FIELD DATA
PLANT.
OATE_ g-£p-"7
SAMPLING LOCATI
SAMPLE TYPE
RUN NUMBER. -3
OPERATOR _
/go _
PROBE LENGTH AND TYPE
NQZZLF ID {/a
AMBIENT TEMPERATURE .
BAROMETRIC PRESSURE _
STATIC PRESSURE, (Ps)_
FILTER NUMBER (s) £
ASSUMED MOISTURE. %.
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AHe A
CFACTOR
/A
-•4.0,
PROBE HEATER SETTING
HEATER BOX SETTING
REFERENCE AP 1.5
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA EVERY_^ MINUTES
ES-041
-------
3
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
'V1'3
VELOCITY
HEAD
(Ap>. in. H0
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in HjOl
DESIRED ACTUAL
STACK
TEMPERATURE
(TSI.°F
DRY GAS METER
TEMPERATURE
INLET
.°F
OUTLET
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
7
10
380
5 to.
to >
*<
A a
5*0
10
-fr
.? 33
£170
70
lo X
M
TO
JOtf
LI
70
38147
r
BjO-
-f~>
^
J—L
o,
042i
O.O
-------
Particle Size Distribution
-------
3 2 9
PARTICLE SIZE DATA SHEET
Type of -Test
1.
2.
3.
4.
5.
6.
7.
8.
10.
*K7?~/ >
£?/^ .~=>-c/ii
^-f t ^f
' fe? TP s^
*^^- I T^ \ *^/ " / ^^_^^ ^^ V*^ r O /
Bar. Press: P^ And,-Impactor Press.
(in.Hg) Drop (Brink Impactor)
. Static (in.Hg)
fi -O (R,8) CXO'^ (R,8)
% C02 . % 02
• 73 (R»8) /^- (R,8)
Sample Rate:Qn Stack Temn. : Tst
(ACFM) (Deg F)
(A, 8)
(A, 24)
^^/(A,24)
/
(A, 16)
(A, 16)
(A,8)
(A, 8)
>/}&&- ^fjj
-^- •••-• (R
Inpactor Temp .
Tj (deg F)
& -o> (R
..... % CO
— y- ^-~- (R
Static Press.
Duct: Pst
Job Number
Client
Plant Location
Unit Tested
Date
Test Condition
Ambient Temp.
Test No. , Stack No.
Test Location
,8) /. (R,8)
Part.
Density
(gm/cc)
,8) 3- (R,8)
%H20
,8) _$C' (R,8)
Test Time :
t (min)
12. And. 2-(
-------
PARTICLE SIZE DATA. SHEET
Type of -Test
1.
2.
3.
4.
5.
6,
7.
8.
9.
^S^V""/ ^7— /" /
>J- X'^7'7
/* ' ' J-^7 ^ ^
<~S &4.~£s-C^i_ /^ ^* 0 *^*-*£. _ i^~^^-^ - C
x£?^XX ^ '
/X^-^2^C^- CJ t-fij2-»_^_
£s&^tf & */ ^^^ ^ f
'/)/ "^ -7^
/£/#/? <**^r-~z— (A, 8) xo
$<,n^r -y •. (A, a? ""•"'•" ^•i^y
••":•-:-- AT^-T T^f>^^
J2 /' & (R,8) ^
-------
PARTICLE SIZE DATA SHEET
•ii~
2 V-ifr '
£• « •. V.'
3. -
4.
5.
6. /1/S
7.
8.
9- £X
Bar. I
(in. He
/
10. (
%
11. .%
Sample
(ACFM)
^f77~/7 (A'8)
^-^f' (A, 24)
(I^^A^^e — ,./£/i<3 , ££-//n?#' /t^X,24)
/£%* ^v 7^ (A, 16)
VStt/*^ - (A/8) ^ . , .(A, 8)
... ; • ', - '1;'^
:' '-ii*v.'>--'' • • - •' . '.•' ••' • . • •--— ~p '- _ ' :. - "•'*"%•• •'•••'•.. =•• •
." * bJ&,v:. .-. .. . • • — ••-.. •-.- . '^yr^^^ XT- •• - • • -;x ••'•'
''-]£>' (A, 8) --7 ^ Zfr-H • (A/8)
.--.,:,. ^FP^TtT/^^WM^
L(y> (R,8) _3 (R,8) J fi ' (R
'reds: Pj., And/-Impactor Press. Inpactor Temp.
f) Drop (Brink Impactor) Tj (deg F)
. Static (in.Hg) ...
*} -& • "9 V *r ' ^ A
(R,8) X^*" ' (R,8) V'O (R
C02 % 02 . . % CO
^ (R,8) '"TP'^'- •'""'" (R,8) "" /^^-^-^R
j Rate:Qn . Stack- Temp. : Tst Static Press.
(Deg F);,-\ Duct: Pst
Type of -Test
Job Number
Client
Plant Location
Unit Tested
Date
Test Condition
Ambient Temp .
Test No. , Stack »To
Test Location
,8) / (R,8)
Part.
Density
(gm/cc)
J7
,8) <=- (R,8).
%H20
,8) y^T' 7&- (R,8)
Test Time:
t (min)
(in.H20)
0
12. And.
Stage
(mg)
13.
Brinks
Stage
(mg)
Filter
6- i 6 ' •? (R,8)
8 Filter
Cyclone
Probe
(R,8)
-------
TP-3 Scrubber Outlet
-------
Particulate
-------
FIELD DATA
PLANT
DATE
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
OPERATOR
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE, (P$)
FILTER NUMBER (s)
PROBE LENGTH AND TYPE.
NOZZLE I.D. . /-**"
ASSUMED MOISTURE, * _O
SAMPLE BOX NUMBER _2J.
METER BOX NUMBER 5 -
METER AH I
PROBE HEATER SETTING _i££l
HEATER BOX SETTING.
REFERENCE Ap_g
SCHEMATIC OF TRAVERSE POINT LAYOUT
C.
READ AND RECORD ALL DATA EVERY.
MINUTES
(0 MLs . HJil IA~
TRAVERSE
POINT
NUMBER
c
TIME, mm
CLOCK TIME
(24'hl
CLOCK)
GAS METER READING
VELOCITY
HEAD
(Ap$), in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
STACK
TEMPERATURE
$4-0
I/
10 U -
- 7^/5"
•s/
/o /
•?. c
too
'
,3 o
10-6
io i
, o
/.£,
(lO
10
AS?
22^.
10
In A
"bC?
2*.
-X2_
to
5-0
0
3-0
o.o
COMMENTS:
ES-041
-------
V
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
' - »
3
VELOCITY
HEAD
tApl. in. H0
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in H20l
DESIRED
ACTUAL
STACK
TEMPERATURE
(TSI.°F
DRY GAS METER
TEMPERATURE
INLET OUTLET
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
6.0
//-*
100
to
3
0-0
f>.0
o.o
It
100
0. 0
Q .O
a
sC
•3.0
38371
38372
38373
-------
FIELD DATA
PLANT.
DATE_
SAMPLING LOCATION
SAMPLE TYPE &>A-
RUN NUMBER ^
OPERATOR gg'"*
AMBIENT TEMPERATURE .
BAROMETRIC PRESSURE .
STATIC PRESSURE, (PJ ~ > 6- 7
FILTER NUMBER (s) # 0<" * '
PROBE LENGTH AND,TYPE_!£.
NOZZLE ID
ASSUMED MOISTURE, %.
SAMPLE BOX NUMBER.
METER BOX NUMBER _J
METER AHg /. € (,
C^flCIOH —
PROBE HEATER SETTING.
HEATER BOX SETTING 1f)9 t'
REFERENCE AP , t (,
SCHEMATIC OF TRAVERSE POINT LAYOUT
READ AND RECORD ALL DATA PVFRY
MINUTES
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
(Vm). It3
VELOCITY
HEAD
APS). in. H20
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
STACK
TEMPERATURE
(T$),°F
DRY GAS METER
TEMPERATURE
INLET
S.o
lio
r.r
9S ,
3oo
l(. 6 Q
. -7-5
>t
1C, 1 0
(3.C?
O. O
/y
(04
-S7
{&&
3.0
"3o o
. n
o
30
/A
37
iOG
0
6 0
7/ •
73.
//x
/H
£.0
72
7*-
1103,
vo_
3.
fr
O-O
0. O
5s"
1(0
3>.o
COMMENTS:
ES-041
-------
TRAVERSE
POINT
NUMBER
°\
/6
ft
il
n
"t
>sv CLOCK TIME
--— ___
// JL- / 7 2L 7
,
'
GAS METER READING
. 1 !>
to & . ^> ^ _
/cV- 7W5
VELOCITY
HEAD
/ /"^
.r^^
~2^^<
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in HjOl
DESIRED
.^ >T
• <-/s"
,5-T
•^5 /
.74
^7V^=^
ACTUAL
^^"
.Vb'
<^/^^)H
F/LJT&IZ-
£>IL-(C&
DRY GAS METER
TEMPERATURE
INLET
•Trajn..°F
//y
'//«~f
lit
ji ^
//*•/
//*/
^P<7^
—
— -
—
OUTLET
'T">out'-°F
no
no
no
110
(e0
I to
\^r^<5
PUMP
VACUUM.
in Hg
-?.£>
^?.-<
"5--ST
^<9<^:
38366
18367
38368
X
,--••
/^
SAMPLE BOX
TEMPERATURE.
°F
3<2C>
~^& &
-£o
~3oOc?
7^./X>O
1
J
n
J
~l
j
- — — --.
IMPINGER
TEMPERATURE.
°F
-------
FIELD DATA
PLANT
DATE
SAMPLIHfi LOCATION
SAMPLE TYPE
RUN NUMBER
OPERATOR
o+jf.
PROBE LENGTH AND TYPE V
NOZZLE I.D..
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
STATIC PRESSURE, (PJ —
FILTER NUMBER (s) . (?,^7
ASSUMED MOISTURE, %
SAMPLE BOX NUMBER.
METER BOX NUMBER _
METER AHg
CFAefOR-___
PROBE HEATER SETTING /tf o&*{ 5 fcr
k.
r t' 0
/OO 8
/ A
/O
(.0
U
$0
Sir
/o<-/7
GAS METER READING
/S .
, -T . 7 X
/ ,
.4 "7
- ^^ • G
, /"•>
VELOCITY
HEAD
(AP$), in. H20
/.o
.-7
75
,1*1
,1*1
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in. H20)
DESIRED ACTUAL
2.
//r
•17
.72.
o
f^
So
PUMP
VACUUM.
in. Hg
£.0
30
3.0
0.0
SAMPLE BOX
TEMPERATURE,
°F
300
^00
O
.. -500
IMPINGER
TEMPERATURE.
°F
So
5-0
f-X
COMMENTS:
O
ES-041
-------
TRAVERSE
POINT
NUMBER
CLOCK TIME
GAS METER READING
IV... It
3
VELOCITY
HEAD
IApsl. in. H^O
ORIFICE PRESSURE
DIFFERENTIAL
(AH), in H20l
DESIRED ACTUAL
STACK
TEMPERATURE
(Tsl.°F
DRY GAS METER
TEMPERATURE
INLET
•Tmjnl.°F
OUTLET
PUMP
VACUUM.
in Hg
SAMPLE BOX
TEMPERATURE.
°F
IMPINGER
TEMPERATURE.
°F
noo
. SO
f.O
10
IO
-------
Particle Size Distribution
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.1,
2.
3.
4.
5.
6.
7.
8.
9.
.3~3>
PARTICLE SIZE DATA SHEET
7 ?
- (A,8)
(A,8)
(R,8)
(R,8)
Type of -Test
_(A,8) Job Number
(A,24) Client
,24) Plant Location
(A,16) Unit Tested
Date
_(A,8) Test Condition
Ambient Temp.
_(A,8) Test No., Stack No,
': (A,24) Test Location
• (R,8) /-
Bar. Press: PJ-, And,-Impactor Press. Inpactor Temp. Part.
(in.Hg) Drop (Brink Impactor) TT (deg F) Density
Static (in.Hg) • . . (gm/cc)
(R,8)
10.
11.
(R,8)
% CO
2
02
(R,8)
..- % CO
%H20
(R,8)
(R,8)
(Rf8)
Sample Rate:Qn Stack- Temp.:
(ACFM) (Deg F)
Static Press.
(Ry8)
Duct : Pst
uuv~k.. ^st
.: -:..-";:;M:^ (in.H20)
Test Time:
t (min)
12. And
Stage
(mg)
13.
Brinks
Stage
(mg)
Filter
£2. &-C7 o-lQ -Oj,,
1 Cyclone
Probe
OO !
,00. i
I
1
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7 8 Filter
-------
Visible Emissions
-------
REPORT NO.
PAGE
?&
Date
Observer
VISIBLE EMISSIONS FIELD DATA /^6-
O\0 (.
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REPORT NO.
PAGE
Date .cPA?/
... VISIBLE EMISSIONS /FIELp DATA /)&&& *<%r-^-^$fc-
fJ-^ ' \v •' Job Nuiriber •/' ? S~/ ? -/ 7-
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REPORT NO.
PAGE
Date
VISIBLE EMISSIONS FIELD DATA
• • .Job
Observer
(Observation Point
Stack: Distance from. ^6 Height
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Plant & Location^
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-------
REPORT NO.
PAGE
Date 5?/*?/??
Obser\
. • Gbser\
Stack:
Gbsen
" ' *
Comma
fcr v./Oc-' ^ LO
. VISIBLE EMISSIONS FIELD DATA /^^ 2^<-
. • • ' Job Nuriber • /- ' 5 < ' f r
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ration Point k^e-ST cr£- O
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-------
REPORT NO.
PAGE
Date ?L$*
( t
Observer L4j o
' ; • Observation P
• 'N • '
;;:..• VISIBLE EMISSIONS FIELD DATA, ['&<"£ ^-"Z — •
/T? • " Job Number /"" ^ 5~/'7"// ^~
<2'<$'£ev'Z— -• Plant & Location W-~^c.jj«-v*
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-------
REPORT NO.
PAGE
-VISIBLE EMISSIONS FIELD DATA
Date
Observer
;-?Ac»/7?
Number A-
Plant & Location
Observation Point
Stack: Distance from ^7?' He i ght 5""°
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TP-4 Bucket Elevator Hood
-------
Visible Emissions
-------
REPORT NO.
PAGE
A
. •• , . VISIBLE EMISSIONS FIELD DAT.
Date 8-Z^
o n o i l == i n
0 p o i ISTIO
• C? !
O • O • ' ^2. ' ^ O Q'0i
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i
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA
Date 6?~2f-7?
Job Number
O 1 0 is.' O O <0 O i ! ^ M O 1 O 0 O
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-------
REPORT NO.
PAGE
Date
Observer
VISIBLE EMISSIONS FIELD DATA • . *
• " Job Number..tf/-/5"/7V7
' Plant 5 L
Observation Point
wind & Speed HiJfl
Stack: Distance from
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Ended
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Opacity
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-------
REPORT NO.
PAGE
.. . -,'. VISIBLE EMISSIONS FIELD DATA . * ':
Date 8-Z9-.79 • • Job Number d/- ?r/7-/7
. • Obser\
Stack:
Obser\
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REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DAT
A
Date 9- 30-79
Observer
Job Number
Plant &
Observation Point F'££R/I£ £z.L£\/'ATaK. Wind & Speed
Stack: Distance frcm A//\ Height A/A Direction •'
A/ 'A
t&L
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' •
-------
REPORT NO.
PAGE
VISIBLE -EMISSIONS FIELD DATA
Date
9 -3O ~7?
Observer
Job Number
Plant &
Observation Point
OP
Stack: Distance from
Height
Wind & Speed_
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Observation Be"gsn /£QO Ended
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Visible Emissions
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REPORT NO.
. . '•.'.; -VISIBLE EMISSIONS FIELD DATA . *.
Date ..-? - c2 9 - ? 9 • - Job Nux^ber • j -*? *? / ?-/ 7~
Observer "su^f ^^U^Kf'-^ Plant £ Lccati.cn &£/*•/ £££5Q{
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REPORT NO.
PAGE
Date
p- J3-
Observer
'*.L>%r- o
y
Observation
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Wind & Speed ,
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-------
REPORT NO.
PAGE /-
'•';•'• ...VISIBLE EMISSIONS FIELD DATA . * ••
Date # - «2 ?~ ~?J . • ' Job Nuniber . • /-f-7<~'/J! 77
Obser*
/er %{& fSfifr^-o Plant & Location ^v4^*
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-------
REPORT NO.
. • '. .'. VISIBLE EMISSIONS FIELD DATA . *
Date P~3-9 -"?? . .• •' Job Nuniber • • -x - ^5"/ T^-'J-
Observer /<£.&' X^^fe-v4x Plant & Lccaticn ^/vyi -/^TO/V
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-------
REPORT NO.
PAGE
. • ':'.. VISIBLE. EMISSIONS FIELD DATA • . *
Date /7" 'SO - •7C; • ' Job Number •/ ^^'/"y- /"?•
Observer /O^" At^e^Ht ? Plant & LOG at icsi /^6v/H i 0
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-------
REPORT NO.
;•''•'• ,;.. • VISIBLE EMISSIONS FIELD DATA' • . '
Date .?- .•?£>''-' '7^ • " Job Nuiriber •/- fr/' ?-/•/*•
Observer />. , Plant & Lccaticn /i^^siS/?"^*,
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Coarse Ore Stockpiling
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TP-1 West of Stockpile
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Visible Emissions
-------
REPORT NO.
PAGE
Date
VISIBLE EMISSIONS FIELD DATA
Job Number ftl -
Observer
-~L) •
Observation. Point
Distance from
Observation Be'gan
Plant & Location
Wind & Speed__
Direction
Skv Condition
Opacity
8
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Comments:
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-------
REPORT NO.
PAGE
Date
VISIBLE EMISSIONS FIELD DATA
Job Number
- °\
-'?
Observer
* A /J/>
Plant & Location
Observation
m/7/
Stack: Distance from
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Wind & Speed . 5"~ /
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REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA
. Date C ~ o^~~fCl - . Job Number n/-^&
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VISIBLE EMISSIONS FIELD DATA
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA
Date 8-^8-79 Job Number Oi-f&7-j7
Obser\
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Visible Emissions
-------
REPORT NO.
PAGE /
VISIBLE EMISSIONS FIELD DATA
Date
Observer
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-------
REPORT NO.
PAGE
Date
VISIBLE EMISSIONS FIELD DATA
Job
Observation. PointT^ n^a^^Pon A
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Observation Be~gan ^-H5"^ Ended
Plant & Location
Wind & Speed Q-^Tn
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA
Date C ~&3 ~?^ Job Number Ot-q.'Ti^CZ.
Ob sen
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-------
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-------
REPORT NO.
PAGE
Date 8-23-7^
Observer A A // £"
VISIBLE EMISSIONS FIELD DATA
job Number
Observation Point
A
Stack: Distance from AM Height
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA
Date #-.23-77
Ob sen
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Stack;
Obsen
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Job Number <5/-rS~/7 -/7
A/i/irtyt •"
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-------
REPORT NO.
PAGE
VISIBLE EMISSIONS FIELD DATA
Date 8 -2"$ -7 9 Job Number rt/-£T/7_/7
Ob sen
Obsen
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Obsen
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REPORT NO.
PAGE
I
Date
Obsei"/er fep.rbrt>h.gX.
Observation Point '
3 -
VISIBLE EMISSIONS FIELD DATA
Job Number • Dl —
Plant £
inq o roi *
• Stack. Distance f r
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Wind & Speed
Direction
Sky Condition
Opacity
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REPORT NO.
PAGE
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• ' Job Nurrier
Observer
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REPORT NO.
PAGE
I
TKUCic r-
"••••''.•.:•.[. .''VISIBLE EMISSIONS FIELD DATA
Date QA * «3<3 - <¥\ - ' Job Number
.of
Observer ftflrbflrEL
. • Observation Point
pilli'nq •iruclC'toi^
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Wind & Speed
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I
J
I
-------
REPORT NO.
PAGE
TfcOCK- (Q — JTlolu bctanum "I&njcs
...''" : - -VISIBLE EMISSIONS FIELD DATA • . V
Date 08-3-Vy^ .• ' Job Number, ft l-95~n-/~V
Observer ftdrlyir"2L 1
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6.3 Laboratory Data
-------
ANALYTICAL DATA
Revisionr Two
Effective Date; 11/13/78
PLANT j-/€A/£e.r.son_ /Y]~in £- -
COMMENTS :
DATE-
SAMPLING LOCATION Crasher
SAMPLE TYPE TA^d
RUN NUMBER I " -3
SAMPLE BOX NUMBER
CLEAN-UP MAN
PARTICULATE RESULTS
SAMPLE SAMPLE . TEST . TEST
ID TYPE LOCATION NO.
• • /-/ce!/6n.<£_ C'^J-sh.er
,3f?" ^ V/o U/V?^v (£)o!"f/€-"fc /
vv. • • i«
3^0^ • 3
VOLUME
(ACETONE)
%0 '
IW
(30
FINAL
HT£? gV'Vy /
' ' » 0 T7S to
9^.^S77
?S,^JAJ
TARE"
sj-
U.Ubl
?^-3fej<^L
TOTAL WEIGHT GAIN • . .. ' .' -
•0-1 •!*/ U - O.QQi/
rrc.e;t«rie_- -O'»*-AC- • f'/"Vi" LESS ACET<
Y^^ ) ' Q.£>co
-------
ANALYTICAL DATA
Kevisxon: Two
Effective Date; 11/13/78
PLANT_
DATE-
A'V/)T€~-~
COMMENTS:
SAMPLING LOCATION vSgrubWr i
SAMPLE TYPE_R.f4i£
RUN NUMBER
- \
/- -3
SAMPLE BOX NUMBER.
CLEAN-UP MAN
PARTICULATE RESULTS
SAMPLE SAMPLE .TEST .TEST
ID TYPE LOCATION NO.
-3&^4f 1X!X ^"sSf '
JWtla " •" 5-
3*3^ " - -••"• ^3
VOLUME
(ACETONE)
/fcr4-
/.re?
//€>^3 «
_3
MOISTURE RESULTS
= © - . ^ O 0 ^
IMPINGSRS
FINAL WT/VOL
INITIAL WT/VOL
.
TOTAL MOISTURE '
-.'
"•'. - •'• •
-------
ANALYTICAL DATA
Revision: Two
Effective Date; 11/13/78
PLANT_
DATE-
COMMENTS;
SAMPLING LOCATION CfMshar
SAMPLE TYPE_
RUN NUMBER
7~ L?
SAMPLE BOX NUMBER_
CLEAN-UP MAN
PARTICULATE RESULTS
SAMPLE SAMPLE . TEST . TEST
ID TYPE LOCATION NO.
^•fcAra. ' u£C <0Stef- H
J2.-K3T7- " ' • • " £~
•-••••• &
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VOLUME
(ACETONE)
S^
. //^
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70
FINAL
WT/<\
J-
ICOJHM
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WT.^\
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^ ^z.( ^67^
f^fev^
TOTAL WEIGHT GAIN • . .. • . ' •
AcLe^P- Bk/(?^f
a cu? fa
MOISTURE RESULTS
c*
J
IMPINGERS
FINAL WT/VOL
INITIAL WT/VOL
TOTAL MOISTURE
}
I
-------
ANALYTICAL DATA
Revision: Two
Effective Date; 11/13/78
PLANT
COMMENTS:
'pro.
SAMPLING LOCATION /
SAMPLE TYPE ?ci(4t & O
RUN NUMBER
7 - 3
V.
SAMPLE BOX NUMBER
CLEAN-UP MAN
PARTICULATE RESULTS
1
SAMPLE
ID
SAMPLE
TYPE
. TEST . TEST
LOCATION NO.
•VOLUME
(ACETONE)
FINAL
TARE-
WEIGH
100.
11
n
0.0 7
u
-3
0, O^o
\-\o
(G-.OC :
TOTAL WEIGHT GAIN
/
I
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LESS ACETONE BLANK
WEIGHT OF PARTICULATE MATTER
0 .
O, - - , -,-
MOISTURE RESULTS Jj ,
(9.
IMPINGERS
FINAL WT/VOL
INITIAL WT/VOL
. TOTAL MOISTURE
-------
ANALYTICAL DATA
Revision: Two
Effective Date; 11/13/78
PLANT.
DATE-
— JJ
maX COMMENTS .-
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
. "* *^n
SAMPLE BOX'NUMBER.
CLEAN-UP MAN
PARTICULATE RESULTS
SAMPLE
ID
SAMPLE
TYPE
. TEST
LOCATION
TEST
NO.
VOLUT'JE.
(ACETONE)
FINAL
TARE"
V7EIGHT
0.0^1
V
mo
-------
ANALYTICAL DATA
Revision: Two
Effective Date; 11/13/73
PLANT,
DATE-
COMMENTS:
Q
r\_
SAMPLING LOCATION /
SAMPLE TYPE
RUN NUMBER
e.r-
SAMPLE BOX NUMBER
CLEAN-UP MAN
PARTICULATE RESULTS
. SAMPLE SAMPLE . TEST . TEST
ID TYPE LOCATION NO.
^'froH-S V/J^K ^Tn|-e>( /
V| . . .
-3^0 V,5~" ' 3-
II . l< '
;
VOLUME
(ACETONE)
i^o:
100
l&o
FINAL
97-.frr
^ S-&A
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TARE"
?f.^
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TOTAL WEIGHT GAIN • . -..-.'• •
• ./). fi . ~RA,nl/-- O'OGlU
• i (!,&• i t/'i~*i— • ••*-*>{(*•' if^ . - • •*• LESS ACETI
~~j^^L / " O.OG/CPc. WEIGHT OF
DNE BLANK .
PARTICULATE MATTER
WEIGHT]
GAIN^
o* ^^ °i
D. 73.7- !
$.3
-------
ANALYTICAL DATA
Revision: Two
Effective Date; 11/13/78
PLANT rreA^ers^A /Mm«e^— rf^y COMMENTS: 9^^,
v. rO-T^
~ ~ r f\ " '
DATE- *& "" 5-Sr ~ S1^ \J • '
SAMPLING LOCATION /"Crasher jCnl-gf /
SAMPLE TYPE 'T«.r*-fj> L>(*Cr«-
RUN NUMBER ^'
»-j >x-y. f*-v ^y / 1 ' i ( ^r^^" / /**->r\ i
31>Q7/ • O /o O lol.S^HO
\\ 'U i
3*8.0 i if _ •'•'•' ' ' 6p' '700 '0/,3(&l
S'SO^ Shnk: ' 3Z(ef-f l~(o. °lO J&/.V73&
TOTAL WEIGHT GAIN • ..
n -ci, , 15/ L <5.<9<5<5L3r.A
-
TARE" WEIGHT
WT.^ GAIN^c,
93.7338 O.'WO
Id. 0.3 ( 4 0.5^Q./r
ff, .1 1 ^ ^ ^^^L. •
IMPINGERS
tlNAL WT/VOL
INITIAL WT/VOL
TOTAL MOISTURE
'l^30&1o
£>>G/I cj
l.zirt
•
-------
ANALYTICAL DATA
Revision: Two
Effective Date; 11/13/78
PLANT.
DATE-
^
COMMENTS:
SAMPLING LOCATION
SAMPLE TYPE P^ r'
RUN NUMBER
J^lef /
'/-.3
SAMPLE BOX NUMBER_
CLEAN-UP MAN
PARTICULATE RESULTS
SAMPLE SAMPLE ' . TEST . TEST
ID TYPE LOCATION NO.
v3S//£ UWv 3^/ef ( 1
3Xf3-_L "• SL
ttiza- " • ' ^3
VOLUC'IS
(ACETONE)
(s>O
*fo
}t<5~
FINAL
o
100, LjolQ
lG3.V>*>H
TARE"
t¥.
-------
ANALYTICAL DATA
Revision: Two
Effective Date; 11/13/78
PLANT
DATE-
COMMENTS:
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
-3
g.recri
- 3
SAMPLE BOX NUMBER
CLEAN-UP MAN
PARTICULATE RESULTS
SAMPLE
. ID •
SAMPLE
TYPE
. TEST
LOCATION
TEST
NO .
VOLUME
(ACETONE)
FINAL
WT
TARE
WEIGHT
GAIN/,
a 03 (^
«
a
1 03-, HOC <%
n
(vO
TOTAL WEIGHT GAIN
0
,55.
ACETONE BLANK
WEIGHT OF PARTICULATE MATTER
MOISTURE RESULTS
IMPINGERS
FINAL WT/VOL
INITIAL T/7T/VOL
•
. TOTAL MOISTURE
!
!
-------
ANALYTICAL DATA
Revision: Two
Effective Date; 11/13/78
PLANT rrenJe.fiSQ'V
COMMENTS :
DATE-
SAMPLING LOCATION
SAMPLE TYPE
RUN NUMBER
SAMPLE BOX NUMBER
CLEAN-UP MAN
PARTICULATE RESULTS
SAMPLE
ID •
SAMPLE
TYPE
. TEST
LOCATION
TEST
NO.
VOLUME
(ACETONE)
FINAL
TARE"
WEIGHT.
GAIN
HO.
"
D.
ill.
1.1 f,
Q.G5C
D-
"
//0.-53V5
TOTAL WEIGHT GAIN
CL3??|
2- O.^tftf^
MOISTURE RESULTS
ACETONE BLANK
WEIGHT OF PARTICULATE MATTER
IMPINGERS
FINAL WT/VOL
INITIAL WT/VOL
TOTAL MOISTURE
-------
ANALYTICAL DATA
Revision: Two
Effective Date; 11/13/78
PLANT y/gWeC5g/v. / f F/ h (?
DATE- ff-^-52? ' - fr-c^-S1--?
SAMPLING LOCATION_
SAMPLE TYPE ~&r^l
RUN NUMBER
SAT4PLE BOX NUZ'1BER_
CLEAN-UP MAN
COMiMENTS : O«.
4o<2_ vx
'^
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PARTICULATE RESULTS
SAMPLE SAMPLE
ID • TYPE
. TEST
LOCATION
TEST
NO .
VOLUME
(ACETONE)
FINAL
TARB
WEIGHT
6L
0.
no
V
ILL
O, 3157-1
38-OIG
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TOTAL WEIGHT GAIN
LESS ACETONE BLANK.
WEIGHT OF PARTICULATE MATTER
MOISTURE RESULTS
IMPINGERS
FINAL WT/VOL
INITIAL WT/VOL
. TOTAL MOISTURE
i
i
!
• i
-------
ANALYTICAL DATA
Revision: Two
Effective Date; 11/13/78
PLANT ~t T [ Jrl/
SAMPLING LOCATION 7s)/- u^r Odi^l^t: _j
SAMPLE TYPE 7* r4\ C u UJ-^_ C\
RUN NUMBER / - V
SAMPLE BOX NUMBER ' '
CLEAN-UP MAN .
• .
PARTI CULATE RESULTS
SAMPLE SAMPLE . . TEST . TEST VOLUME
ID • TYPE . LOCATION . NO. (ACETONE)
"TV ^T"/
t
FINAL
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TOTAL WEIGHT GAIN . .
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1 ^— tA, / • *• w
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3 0. .0O jCN O "? O — *^
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MOISTURE RESULTS . . '
IMPINGERS
FINAL WT/VOL -
INITIAL WT/VOL
. TOTAL MOISTURE
V O(®{^
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-------
JOB NO.
No .
TYPE OF SAMl'f.E:
DATK:
Type
&
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Test
O.^H-ll 7
O.-1136'l
0.
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JOB NO. g-
PAHT.ICULATE ANALYSTS FORM
TYPE OF SAMPLE:
DATE
iOq No
Type
/U &
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1
Stack No
TP/
Tesl
Gross(Gr)
> 1
Tare (Gr)
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0 , 1 7
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Net (Gr)
Vol. (ml.)
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0 .06-* t£
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^
-------
NO:
TYPE OF SAMPLE:
.gq Mo .
32372
Type
L__&._
J2_
Slack No.
Test
Gross (Gr)
n.
6.
D.
Tare (Gr)
O.I&OO
n
0. I
-------
JOU NO.
PART I CUT.ATI? ANALYSTS RWM
TYPE OF SAMPLE:
DA-IT::
,o
-------
MO.
TYPE OP SAMPLE:
DATI;:
No .
28703
_ '»'ypc
M_J3_
/
Stack No
Test
Gross (<
0 .1
.{COX'S
0.1R-2.JS
Tare (Gr)
0.172-02.
0,1
o,
O.I £-2 00
Glass (Gr)
Net (Gr)
Vol. (ml)
Ml.nnk (Gr)
no.su J.1. (
Q.OOO73.
~>
3.0000 }
O.OGd 15
2JJL
z
TP3
c*/
o .2537?
O.OOO2-0
-Q. 1)0002.
a. ocooq
0-01 5 £
6. \7tt3.
0 . \7177
o .
6. 0605-2.
7
V •
.£.
o.i
0-
p_._ccoj
0 .OOCJ-
0-
7
-------
JOB NO.
PAUTJCULATE ANALYSTS FORM
TYPE OF SAMPLE:
DATP:
.oq No .
=3F5?7
JL
ype
Stack Mo.
Test
f-
Gross (Gr)
0.3. H (
o ,
Tare (Gr)
0 . 1 £8*15
Glass (Or)
Net (Gr)
Vol. (ml.)
Hank (Gi:)
HcsuJ.t (•
0.01376.
3.00
Q. 00177
O.OO052
±
&
5
7
7"
O.Q0700
Q.OWI
o ,
l 62-06
d ,
0 -
o .00022.
0.
0 . (
0 .
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0.
(2_il
JU
^>.
0-00^
-------
ri(HM\n_
0.
o
0.\41CO
-Q.OOOV'-
d. Oo oo
0-00077
0.
0. I7D.3+
7
y
O.I3I3(
11
0
6, a?
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S.
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o.
0*0032^
0,003*5
0. OOjLl*-}
0.00372.
1
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0.
fx (,.$ 0 6
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PART-ICUl-ATIS ANALYSTS FOKM
TYPE OF SAMPLR:
.oq No .
2E3 %%
_ '!^J££_
Stack No.
Test
Gross (Gr)
O./C
Tare (Gr)
Q.aSC
0, \
0.121
Glngs (Gr)
NeL (Gr)
Vol. (ml)
iM.ank (Gr)
;r)| Mosul
0-coooS
0J7337
0. \7l-73
0,177^7
0.
£
7
o. 11> L to
f to 3
n,\
7
5"
^
\& 7
0. boo 02-
Q.60&H
S.
O.OOW)
0.175&S
0, OOC&3
o,ooofi3
(>
^p^, '-/-IP"
—,/"i /^ ^^, I
-------
JOU
PAIlM'Tf'lll JVPI? AMAI VfjrC
TYPE OF SAMIT.E:
DATIS
jOq No .
3?3^
\
, " .
Type
A*l 6
t
^
3
/
^
6
7
r
Stack No.
Cvau^ese
14 K 7
0. 16 3-2-]
0> \. \7H-77
Tare (Gr)
o.^Jh7^5
£?. ; ^70
o.mof
c.i WC
("). )C\7JL
0.tf\L\
rt./7f X5"
/Jj4a^.f
6. 17 ^-yf
Glass (Gr)
NoL (Gr)
a
Vol. (ml)
/
//•
'/:
*
Mia nk (Gi:)
lle.su J.L (•
<0,CK)n/6
-O,OQ287
0,0001^
O.OCOO&
0>OOQ\2
O.booo\
Q . 00003
Q.OC&>1>
n.oo&o2>
-------
MO.
PAIITJCUF.ATI-] ANALYSTS
TYPE O1T SAMPJ.R:.
DATI?.
No .
l2£3_i_
J2._
/
TnTftL*
Stack No.
/
f r
I ML IT i
r
? r
Tea I
a'
O.
o
Tare (Cr)
o.
0
Glass (Or)
y
Not (Gr)
_Vol_ _Ji»|)
nank Gi.
o.
0.
$
9
T7/-
-------
jon HO.
TYPE 'OF BAMPI.E;
I,oq No .
2 orj <)
_!i'yi-!«
PeHle ?
fl££kL
r ^
TUT
9C
._aai^.^
TQ rfl j.
SUipk No
FX.£ T k
TP7-Jwi.tr
oorxgr
Qt)Tl.<> T
OOTI? r
O
Tesl
8
A
p
Tai.e (Gr]
O. _*J_*J/3Jl_
0.1SO&6
O.WXV
0.'11650
?.r;
y
y
v./.
Not (Gr)
_Vpl_ (ml)
lll.uik (Ci )
U
&.
0. eve* 0 6>
o.
-------
JOB NO
PAUTTCUI.ATF. ANALYSTS FORM
TYPE OF SAMPLE:
dog No .
Type
Stack No.
Tesl
t
Gross (Gr)
Tare (Gr)
Glass(Gr)
Net (Gr)
Vol. (ml.)
M.nnk (Gi:)
HosnJ t;(
0,00235
0.002.3 \
0,C)036&
0.0^7
6,000%
6,000^(0
6
6
7
T-
0.
o.
o.ooo^
d.ooooj
0.0006$
b.
o.
a,«
0 . o/^n
. ox? '-/
0_:.QOoT£_
-------
LM
CABLE ADDRESS "LEOOUX TEANECK"
TELEX 1343*0
nue, Teaneck. New Jersey 07666 . Telephones: 2£(
IfltUPENOENT CONTRQl. AND RESEARCH CHEMISTRY. INSTRUMENTAL ANO CHEMICAL ANALYSIS • SAMPLING.
! WEIGHING SHIPPERS' REPRESENr.UIQN. EENSf ICIATION. AND STGRAUE OF ORES ANO METALS
REPORT OF ANALYSIS
No.
October 31, 1980
Our analysis of the sample of . _ .
* Oust Samples
t-rom York Research Corporation
Marked: ,15 Lots A$ BeLow p>0>#3_5830
To
PARTS PER MILLION
#37702
COPPER 20.
NICKEL 100.
COBALT 50.
IRON =~ M
MANGANESE M '
CHROMIUM 200.
VANADIUM 500.
TITANIUM M
SCANDIUM 20.
CALCIUM 1000.
POTASSIUM 1000.
CHLORINE 2.
SULFUR 10. .
PHOSPHORUS 500.
SILICON M
ALUMINUM M
MAGNESIUM A
SODIUM 500.
FLUORINE <1.
CARBON
BORON 20.
BERYLLIUM ' A
LITHIUM '— <0.5
-------
CAUL" AODPC5S -LSDOUX THANEC;'.
TELEX 134340-
LM
EST. ma "
AV'h 359 Alfred Avemte..Teaneck, New Jersey 07666 • Ti-kplwus:
INDEPENDENT CONTilQl, AND RESEARCH CHEVISTSY. INSTRL'.VE.'JTAL A.'IB CH5M1CAI. Af!,M.V3!S •. S-VM?UMC.
i WEIGHIfili, SHI7PEHS1 RtrnESENTATION, BEKEFICIATIOfl. A,VU STORAGE Of Oi'tES ASO KH
REPORT OF ANALYSIS
No.
October 31x 1980
Our analysis of the sample of Dust Samples
From York Research Corporation
Marked:
15 Lots As Below P.0.# 3-5830
and submitted to
PARTS PER MILLION •
us, shows:
# 37702
CERIUM 100
LANTHANUM — IQQ"
BARIUM 100*
CESIUM
-------
CABLE AOOHESS "LESOUX TCANECK"
TELEX 134340
20! S37 7160
Alfred Avenue, Teaneck. New Jersey 07666 • Telephones:
INDEPENDENT CONTflOl. AND RESEARCH CHEMISTRY. INSTRUMENTAL AHO CHcMICAL ANALYSIS • SAMPLUJG.
I WEIGHING SHIPPERS' REPRESENTATION. BENEFICIATION. AND STORAGE Of ORES ANO METALS
REPORT OF ANALYSIS
No.__1014215.
October 31X. 1980
Our analysis of the sample of ous^ $amp les
From York Research Corporation
Marked: 15 Lots as Below P.O.#3-5830
To
aitd
••- •:••-PARTS-PER MILLION-. ' '
URANIUM--"------— —-—
THORIUM ----------------
, BISMUTH : --------- --- ---'
LEAD ------- :-*- — -- ------
.#377Qa.
'20.'^ :'":
<1."
"
' MERCURY' -—-—£—----- ' ' <2.: •"••••
GOLD — ---- : ------------ <1.
PLATINUM --------------- <2.
IRIDIUM ---------------- <1.
OSMIUM ----------------- <2.
RHENIUM ---------------- <2.
TUNGSTEN --------------- <2.
TANTALUM -------- : ------- <1 .
HAFNIUM ------- . --------- <2.' '
LUTETIUM --------------- <0.2
YTTERBIUM --------------- <1 .
THULIUM ---------------- <0.2
ERBIUM ------------- - ---
-------
CUSTOMER
ATTENTION
ADDRESS
CITY
S.O. NO.
YORK RESEARCH CORPORATION
One Research Drive
Stamford, Connecticut 06906
4678
ALBUQUERQUE LABORATORY
6
REPORT OF RNflLYSIS
'• DETERMINATION of POLONIUM-210
rv.MOFANAi.vsnn FILTER RESIDUE SAMPLES
4-5349
CUSTOMER ORDER NUMBER
SAMPLES RECEIVED
2/21/80
Sample
Identification
Date
Collected
Total
Weight (g)
•27077
27081
27084
28192
•28197
11/20/79
11/20/79
11/20/79
11/20/79
11/20/80
38001
38004
38007
38012
REPORTE5 VIA TEH
REPORTED VIA TWX
08/23/79
08/23/79
08/23/79
08/23/79
pCi/sample
0.0 ± 1.0
0.0 ± 1.0
0.0 ± 1.0
0.0 ± 1.0
0.0 ± 1.0
0.0 ± 1.0
0.0 ± 1.0
0.0 ± 1.0
0.0 ± 1.0
0.0 ± 1.0
0.0 ± 1.0
0.0 ± 1.0
0.0 ± 1.0
pCi/g
PAGE__1 OF 2 PAGE
P.O. 30X 3874 iLBUGUERQUE. NEW MEXICO 37110
PHONE iSOS) 345-3461 TWX: 310.985-0678
3/18/80
APPROVED BY 'j DATE
MICHAEL A. ORTIZ, Laboratory Manager
-------
ALBUQUERQUE LABORATORY
CUSTOMER
ATTENTION
ADDRESS
CITY
S.O. NO.
YORK RESEARCH CORPORATION
One Research Drive
Stamford, Connecticut 06906
4678
DETERMINATION of POLONIUM-210
TYPE OF ANALYSIS in. FILTER RESIDUE SAMPLES
4-5349
CUSTOMER ORDER NUMBER
REPORT OF flNRLYSir
SAMPLES RECEIVED
2/21/80
Sample
Identification,,
Date Total
..„.., .Collected. „,„.,,„ Weight, (g) ..^
,,,.,pCi/ sample.',,,.,^. .;,._..p.Ci/g..
08/23/79
08/23/79
08/24/79
08/24/79
0.0 ± 1.0
0.0 ± 1.0
0.0 ± 1.0
0.0 ± 1.0
39668
11/20/79
3.1 ± 1.1
REPORTED VIA TELEPHONE
REPORTED VIA TWX
PAGE ? OF 7 PAGE
APPROVED BY
3/18/80
P.O. 3OX 3874 ALBUQUERQUE. NEW MEXICO 87110
PHONE 1505) 345-3461 TWX: 910-985-0678
MICHAEL A. ORTIZ, Laboratory Manager
-------
\5*n0e.£" /? -
r"fuc.^ (o
n
,
g,
/"
— fc /a
b
Q Cf o S ^T Q
©
/
-
0/n
-------
JOII NO.
I'AKTICUI.ATF. AHAr.Y.S.I.S FUI1M
TYPE OF .SAMPLE:
oq No.
-lYl'C
over .D
d
£
Stuck Mo.
Test
Groorj (Gr)
*& pp^i V?
fall,?
7T/.g
Tare (Or)
'Ti^n
703, Iff
7
Glaaa (Or)
Not (C,r)
""*" -~~~~J — —
Vol (ml.)
-------
FOR
TE3T To
BRIDGEPORT TESTING LABORATORY, INC.
ESTABLISHED 19O9
Industrial Chemists and Metallurgists
BRIDGEPORT. CONNECTICUT O661O
(203) 384-O361
YORK RESEARCH CORP
INSTRUCTIONS
°ATE April 18, 1980
TEST NO. 552274
P.O. NO. 4-5332
Samole
A - ore before crusher
C - ore before crusher
Test run #2 )
T.P. 1&2 from crusher'
entrance )
"----•**•
RC 65
RC 68
RC 65
ggsssEss-
- 70
- 70
- 68
— ^
(1-9517-17) •*
(1-9517-17)
/
Test #3 (from conveyor leaving
crusher
RC 66 - 70
Test #3 (from crusher entrance) RC68 - 70
Test #2 (from conveyor leaging
the crusher) RC 68 - 70
WE CERTIFY THAT THIS IS A TRUE COPY OF OUR RECORDS.
SIGNED FOR BRIDGEPORT TESTING LABORATORY, INC. BY
) If Checked
CHECKS AND CALIBRATION OF EQUIPMENT USED FOR THE ABOVE TEST WERE IN ACCORDANCE WITH PWA MCL MANUAL
SECTION F-23.
•NOTE — Semi-Quantitative Spectrographic Examination is an approximation of material identity. It is not a positive identification, and should be used
for confirmation purposes only. Where positive identification is necessary, complete chemical analysis should be requested.
Vhto leport is iubmmed with the understanding that it li not to be reproduced for advertising or other purposes over our signature without expmi written permission from us.
We Jo not accept any liability concerning the utc o/ these results.
MP
-------
6.4 Calibration Data
-------
PITOT CALI3SATIGN
s
fc A ?3«
A ?std
0.
a?
7?
• '
i ',. ••
27
35
.••^i < — i
v /
.77
..67
•
s «
FLCW
.S?
4 i
-------
PITOT CALIBRATION
A. "i
IK' A ?3td I A?3
!
<=? i
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> -1C
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.70
o • /
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7
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PITOT CALIBRATION
A 93td
A ?srd
0
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A ?3t
A ?strd
,33
0
.30
3%
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3±
1
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-------
PITOT CALIBRATION
A?STd
A P3t
-------
PITOT C.ALI3SATICN
A ?std
33,
31
.S'S
'32
O /
/ 6 .
.75
1
?LCW
J-*'*'
1
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A P3tc
A. ?sl:d
70
11
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PITOT CALI3SATICN
A ?std
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5 j
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PITOT CALI3RATICN
iE
A ?strd
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16
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37
.79
20
73
3
A
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-------
PITOT CALIBRATION
A 93td I-
A ?sl:d
••P7
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7
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A st
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- 7. -7, "-
-8;— .'i
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__...__ - —- -
v
-------
-.* REPORT NO.
PAGE
ORIFICE AND METER CALIBRATION
Date: V 111 /9cy Box No..
O " c^ /
Man.
0 r if ice, CFW, CF^, T,^
Td Time
OT^- , Ave. , t
.5
•63
100
96
/.Ol
1.0
63
.^
9-31
1.01
2.0
/O
4.0
'OS
l.O
6-
6
/Ob
8.3')
/.Or
3.0
10
7V
Tolerances:
Y = .99-1.01 Ideal '100
= 1.6-2.1
Ideal 1.34
-------
ONS RESEARCH QRIVS.STAMrOnO.CCNMSCTlCtJT OG305
Zc2 4^
V /
r, (TV -,
f ,'/'-*
. ?_x } -?^t
7 . Ofe.^f
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-------
REPORT NO.
PAGE
Date:
//$"/?
ORIFICE AHD METER CALIBRATION
BOX NO. S~ £ I & & P-,
Man .
Orifice, CF. ,, CP^
OT^- , Ave.
Time
t
.5
1.03.
1.0
11
80
1.0 I
2.0
S'o
1.03L
4.0
War
1. OS.
6.0
(.03.
8.0
10
9.8?
Tolerances:
Y = .99-1.01 Ideal '100
El> = 1.6-2.1 ' Ideal 1.34
-------
ONE RESEARCH 03IVE, STA.MrOaO. CONNECTICUT OG305
I?AC eo/r
"fi
a °
Ps
c n/o?<"
D . \^s i >J o -j_
" -- -7 <2 <^
. c. / /
03V T
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-------
REPORT NO.
PAGE
^
X
ORIFICE AND METER. CALIBRATION"
Date- (nCf-tl -09 Box No1. X~/9W PV, ^V.S'S
Man.
Orifice. CF... CF^a
.5
1.0
2.0
4.0
6.0
8.0
3.113
6
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»,„
10
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•-:
••>«
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f :
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Tolerances': Y = .99-1.01 Ideal 100 '';'
c^Ei = 1.6-2.1 Ideal 1.34.
-------
, •:..!> •"(
8
\7 *-»»-» 5 f ?•- / ;>-x £» .ex ..—I T» .?"» i/-s
5 O 3 i\ fi \ $5 b O* C; i \^ 52
ONE RESEARCH DRIVE, STAMFORD, CONNECTICUT 06906
. » • /
U S * J <^ a Ci i. S O i
BOX CALI&.
#
CFUJ j
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+
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/ .03/7
/ .
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660 \
x
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. I
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K $
X
f
53?f
-------
REPORT NO.
. PAGE
ORIFICE AND METER CALIBRATION
Date: V / cW / '/ c!
Man.
•Orifice, CF. . CF^,
.5
1.0
2.0
4.0
6.0
8.0
s
'ID-
ID
10
10'
.0,
^"7 *— * ^
9.95
9.9J
?.7V
Box Mo . S- 3. II 9
T,..,
7?
96
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9 7
p.. 3(0, 1.^
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ITj , CT^ , Ave . . t ,•£*!?& , Y
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s=
c /•
/b
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= 1.6-2.1 Ideal 1.34
1
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Ci\'S RESEARCH DRIVE, ST;
o r K p y , u, / / .o
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-------
REPORT N7O.
T
PAGE
ORIFICE AND METER CALIBRATION
Box
Man.
orifice, CP CF^, • T.
.5
70
Td Time
, CT,a , Ave. t
1.0
70
2.0
/o
10
fj
4.0
/o
10
5-7
6.0
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r-'.) -
H-1"/ ONE RESEARCH DRIVE. STAMFORD, CONNECTICUT OG906
.
fa.
PC
.o/rsr
.S. 03^
03/7
.0737
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L.
"
5~,/0
V
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8
'f
3o
- 3/ ^3 3 cf'^ J>' 30
-------
REPORT NO.
PAGE
ORIFICE AND METER CALIBRATION
Date: /A/79 Box No. ^^\^1 Pb 3\O X<2
Man. . Td Time
Orifice CF.,
. 5
1.0
2.0
4.0
6.0
8.0
^£ O i O
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O.N'S RESEARCH DRIVE, STAMrORO, CONf-!£CT:CUT OG30S
'"P^^^i.yr^^^g^T
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COLORADO
DEPARTMENT OF HEALTH
This Certifies thot DIANE M.
Volid until t/J
ho> saliifoctorily completed a courts In
observing and recording the density of
Vnccjce on^ '* qualified to datarmln* and
grad« visibta ara^uionA \yl*tm* 5r o)7n»
city.
Coordinator
-------
COLORADO
DEPARTMENT OF HEALTH
This Certifies thot KITT KITTREDGE
ho* jQtiifoctorily completed a course \n
observing and recording the density of
•JmoVa and is qualified to datefminercnd
d& visible emiijioaa^Ji^TermsVij^opa- ff
///
Valid until
-------
;^JI«^
^•;\^W^i iPKS^fe&tatF of (Em
&0nn?rti$it&
roterttim
CERTIFICATE OF TRAINING
This is to witness that* Through the authority uested in me by the
General Assembly of the State of Connecticut it is made known
and attested'tharl?:; ^?t;BRUCE'WUEBBER • "•"•'•' -vr^^\^r:Y''''::':::
acted with such -merit as to be proclaimed publicly to haue
completed the course of instruction and demonstrated proficiency
in ':^ v;>^K^2fe4^1;,-,-,,-,VISIBL.E EMISSIONS EVALUATION ,_.-•'
^»p. "®?^;Sir"-•',
•!'•••''':VlJ- ••-'V-f''•';'*"'; !"-'••
In testimony whereof I subscribe my name and affix the seal
of the Department of Environmental Protection on this
day of ^
-------
COLORADO
DEPARTMENT OF HEALTH
This Certifies thot A. GLEN LANE
Valid until
has sattifoetorilj' completed a cours« in
ebiarving and recording the density of
> and i» qualified to dalerm'i»p and
fads visible em'i^o'yi/n tarnu^r opa-fl
-TT
-------
6.5 Sample Calculations
-------
PARTICULATE CALCULATION KEY
2
AS = Stack area (ft )
C = Dry particulate concentration - Gr/SCFD
C£>2' °2' N2' C0 = Percent by volume (dry basis?" in flue 'gas
C = Pitot tube correction factor
D = Sample nozzle diameter (in.)
E = Dry particulate emissions - Ib/hr
% EA = Percent excess air
E-, = Emissions by F Factor - Lb/MMBtu
E_ = Emissions by F Factor - Lb/MMBtu
£ C C
£„_ = Emissions by actual heat input - Lb/MMBtu
nJ.
E = Average normal emission rate (non-soot blow)
E = Prorated emission rate
E , = Emission rate during soot blow
F = F Factor (SCFD/MMBtu)
F = F Factor
c c
GCV = Gross caloric value- of fuel fired (Btu/lb)
H, C, S, N, 0 = Percent by weight of fuel fired
% I = Sampling isokinetics
% M = Percent moisture by volume in stack gas
M, = Mole fraction of dry gas
Mf = Front half sample weight (milligrams)
MW = Molecular weight of stack gas
MW, = Molecular weight of dry stack gas
P, = Barometric pressure ("Hg)
-------
P = Average orifice pressure drop ("H2Q).
P = Stack pressure ("Hg absolute)
APg = Velocity pressure ("H20)
Q, = Stack gas flow rate, stack conditions - ACFM
Q = Stack gas flow rate, standard conditions - SCFMD
s
T = Time unit in operation, per day (hours)
T = Average meter temperature (°F)
T = Stack temperature (°F)
S
T , = Time unit blows soot per day (hours)
T = Test time (minutes)
V = Volume of gas sampled at meter conditions - ft
V = Volume of dry gas sampled at standard conditions
mstd ft3
V = Stack gas velocity at stack conditions - fps
S
w " = Milliliters of water condensed in impingers
V = Volume of water vapor at 70°F and 29.92" Hg, ft3
wgas
-------
PARTICULATE CALCULATIONS
The following are the basic equations used in calculating .the .data
as found in the final summary.
1. Volume of dry gas sampled at standard conditions - 70 F, 29.92"Hg,
ft.3
17.7 x Vm(Pb + Pm )
mstd = 13.6
(Tm + 460)
2. Volume of water vapor at 70°F and 29.92" Hg, ft.3
Vwgas = °-0474 x Vw
3 . % Moisture in stack gas
100 x V
M =
vmstd + vwgas
4. Mole fraction of dry gas
Md = 100 - % M
TOO
5. Average molecular weight of dry stack gas
M Wd = (% C02 x .44) + (% 02 x .32) 4- (% N2 x .28) + (% CO x .28)
6. Molecular weight of stack gas
M W = (M Wd x Md) +18 (1 - Md)
7. Stack velocity at stack conditions, fps
AP x (T + 460)
rg = 85.48 x C '
-------
7s. Average stack velocity at stack conditions, fps
Vs = (85.48) (C ) PS(TS+ 460)
where VA?(T + 460) is the average square root of the product of
the velocity head and the absolute stack temperature.
8. Stack gas flow rate, stack conditions, ACFM
QA = 60 x Vs x As
9. Stack gas flow rate, standard conditions, SCFMD
1062.6 x Vs x As x Md x PS
3 (T + 460)
S
10. Percent isokinetic
17.24 x (Ts + 460) x Vmstd
V_ x T. x P x M, x (Dn)2
s t s d n
11. Dry particulate concentration - Gr/SCFD
Mf
C = 0.01543 x
Vmstd
12. Dry particulate emissions - Ib/hr
E = 0.008572 x C x Qc
S
13. Particulate emissions by actual heat input - Lb/iMMBtu
HI MMBtu/Hr
14. % Excess air at sampling point
100 x (% 02 - 0.5% CO)
% EA =
(0.264 x % N2) - (% 02 - 0.5% CO)
-------
15. F Factor
F = 1Q (3.64%H) + (1.53%C) + (.57%S) + (.14%N) - (.46%0)
GCV
16. F Factor
F = 321 x 103 %C
c GCV
17. Emissions by F Factor (Lb/MMBtu)
CF 20.9
TOTOO" 20.9-% 0
18. Emissions by F_ Factor (Lb/MMBtu)
CF
F = _ C 100
Fc 7000 % C02
19. Prorated Emissions
Ep - En + (Esb - V
-------
ENGLISH TO METRIC
CONVERSION FACTORS
FROM ENGLISH TO
DSCF
DSCFM
Tons/hr
gr/DSCF
Ib/hr
Ib/ton
oF
METRIC
DNm3
DNm /rain
Mg/hr
g/DNm3
Kg/hr
Kg/Mg
°C
MULTIPLY BY
0.02832
0.02832
0.9072
2.288
0.4536
0.5
-32, x 5/9*
First subtract 32 from °F temperature, then multiply by 5/9
-------
6.6 Method 22 - Visual Determination
of Fugitive Emissions from
Material Processing Sources
-------
METHOD 22--VISUAL DETERMINATION OF FUGITIVE
EMISSIONS FROM MATERIAL PROCESSING SOURCES
1. 'Introduction
This method involves the visual determination of fugitive
P
emissions; i.e., emissions not emitted directly from a process stack or
duct. Fugitive emissions include emissions that (1) escape capture by
•.process equipment exhaust hoods, (2) are emitted during material
transfer, (3) are emitted from buildings housing material processing
or handling equipment, and (4) are emitted directly from process
equipment.
This method determines the amount of time that any visible
emissions occur during the observation period, i.e., the accumulated
emission time. This method does not require that the opacity of
emissions be determined. Since this procedure requires only the
determination of whether a visible emission occurs and does not require
the determination of opacity levels, observer certification
according to the procedures of Reference Test Method 9 are not required.
However, it is necessary that the observer- is educated on the general
procedures for determining the level of visible emissions. As a
minimum the observer should be trained regarding the effects on the
visibility of emissions caused by background contrast, ambient lighting,
observer position relative to lighting, wind, and the presence of
ur.combined water (condensing v/ater vapor).
-------
2. Applicability and Principle
2.1 Applicability. This method applies to the determination
of the frequency of fugitive emissions from stationary sources
(.located indoors or outdoors) when specified as the test method for
. determining compliance with new source performance standards.
2.2 Principle. Fugitive emissions produced during material
processing, handling, and transfer operations are visibly determined
by an observer without the aid of instruments.
3. Definitions
3.1 Emission Frequency. Percentage of time that emissions
are visible during the observation period.
3.2 Emission Time. Accumulated amount of time that emissions
are visible during the observation period.
3.3 Fugitive Emission. Pollutant generated by an affected
facility that.is not collected by a capture system and is released
to the atmosphere.
3.4 Observation Period. Accumulated time period during which
observations are conducted, not to be less than 6 minutes.
4. Equipment
4.1 Stopwatches, accumulative type, with unit divisions of at
least 0.5 second; two required.
4.2 Light Meter. Light meter capable of measuring illuminance
in the 50- to 200-lux range; required for indoor observations only.
5. Procedure
5.1 Position. Survey the affected facility or building or
structure housing the process unit to be observed, and determine the
-------
locations of potential emissions. If the affected facility is located
inside a building, determine an observation location that is consistent
•
with the requirements of the applicable regulation (i.e., outside
observation of emissions escaping the building/structure or insida
observation of emissions directly emitted from the affected facility
process unit.)
Then select a position that enables a clear view of the potential .
emission point(s) of the affected facility or of the building or
structure housing the affected facility, as appropriate for the
applicable subpart. A position of at least 15 feet but not more than
0.25 mile from the emission source is recorrinended. For outdoor
locations, select a position where the sun is not directly in the
observer's eyes.
5.2 Field Records • ;..
5.2.1 Outdoor Location. Record the following information
on the field data sheet (Figure 22-1): company name, industry,
process unit, observer's name, observer's affiliation, and date.
Record also the estimated wind speed, wind direction, and sky condition.
Sketch the process unit being observed, and note observer location
relative to the source and the sun. Indicate the potential and actual
fugitive emission points on the sketch.
5.2.2 Indoor Location. Record the following information on the
field data sheet (Figure 22-2): company name, industry, process unit,
observer's name, observer's affiliation, and date. Record, as
appropriate, the type, location, and intensity of lighting on the
-------
data sheet. Sketch the process unit being observed, and note
observer location relative to the source. Indicate the potential
and actual fugitive emission points on the sketch.
5.3 Indoor Lighting Requirements. For indoor locations,
use a light meter to measure the level of illumination at a
location as close to the emission source(s) as is feasible. An
illumination of greater than 100 lux (10 foot candles) is
considered necessary for proper application of this method.
5.4 Observations. .Record the clock time when observations :
begin. Use one stopwatch to monitor the duration of the observa-
tion period; start this stopwatch when the observation period
begins. If the observation period is divided into two or more
segments by process shutdowns or observer rest breaks, stop the
stopwatch when a break begins and restart it without resetting -
when the break ends. Stop the stopwatch at the end of the
observation period. The accumulated time indicated by this stopwatch
is the duration of the observation period.1 When the observation
period is completed, record the clock time.
During the observation period, continuously watch the emission
source. Upon observing an emission (condensed water vapor is not
considered an emission), start the second accumulative stopwatch;
stop the watch when the emission stops. Continue this procedure
for the entire observation period. The accumulated elapsed time on
this stopwatch is the total time emissions were visible during the
observation period, i.e., the emission time.
-------
5.4.1 Observation Period. Choose an observation period of
sufficient length to meet the requirements for determining
compliance with the emission regulation in the applicable subpart.
When the length of the observation period is specifically stated
in the applicable subpart, it may not be necessary to observe
the source for this entire period if the emission time required
to indicate non-compliance (based on the specified observation
period) is observed in a shorter time period. In other words
if the regulation prohibits emissions for more than 6 minutes in
any hour, then observations may (optional) be stopped after an
emission time of 6 minutes is exceeded. Similarly, when the
regulation is expressed as an emission frequency and the regulation
prohibits emissions for greater than 10 percent of the time in
any hour, then observations may (optional) be terminated after
6 minutes of emissions are observed since 6 minutes is 10 percent
of an hour. In any case, the observation period shall not be less
than 6 minutes i.n duration. In some cases, the process operation
may be intermittent or cyclic. In such cases, it may be
convenient for the observation period to coincide with the length
of the process cycle.
5.4.2 Observer Rest Breaks. Do not observe emissions
continuously for a period of more than 15 to 20 minutes without
taking a rest break. For sources requiring observation periods
of greater than 20 minutes, the observer shall take a break of
not less than 5 minutes and not more than 10 minutes after every
-------
15 to 20 minutes of observation. If continuous observations are
desired for extended time periods, two observers can alternate
between making observations and taking breaks.
5.4.3 Visual Interference. Occasionally, fugitive emissions
from sources other than the affected facility (e.g., road dust)
may prevent a clear view of the affected facility. This may
particularly be a problem during periods of high wind. If the
view of the potential emission points is obscured to such a degree
that the observer questions the validity of continuing observations,
then the observations are terminated and the observer clearly notes
this fact on the data form.
5.5 Recording Observations. Record the accumulated time of
the observation period on the data sheet as the observation period
duration. Record the accumulated time emissions were observed on
the data sheet as the emission time. Record the clock time the -
observation period began and ended, as well as the clock time any
observer breaks began and ended.
6. Calculations
If the applicable subpart requires that the emission rate be
expressed as an emission frequency (in percent), determine this
value as follows: Divide the accumulated emission time (in seconds)
by the duration of the observation period (in seconds) or by any
minimum observation period required in the applicable subpart if
the actual observation period is less than the required period, and
jnultiply this quotient by 100.
-------
FUGITIVE EMISSION INSPECTION
OUTDOOR LOCATION
Company
Location.
Company representative
Observer
Affiliation
Date
Sky conditions
Precipitation _
Wind direction
Wind speed
Industry
Process unit,
Sketch process unit; indicate observer position relative to source and sun; indicate potential
emission points and/or actual emission points.
OBSERVATIONS
Begin observation
Clock
time
Observation
period
duration,
min:sec
Accumulated
emission
time,
min:sec
End observation
-------
FUGITIVE EMISSION INSPECTION
INDOOR LOCATION
Company
Location
Company representative
Observer .
Affiliaton.
Date
Industry.
Process unit
Light type (flourescent, incandescent, natural) _
Light location (overhead, behind observer, etc.)
Illuminance (lux or footcandles)
Sketch process unit; indicate observer position relative to source; incicate potential emission
points and/or actual emission points.
OBSERVATIONS
Clock
time
Observation
period!
duration,!
min:sec
Accumulated
emission
time,
min:sec
Begin observation
End observation
Figure 22-2
-------
6.7 Project Participants
-------
The following personnel participated in the test program:
Affiliation Title
Name
Dennis Holzschuh
Kenneth Kloska
Roger Kniskern
William Cesareo
Jonathan Gardner
Laurie Behr
Barbara Drummond
Albert Burton
Bruce Wuebber
Richard Keith
Joel Burke
Peter Rehder
Dana Birkby
Diane Lacy
John Kittredge
Glen Lane
Keith Synnestvedt
EPA
Climax
YRC
YRC
YRC
YRC
YRC
YRC
YRC
YRC
YRC
YRC
YRC
YRC
YRC
YRC
YRC
Technical Manager
Plant Liaison
Project Manager
Project Director
Test Engineer
Test Technician
Opacity Observer
Test Technician
Opacity Observer
Test Technician
Test Technician
Test Technician
Test Technician
Test Technician
Opacity Observer
Opacity Observer
Test Technician
-------
6.8 Work Assignment
-------
WO8X ASSIGNMENT . .
ENVIRONMENTAL PROTECTION AGENCY
•
Research Trianala Par*; N.C, 27711
* • . •
"tie . . . . ' '
Emission Test Metallic Mineral Plant • .
* . * •
gfrA cnwt»*cr no
68-02-2819-
co*jr»ACTO«
York Research '
ASSIGNMENT riO
a 17
ASaidWUsNT CHANQS MO
DAT6
oascjwno* '..... ..•'..•
The Contractor shall perform an emission te.s.t in accordance' '
with the basic contract scope.of work for the Emission Measurement Branch, and as
•set forth in the attached "Source Sampling and Analysis Schedule" .at the following
"site: . '•.-:-.'- .;.'•. • •
. Company: Henderson Project
• Location:, Henderson, Colorado - • •
Industry:' Molybdenum Processing
Project. No.: • 79-M£Tr2.' . • '-
The- Emission Measurement Branch's Technical Manager is Dennis Holzschuh
.Mail Drop 13; .EMS, ESED, OAQPS,. Research Triangle Park, North Carolina 27711.
Upon.notification of approval of the proposed source test report, the Contractor
shall provide 12 copies.of the final report with appendices and
i summary without appendices. ... . . .-.•"•--.
copies as a.
* Zl •
All pretest survey, proposed'final,, and final source test reports and SOTDAT
Data Forms shall be submitted directly to'J. 'E. McCarley,, Emission Measurement Branch,
ESED, MaiT Drop 13, Research Triangle Park, North Carolina 27711. ' -
All samples shall'-'be shipped to: Dennis P.. HoTzschuh '
GOVCRNMgNr XSTIMATg .
2000 man hours
aufATIOM O> WORK
90 days
Nov. 16, 1.979
Dennis P. Holzschuh
coos
ESED/EMB
T6LEPHQ.MC
541-5243
DATE
8/6/79
-------
RCE SAMPLING AND ANALYSIS SCHEDULE
9
Total
Ho. of
jasples
3
3
3
3
3
1
3
3
3
3
Sample
Type
Particulate
Particle
Size
Particulate
Particle
Size
Particulate
Particle
Size
Visible
Emissions
Visible &
Fugitive
Visible &
Fugitive •
Visible &
Fuqitive
Note: This
witho
__ —
-
Sampling
Method
EPA-5
Anderson
EPA-5
Apder?on
EPA-5
Anderson
EPA-9
EPA-9
. EPA-22
EPA-9
EPA-22
EPA-9
EPA-22
test is to b
it wet suppr
—
Acairr-ccr.t Xucbor
Contract m.i 68-02-2819
lonpiny fuse: Uojpjny uociticn:
ClJjiiajLJteQderson Project Henderson^ Co lor ado
i nous try;
-Molybdenum- Processing
Saa'ple
Collected
Jy.
CTR
CTR
CTR
CTR
CTR
CTR
CTR
CTR
CTR
CTR
done fir
ssion sys
Minimus
Sacplina
Tiro .
1 hr
N/A
1 hr
N/A
1 hr
N/A
1 hr
1 hp
1 hr
1 hr
it with th
:em operal
..
Minimum Gas
Volume ,
S jB.pl ed ft4
60 ft3
N/A
60 ft3
N/A
60 ft3
N/A
-
.
.
e wet sup
ing.
K
process! Rai] Car Unlc
primary Crushe
Initial Analysis
Type
Mass
-
Mass
.
Mass
_
-
—
.
iresslon sy
Method
EPA-5
-
EPA-5
_
EPA-5
-'
_
.
tern operat
>ading and Contro1 n»«w»t«
;rs Oucon Wet "Scrubbers
6y
4*
CTR.
-
CTR
_
CTR
-
-
-
.
ng then c
_p1na) Analysis.
Type Method
Dne again
.
^
s Required
It Ion I
KEMRXSl
1. Sampling ihall be pcrforccd with i 102 Ijoklnctlc conditions.
2, Kcthodi arc tPA unless Indicated otherwise.
3. leplngors and analysis of loplnijcr catch will be per tha federal Register. Volura 36,
fa,
-------
iOUflCE SAMPLING AND ANALYSIS SCHEDULE
iling
• t
re
1*
1*
,*
*
>A*
!A*
k
\
*
*
1
*
.*
I
Total
li'O. Of
3
3
3
3
3
3
f*
*l
3
3
3
Sample
Type
Particulate
Particle
Sizing
Particulate
Particle
Sizinq
Particulate
Particle
Sizing
Particulate
Particle
Sizina
Visible
Emission
Visible &
Fugitive
Visible &
Fugitive
•
Sampling
Me thod
EPA-5
Anderson
EPA-5
Anderson
EPA-5
Anderson
EPA-5
Anderson
EPA-9
EPA-9
EPA-22
EPA-9
EPA-22
/ . • — 1
Ccripany name:
— Climax-Henderson Project
industry;
— Molybdenum- Processing
Saaplo
Collected
CTR
CTR
CTR
CTR
CTR
CTR
CTR
CTR
CTR
CTR
CTR
Minimal
Samp lint)
Tint!
1 hr
N/A
1 hr
N/A
1 hr
N/A
1 hr
N/A
1 hr
1 hr
1 hr
..
Minimum Gas
Volune ,
Sampled ft
60 ft3
N/A
60 ft3
N/A
60 ft3
N/A
60 ft3
N/A
-
-
-
, • !f '
process: pebble
8. Mil
,,m*>^m ^
company Location:
Henderson,
Screening
ling
Initial Analysts
Type Method 6y
**
Mass
-
Mass
M
Mass
-
Mass
—
-
-
-
EPA-5
-
EPA-5
_
EPA-5
-
EPA-5
^
-
-
-
CTRt
-
CTR
_
CTR
-
CTR
M
-
-
-
Colorado
Control Equipment:
Wet Scrubbers
Final Analysis
Type Method
•
.
-
- , , ••*"•»-.
•
^
i-jlUneous Swpllni Required
MTont.-actor, cPA-i/ivlroracntJl ProtccKo/i /l(rcncyt.
1. Stcplfng thtll be performed with t 10: isoklnatlc conditions.
2. flcthodt l-'-.
-------
lURCE SAMPLING AND ANALYSIS SCHEDULED
lns
*
*
*
Jc
Ar
—
Totll
KO. of
3
3
>i
*t
3
3
Simple
Type
Particulate
Particle
Sizing
Particulate
Particle
Sizing
Visible
Visible &
Fugitive A
Exit
•
Stapling
IVsthad
EPA-5
Anderson
EPA-5
Anderson
EPA-9
EPA-9
EPA-22
*
Conuoct*,: 68_Q2_2819 |A33i!« Ku.^
lonpony flame: ' i.ompa/iy Location:
—ClJmajsJlejlderson Project Henderson, Colorado
industry: Process! Control Equlpacnti
-Molybdenum Processing Mol-ybdenuro-Oryer Wet Scrubber
Sinpla
Collected
M
CTR
CTR
CTR
CTR
CTR
CTR
f-Method
Minima
Time ™
1 hr
N/A
1 hr
N/A
N/A
1 hr
to be su
. ,
Klnlnug fas
San.pl cd ft1
60 ft3
N/A
60 ft3
N/A
N/A
N/A
plied by
,r
Initial Analysis
Type Method 6y
Mass
Mass
-
-
:PA
EPA-5
EPA-5
-
-
CTR,
CTR
-
- -
Final Analysis,
Type Method
PO 210
PO 210
i
Radio *
Activity
Radio
Activity
.
-
CTR
CTR
^
pn t f 1
n u 1
1.
Sampling thill bo performed with t 10: ttoklncUc conditions.
Methods »
»ra CPA unless Indicated otherwise.
3. I^plngirs and analysis of implnpor citcn will b
San;
ha F
Pro
flccI
-------
tract I
160-iPtmP
ii2
SOURCE SAMPLING AND ANALYSIS SCHEDULE
JTpling
)int
'<>ure
b 1
b 2
Too)
Co. of
jj-plcs
3
3
Sample
Type
Visible &
Fugitive
Visible &
Fugitive
•
Sampling
I'cthoJ
EPA-9
EPA-22
EPA-9
EPA-22
1 lonpany ftawc: uupany tocniun:
C-UinaxOtenderson Project Hende.rson^Colorado
industry: Process: Control equipment: . .
1 -Molybdenum Processing Ta.tUng nisposal Subaqueous Deposition
Saaple
Collected
M
CTR
CTR
Klnimuo
SacipHng
limo .
1 hr
1 hr
— »
Hinlmura fijj
Volume .
San.pl ed ft
N/A
N/A
-------
URGE SAMPLING AND ANALYSIS SCHEDULED
"9
•
—
Toll)
Co. of
J»cy\ci
3
3
Sample
Type
Visible &
Fugitive
Visible &
Fugitive
.
Sinpl ing
Ms thod
EPA-9
EPA-22
EPA-9
EPA-22
»
(/Uaigaccnt Uucbor
lo.-ipopy tome: Loupjny tocmon:
Cl-imax-4teaderson Project ___ .Henderson^- Co lor ado
inousiry: Proccsi: Control Cqutpacflt:
— Molybdenum-Processing — Gearee-Ore Stockpiles Wet Suppression
Sample
Collected
iy
CTR
CTR
•
Minimum
Sampling
Tiro .
1
1
, •
Minimum fas
Volume %
SanpleiJ ft1
CTR
CTR
•!
Initial Analysis
Type fie thod 6y
4*
*•
'
Final Anatysjs.
Typ«
1
Method
.
• /X^'x
•
/->
jncous
Required
tl
------- |