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FINAL REPORT
to
MINNESOTA ENVIRONMENTAL QUALITY BOARDREGIONAL COPPER-NICKEL STUDY
Mineral Processing Studies
Dust Generation in Crushing and Handling
Mineral Resources Research CenterUniversity of Minnesota
Apri 1 24, 1980
This document is made available electronically by the Minnesota Legislative Reference Library as part of an ongoing digital archiving project. http://www.leg.state.mn.us/lrl/lrl.asp
FINAL REPORT
to
Minnesota Environmental Quality Board
Regional Copper-Nickel Study
Mineral Processing Studies
Dust Generation in Crushing and Handling
by
I. IwasakiK.A. SmithP.L. Glader
Mineral Resources Research Center56 East River Road
University of MinnesotaMinneapolis, Minnesota 55455
April 24, 1978
DUST GENERATION IN CRUSHING AND HANDLING
The purpose of the present investigation is to provide data that will
permit reasonable extrapolation on the amount and character of dusts to
be generated in the crushing and handling of copper-nickel bearing Duluth
gabbro. No direct measurements of dust concentrations near a pilot-plant
crusher operating on Duluth gabbro samples would simulate the real situation
in a crusher plant or the air effluent from the dust collection system. It
was proposed, therefore, that the following four sets of experimental data
be used to estimate by extrapolation the potential dust generated not only
in crushing, but also from conveyors, loading and transfer s~ons, and
storage piles.
1. "Dust data" in crusher building; and air effluents from
operating taconite plants.
2. Size distribution of crushed products from each stage
of the taconite plant crushing process, especially in the micron size
range.
3. Size distribution of the taconite samples crushed in each
stage of the MRRC pilot plant.
4. Size distribution of Duluth gabbro samples crushed in each
stage of the MRRC pilot plant.
Although such' an approach could not give precise quantitative information
the data could be utilized to estimate the dust generation potential in
a semi-quantitative manner.
Ideally, the "dust data" and the taconite samples should be collected
simul taneously. Several different taconite p'.ants with different degrees
of dust control facilities, including a plant meeting EPA new source
performance standards should be sampled. Furthermore, about half a
dozen samples of Duluth gabbro to cover a range of texture and degree
of mineralization should be included. The size distribution data of
both the taconite and Duluth gabbro samples in the MRRC pilot plant are
necessary since the distribution characteristics of crushed products
differ for different materials and for different crushers. Due to the
Copper-Nickel budget constraints, however, the number of taconite and
Duluth gabbro samples in the present report was limited to one s~Ple
each.
For comparative crushing studies of copper-nickel crude and taconite
samples approximately a one-ton sample of 4 to 6-inch lumps of copper-
nickel crude sample was hand picked from the AMAX Sample 2 pile. Three
drums of taconite lumps weighing in excess of one ton were received from
Erie Mining Company on November 22, 1977. The flowsheet for the crushing
studies, patterned after the Erie plant flowsheet, is shown below. The
crushers at MRRC were a lO-inch x 20-inch Traylor jaw crusher and a 2-foot
Symons cone crusher.
One-ton Sample
JJaw Crusher (-2 1/2 inch)
\
JCrushed Sample
Screen (1/8 inch)
1. d1.OverSlze Un erSlze
1Cone Crusher (-1 inch)
rCrushed Sample
The size distributions of the jaw crusher, minus 3/8-inch screen, and
the cone crusher products were determined using testing screens to 200 mesh
and then microscreens wet to 10 ~m. Originally, the minus 200-mesh fractions
were to be fractionated with an air classifier by the Donaldson Company, but
sufficiently large samples of the minus 200-mesh fractions were not obtained.
The results are given in Tables 1 and 2, and the size distribution data are
plotted in Figures 1 and 2 in terms of cumulative percent weight passing
versus particle diameter on a log-log paper. It is apparent both in the
tables and figures that the jaw crusher product of the taconite sample was
coarser than that of the Duluth gabbro sample, but that the size distributions
of the minus 3/8-inch screen products and the cone crusher products were
similar.
To investigate if the copper and nickel contents might segregate upon
crushing, the size fractions were combined in regular intervals and analyzed.
The analytical results are included in Table 2(a). Both the copper and nickel
contents showed tendencies to increase in finer size fractions. A head
sample was prepared by reconstituting the minus 3/8-inch screen product
and the cone crusher products in proportion to the weights and analyzed.
The head analysis is given in Table 3.
TABLE 3. HEAD ANALYSIS OF DULUTH GABBRO SAMPLE
Constituent Percent
Copper (Cu) 0.90
Nickel (Ni) 0.20
Cobalt (Co) 0.032
Iron (Fe) 12.99
Sulfur (S) 1.74
TABLE 1. SIZE DISTRIBUTIONS OF CRUSHED PRODUCTS OF ATACONITE SAMPLE FROM ERIE MINING COMPANY
-3/8" Cone CrusherJaw Screen Product Product
Crusher (5.07% (94.93%Size Product by Weight) by Weight)
+3 inch 41.12
+2 29.74
+1.5 9.91
+1 6.35 3.93
+0.742 3.38 16.85
+0.525 2.87 0.04 28.53
+0.371 1.93 0.07 18.69
+3 mesh 1.27 6.24 10.20
+4 0.79 14.44 5.33
+6 0.61 14.46 3.86
+8 0.46 12.24 2.82
+10 0.34 9.76 2.11
+14 0.25 7.90 1.36
+20 0.18 6.07 1.27
+28 0.14 5.01 0.93
+35 0.09 3.41 0.65
+48 0.09 3.64 0.70
+65 0.07 2.74 0.50
+100 0.06 2.38 0.42
+150 0.07 2.29 0.38
+200 0.05 1.59 0.19
+37 11m 0.10 3.37 0.47
+20 0.05 1.85 0.30
+10 0.03 0.83 0.17
-10 0.05 1.67 0.34
TABLE 2(a). SIZE DISTRIBUTIONS OF CRUSHED PRODUCTS OF MRRC LOT 2DULUTH GABBRO SAMPLE FROM AMAX
Jaw Crusher -3/8" Screen Product Cone Crusher ProductProduct (5.22% by Weight) (94.78% by Weight)
Size % Wt % Cu % Ni % Wt % Cu % Ni % Wt % Cu % Ni
+3 inch 35.78
+2 29.48 * *+1.5 8.47
+1 6.06 1.62
+0.742 3.29} 14.06 0.73 0.18+0.525 3.33 0.65 0.19 32.71
+0.371 2.36 o.lO} 18.82
+3 mesh lo67} 0.72 0.26 2.54 0.89 0.19 9.48} 0.80 0.18+4 1.16 7.28 5.10
+6 O.99} 0.86 0.25 9.00} 1.05 0.26 3.63} 0.90 0.20+8 0.79 8.20 2.62
+10 O.73} 1.03 0.255 7.S8} 1.07 0.27 2.0S} 0.96 0.225+14 0.62 6.78 1.54
+20 O.S8} 1.27 0.295 6.26} 1.17 0.28 lo28} 1.21 0.27+28 0.56 5.67 1.11
+35 O.4S} 1.20 0.26 S.64} 1.16 0.26 O.79} 1.28 0.275+48 0.53 5.62 1.01
+65 O.S6} 1.05 0.255 6.86} 1.16 0.265 O.86} 1.30 0.275+100 0.43 5.80 0.80
+150 o.71} 1.01 0.27 6.lS} 1.14 0.295 O.76} 1.40 0.31+200 0.37 3.97 0.53
-200 1.08 1.32 0.405 12.50 1.32 0.40 1.23 1.75 0.395
*Analyses not available
TABLE 2(b). SIZE DISTRIBUTIONS OF THE MINUS 200-MESH FRACTIONSOF CRUSHED PRODUCTS OF MRRC LOT 2 DULUTH GABBROSAMPLE FROM AMAX
Size
Jaw CrusherProduct
% Wt % Cu % Ni
-3/8" Screen Product(5.22% by Weight)
% Wt % Cu % Ni
Cone Crusher Product(94.78% by Weight)
% Wt % Cu % Ni
A. Sized by Microscreening
+37 llm 0.67 1.23 0.385 6.89 1.29 0.41 0.66 1.63 0.39
+20 0.16 1.45 0.50 2.18 1.40 0.45 0.21 1.55 0.40
+10 0.07 1.80 0.54 0.69 1.52 0.50 0.06 2.83 0.66
-10 0.18 2.16 0.39 2.74 2.17 0.31 0.30 2.29 0.38
Composite 1.08 1.45 0.41 12.50 1.52 0.40 1.23 1.84 0.40
B. Sized by Sedimentation Sizing
+37 llm 0.74 1.41 0.44
+20 0.16 1.07 0.32
+10 0.09 1.31 0.35
-10 0.09 1.29 0.30
Composite 1.08 1.34 0.40
1OCt . 2 3 5 6 7 8 9 1 3 4 5 6 7 8 9 1 2 3 4 5 6 7 8 9 1 2 3 4 5 6 7 89 1 ,2 3 4 5 6 7 B 9 19 'I I ,i 1 , ' I ' I,,' 'e" ,_ .,.. ._ ", I I: I I ,i.l.l:..#!:t: • IJ.... I I' ,f I I ' Iii i : 'I I, 'L_,',l"~=~il
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Particle Size, ~m
FIGURE 1. SIZE DISTRIBUTIONS OF CRUSHED PRODUCTS OF A TACONITE SAMPLE FROM ERIE MINING COMPANY
50,000 100,00010,00050001000500100SO
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Particle Size, ~m
FIGURE 2. SIZE DISTRIBUTIONS OF CRUSHED PRODUCTS OF MRRC LOT 2 DULUTH GABBRO SAMPLE FROM AMAX
In a separate investigation the minus 200-mesh fractions of pilot
plant flotation tailing samples were sized with microscreens and each
size fraction was analyzed for copper and nickel. The copper contents
of minus IO-~m fractions were noted to be unexpectedly high. Similar
trends were noted in the analytical results of microscreened fractions
of the presentsamples as shown in Table 2(b). Since all the water
samples used in microscreening (amounting to approximately 3 liters)
ended with minus IO-~m fractions and were removed by evaporation in
order to recover all the dissolved elements, the high copper contents
of minus IO-~m fractions were suspected to be due to dissolution
of the brass rims of the microscreens. Hence, the minus 200-mesh product
of the Jaw Crusher Product was fractionated into the same size ranges
using the sedimentation sizing method. The results shown in Table 2(b)
show that the copper content of the minus IO-~m fraction was appreciably
less and the composite analysis of the minus ZOO-mesh fraction was more
in line with the analytical data in Table 2(a). It is evident that the
sedimentation sizing method rather than microscreens should have been
used to avoid sample contamination.
The head sample and the minus lO-~m fractions of the three products
of the crushed Duluth gabbro were submitted to the Regional Copper-Nickel
Study for shipment to Barringer Research Ltd. for analysis of elemental
composition. The results received from Barringer are given in Table 4.
A comparison of the analytical results on the Jaw Crusher Product frac-
tionated by microscreening and sedimentation sizing, particularly those
of copper and zinc, suggests that the corrosion of microscreens affected
the analytical results of these two elements. Since the head sample and
the Jaw Crusher Product fractionated by sedimentation sizing were free
from such contamination, more importance should be given to these two
TABLE 4. TRACE ELEMENT ANALYSIS RESULTS IN PERCENT ON MRRCLOT 2 DULUTH GABBRO SAMPLE FROM AMAX AND ON MINUS10-~m FRACTIONS OF ITS CRUSHED PRODUCTS
Minus 10-~m Fraction of Crushed Products-3/8" Screen Cone Crusher
Jaw Crusher Product Product ProductHead (microscreen) (sedimentation) (microscreen) (microscreen)
Al 8.55 7.79 6.61 6.46 8.31
B
Be 0.00012 0.00009 0.00005 0.0001 0.00009
Ca 5.1 4.38 3.86 4.04 5.27
Cu 0.999 2.52 * 1.21 2.46* 2.63*
Fe 13.8 15.6 10.8 20.5 14.4
Mg 4.28 4.05 2.97 3.39 3.88
Mn 0.132 0.143 0.134 0.219 0.126
P nd nd nd nd nd
Ba 0.0258 0.0129 0.0667 0.0134 0.0098
Se
Te
As
Si
Sr 0.0239 0.022 0.0205 0.0189 0.0252
Zr 0.012 0.0116 0.00783 0.00884 0.0123
Ti 1.09 0.935 0.638 0.929 0.955
V 0.0162 0.0151 0.0096 0.0233 0.0135
Zn 0.0113 0.364 * 0.0579 0.41 * 0.257 *
Th 0.0004 0.0005 0.00049 0.0008 0.0007
K 0.767 0.655 0.596 0.61 0.593
Na 2.4 1.67 1.58 1.12 1.92
Cd nd nd 0.0009 nd nd
Cr 0.0126 0.0132 0.0141 0.0017 0.014
Co 0.018 0.0263 0.0191 0.0239 0.0258
Ag 0.0002 0.0007 0.0008 0.0007 0.0008
Mo 0.0008 nd 0.002 0.0027 nd
Ni 0.17 0.346 0.21 0.284 0.326
Pb 0.005 0.024 0.012 0.0265 0.029
*Contamination through corrosion of microscreens suspected
sets of data. It is evident that copper, zinc, silver and nickel tended
to increase their concentrations somewhat in the 'dust' fraction upon
crushing, indicating that sulfide minerals were broken to finer sizes
more readily, but all the other elements did not change their concentrations
significantly.
SUMMARY
Duluth gabbro and taconite lumps crushed through a pilot plant jaw
crusher and cone crusher gave similar size distributions. Therefore,
it was surmised that the dust generation potential in crushing Duluth
gabbro would be similar to that in the existing crushing facilities
for taconite. Though sulfide minerals tend to break somewhat preferen
tially, there were no unusual concentrations of any trace elements in
the potential dust fraction.