U.S. patent number 3,926,793 [Application Number 05/350,241] was granted by the patent office on 1975-12-16 for mineral separation apparatus.
Invention is credited to James Charles Wise.
United States Patent |
3,926,793 |
Wise |
December 16, 1975 |
Mineral separation apparatus
Abstract
An oscillating mineral dressing table which may be easily
adapted for automation, and provides for continuous particle
concentration, classification, sizing, shape sorting and flotation.
The mineral separating apparatus provides an elongated planar
porous member which is inclined to the horizontal and vertical
planes. Mineral feed is introduced along the higher lateral side of
the porous member and the mineral is separated by oscillating this
member in the direction of the lateral side through a liquid
medium. By this mechanism the coarsest highest density particles
are caused to climb up the lateral incline of the porous member
whilst the finer less dense particles are displaced to the lowest
end of the member. The mineral process flow is transverse to the
direction of oscillation, that is, in the longitudinal direction of
the porous member. The application of the dressing table with its
multi-range of operational variables and its increased sensitivity
is particularly suitable for increasing the usable output of lean
mineral feeds.
Inventors: |
Wise; James Charles (Epping
West, New South Wales 2121, AU) |
Family
ID: |
3764984 |
Appl.
No.: |
05/350,241 |
Filed: |
April 11, 1973 |
Foreign Application Priority Data
|
|
|
|
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Apr 12, 1972 [AU] |
|
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8578/72 |
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Current U.S.
Class: |
209/426; 209/44;
209/504; 209/170; 209/508 |
Current CPC
Class: |
B03B
5/36 (20130101); B03B 5/02 (20130101) |
Current International
Class: |
B03B
5/00 (20060101); B03B 5/28 (20060101); B03B
5/36 (20060101); B03B 5/02 (20060101); B03B
005/12 () |
Field of
Search: |
;209/422-427,503,504,508,170,367,441,448-450,446,44 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Lutter; Frank W.
Assistant Examiner: Hill; Ralph J.
Attorney, Agent or Firm: Ladas, Parry, Von Gehr, Goldsmith
& Deschamps
Claims
What I claim is:
1. A mineral separating apparatus comprising a housing containing
therein a substantially elongated planar porous means, said porous
means being inclined relative to the horizontal and vertical planes
such that there is an upper and lower lateral and longitudinal
side, means for adjustably controlling the said incline of the said
porous means, oscillating means to oscillate said porous means in a
direction parallel to the lateral side, a power means connected to
said oscillating means whereupon initiation of said power means
said porous means oscillates in a substantially sinusoidal or
arcuate path, said porous means being further immersed in a body of
liquid such that by the action of the oscillations and said body of
liquid mineral feed which is introduced onto said porous means
travels upwardly on the porous means in a direction substantially
parallel to the lateral side whereby the coarsest highest density
particles of the feed are arranged substantially along the upper
longitudinal side whilst the fine least dense particles are
arranged along the lower longitudinal side, and whereby the
material product travels downwardly in a direction substantially
transverse to the direction of oscillation to discharge at a
product outlet.
2. The apparatus as claimed in claim 1 where there is provided
means for controlling the amplitude of said oscillation and a means
for controlling the speed of oscillation.
3. The apparatus as claimed in claim 1 wherein the said means for
adjustably controlling the incline of the said porous means is a
screw means and the oscillating motion is controlled by pivot arms
attached at one end to an eccentric shaft and the adjacent end to
the longitudinal side of said porous means.
4. The apparatus of claim 1 wherein the said body of liquid is a
rising body of liquid introduced to the said housing through a
manifold connected to a distributor portion of said housing located
beneath the said porous means, such that liquid passes through said
porous means to a liquid outflow in the form of a weir located
along one or more sides of the housing above the said porous
means.
5. The apparatus as claimed in claim 1 wherein the body of liquid
is water.
6. The apparatus of claim 1 wherein the planar porous means is a
rectangular sieve.
7. The apparatus as claimed in claim 1 wherein the said means for
adjustably controlling the incline of the said porous means are
hydraulic rams and the oscillating motion is controlled by a
hydraulic ram connected at one end to an eccentric shaft and at the
adjacent end to the longitudinal side of said porous means.
8. A method for separation of mineral feed in an oscillating
apparatus comprising the following steps:
adjusting the incline of a substantially elongated planar porous
means such that said porous means is inclined relative to the
horizontal and vertical planes whereby the porous means has an
upper and lower lateral and longitudinal side,
initiating a power means to oscillate said porous means in a body
of liquid along a substantially sinusoidal or arcuate path said
oscillations being in a direction parallel to the lateral side,
and introducing the mineral feed onto said porous means whereupon
the mineral feed travels upwardly on the porous means in the
direction of the lateral side such that the heaviest fraction of
the feed is arranged substantially along the upper longitudinal
side and said mineral further travels downwardly in a direction
substantially transverse to the direction of oscillation to
discharge at a product discharge.
9. The method as claimed in claim 8 wherein finest highest density
particles of the mineral feed are collected at the bottom of said
housing and finest least dense particles of the mineral feed are
collected at the overflow of the rising liquid discharge.
10. The method as claimed in claim 8 wherein the said body of
liquid is a rising body of liquid passing through said porous
means.
Description
This invention relates to separators and more particularly to
vibrating mineral dressing tables.
In general, many industries suffer from the lack of a machine which
will
A. CONCENTRATE AND/OR CLASSIFY WITH SUFFICIENT SENSITIVITY COARSE
SIZED MINERALS SUCH AS MINED ROCK, GRAVELS AND THE LIKE;
B. CONCENTRATE AND/OR CLASSIFY WITH SUFFICIENT SENSITIVITY IN THE
CRUSHING SECTIONS OF TREATMENT PLANTS;
C. DETERMINE OR HELP DETERMINE THE "GRAIN SIZE" OR "LIBERATION"
CHARACTERISTICS OF MINERALS AND THE LIKE, PARTICULARLY DURING
PROCESSING;
D. INCREASE THE CLASSIFICATION, GRINDING, FLOTATION EFFICIENCIES OF
MINERAL TREATMENT PLANTS AND THE LIKE.
The above are only a few examples to illustrate the need for new
methods and machines. It is the object of this invention then, to
provide the primary, secondary, building and construction
industries with:
A. a gravity concentrating machine for general application.
B. a gravity classifying machine for general application.
C. a sizing machine for general application.
A shape sorting machine for general application.
E. a flotation machine
F. a machine capable of providing accurate and/or relative
liberation characteristics of minerals, mineral particles and the
like for "on stream" control of plants either under computer or
manual control, for research or the like.
G. a machine capable of providing advance information of flotation
and/or gravity recovery patterns so that process controls can be
varied within sufficient time to provide optimum or improved
recovery or throughput or the plant.
H. a machine capable of concentrating, classifying and/or sizing
minerals and such like from alluvial and hard rock mining, from
boulder size through gravels, crushed rock and fines. In addition
to the above sub-paragraphs a, b, c and d, this application and
methods of the present invention is aimed at decreasing the "cut
off" grade of a mine, ore deposit and the like, thereby increasing
the reserves and follow on values.
i. a machine capable of classifying and/or concentrating minerals
in the crushing circuits of mineral treatment plants and the like,
such that:
1. general crushing can be extended to finer sizes.
2. fractions of mineral sizes that would be best suited for coarse
ball milling, fine ball milling or the like, and finished product.
Such fractions would then be sent to appropriate machines thus
by-passing the rod mill process and thereby increasing plant
efficiency, capacity and throughput.
3. concentration of liberated minerals and the like can be achieved
e.g., tin circuit, so that sliming loss ocasioned by unnecessary
further comminution (rod or ball milling) is avoided thereby
increasing recovery and plant profitability.
j. a machine capable of classifying and/or concentrating a ground
mineral product or the like, particularly a rod mill product, such
that fractionation of particles coarser than efficient operation of
current cyclones or classifiers and processing through mills best
suited for such sizes results in improved efficiency and/or
throughput. Likewise, overgrinding of coarser liberated particles
is minimised.
k. new methods of treatment of minerals and the like arising from
the invention. These new methods are generally covered by
sub-paragraphs f through to j above, either singularly or in
multiple combinations thereof.
Two particular features of the present apparatus are the
sensitivity of the apparatus and the range of operational
variables. Such variables include: variable fluid flow, variable
densities and viscosities of fluids by initial selection, variable
speed and amplitude of deck oscillation, range of sieves and
variable deck path geometry (including longitudinal incline,
lateral incline, angle of oscillation -- equal on radii, angle of
oscillation -- unequal on radii, equal length radii for
oscillation, unequal length radii for oscillation). Since the sieve
or porous member is elongated in shape preferably rectangular, the
terms `longitudinal` and `lateral` are herein used refer to longer
and shorter lengths or axes respectively of the sieve or porous
member. The apparatus is designed on the maximum utilisation and
application of these variables to produce the sensitivity of
separations or of deliniations for the most difficult application,
namely, relative liberation parameters. The application of the
apparatus then, is for the functions of gravity concentration,
classification and sizing, shape sorting, and flotation with
application in the primary, secondary building and construction
industries. Due to the characteristics and applications of the
machine, new methods for treating fractured rocks, gravels, mineral
particles and the like are established.
Broadly, the apparatus of the present invention provides a mineral
separating apparatus comprising a housing containing therein a
substantially elongated planar porous means, said porous means
being inclined relative to the horizontal and vertical planes such
that there is an upper and lower lateral and longitudinal side,
means for adjustably controlling the said incline of the said
porous means, oscillating means to oscillate said porous means in a
direction parallel to the lateral side, a power means connected to
said oscillating means whereupon initiation of said power means
said porous means oscillates in a substantially sinusoidal or
arcuate path, said porous means being further immersed in a body of
liquid such that by the action of the oscillations and said body of
liquid mineral feed which is introduced onto said porous means
travels upwardly on the porous means in a direction substantially
parallel to the lateral side whereby the coarsest highest density
particles of the feed are arranged substantially along the upper
longitudinal side whilst the fine least dense particles are
arranged along the lower longitudinal side, and whereby the
material product travels downwardly in a direction substantially
transverse to the direction of oscillation to discharge at a
product outlet.
More particularly, the machine of the present invention can be
likened to a rectangular box, or upper container inclined in the
horizontal plane along both the longitudinal and lateral axis, with
a porous screen fitted at the bottom thereof. The incline of the
upper container and screen thus effectively provides relative to a
horizontal plane, a high and low side of the longitudinal or longer
sides and a high and low side of the lateral or shorter sides of
the upper container and screen. The screen, with the aid of upward
rising fluid, provides a support for the mineral particles. The
upper container including the screen oscillates in the lateral
direction which largely gives rise to particle separations, while
the longitudinal incline gives rise to process flow. The
oscillation of the upper container and screen cause these integers
to scribe a substantially sinusoidal or arcuate path. This
oscillating action combined with an upwardly rising body of liquid
results in the heaviest densest particles climbing upwardly in the
lateral direction, that is, in the direction of oscillation whilst
the finer less dense particles are displaced to the lowest lateral
end of the screen.
The mineral process flow is in the direction of the longitudinal
side, that is transverse to the direction of oscillation, and as
such indicates a time constant of the particles on the screen.
Material to be treated is introduced onto the upper inclined
longitudinal end of the deck box and the products are removed
from:
a. the other end of the deck box, where splitters keep the products
separate (concentration, classification, sizing)
b. the deck box fluid overflow (classification, density,
separations, flotation)
c. from the under deck or liquid distributor (jigging
arrangement)
The fluid utilised in this process could include for example,
water, hydrocarbons and other such liquids, "heavy liquids" e.g.,
tetrabromoethane, bromoform and such like, heavy liquids such as
water or hydrocarbon base and such like containing dissolved salts,
and suspended particles commonly referred to in the art as "heavy
media". When this apparatus is used as a flotation machine, gas
(usually air) is also introduced with the fluid, under the porous
screen.
The invention will now be more particularly described by way of
example only, with reference to the accompanying drawings
wherein:
FIG. 1 is an end elevational view of one form of the invention.
FIG. 2 is a plan view of the invention in FIG. 1 with the screen
and base removed to more clearly show the liquid inlet and the
dense "fines" product outlet.
FIG. 3 is an end elevational view of another form of the invention
with the hopper discharge removed for clarity.
FIG. 4 is a plan view of the invention in FIG. 3.
FIG. 5 is a perspective view of the invention of FIGS. 1 and 2.
FIG. 6 is a perspective view of the invention of FIGS. 3 and 4 with
the screen removed to more clearly show the base.
To simplify the description, identical numerals will be used
throughout the specification to designate identical integers of the
invention.
Referring to the drawings, and in particular to FIGS. 1 and 2, the
framework in general consists of two sections. The first is a main
frame section which provides a base for siting and indirectly
fastening the apparatus of the present invention to the appropriate
foundations. The other is the sub-frame section, to which the
apparatus is directly fastened. The sub-frame section then, is
pivotly connected above the main frame section by means of
adjusting screws or hydraulic or pneumatic rams which may be locked
in any desired position. By altering the position of the subframe
relative to the mainframe, any appropriate longitudinal incline of
the deck may be achieved.
The fluid containing under deck distributor box with its associated
centrifugal pump and ducting means is attached to the fixed
mainframe section. Whilst mounted on the adjustable subframe is an
oscillator apparatus together with its motor and associated drive
train.
For the sake of simplicity the mainframe and subframe sections have
not been illustrated in the drawings. However, the frames should
preferably be fabricated from steel unless the apparatus is used in
a corrosive environment, wherein special precaution may be
necessary. In general however, the framework especially the
mainframe, should be of sufficient mass to absorb the vibration
caused by the oscillating deck. Fabrication section could be angle,
channel, hollow rectangular, I-beam and plate depending on size and
duty.
More specifically, the apparatus of the present invention provides
an assembly 10, which includes an upper container or deck box 19,
and a lower container or liquid distributor 23. Separating the deck
box 19 from the liquid distributor 23 is a base 21 over which is
tightly stretched a screen 20. As may be seen from the plan view in
FIG. 2, the deck box 19 is of rectangular shape, however in
elevation as may be seen from FIG. 1 one side wall along the
longitudinal length of the deck box is higher than the side wall of
the adjacent longitudinal length. A weir overflow 29 is situated on
the higher side wall along the longitudinal side wall of the deck
box 19 and a liquid outlet drain 30 is positioned directly adjacent
the weir 29. The base 21 has a planar rectangular configuration and
is inclined in the horizontal plane along both the longitudinal and
lateral axis when positioned in the deck box 19. As mentioned
previously the incline in both the longitudinal and lateral
direction effectively provides, relative to a given horizontal
plane, a high and low side along both the longitudinal and lateral
sides of the base 21 and screen 20.
The screen 20 may be made from any convenient porous material such
as woven metal, rubber or plastic; punched plate; sintered metal or
porous plastic. However aperture size of the screen should be
sufficiently large as to avoid clogging or blinding by the process
mineral.
In one form of the embodiment (FIGS. 1 and 2) the container base 21
connects the lower deck or liquid distributor 23 by means of a
flexible saw-tooth member 44 made of any convenient material such
as rubber ply. The lower container 23, which is immovably contained
in the main frame assembly is a simple bin structure with a
converging bottom. Along one side of the sloping bottom are
connected fluid inlet tubes 25, whilst along the other sloping side
at the point of convergence of the sloping sections, are connected
several off-take product outlets 24.
Product discharge hoppers 22 are attached to the lower end of the
base 21 and along the lower most lateral side of the deck box 19.
Attached to the top of the deck box 19 at the product discharge
end, is also a splitter support bar 36, which supports splitters
38. The splitters 38 are substantially inverted T-shaped plates
whereby the lower end of each plate extends into the discharge
hopper 22 whilst the upper end is allowed to slide along the
support 36 to divert the different mineral fraction into separate
product discharge hoppers 22. The splitters 38 seal against the
screen 20 and are further held in position by any convenient
fastening means (not shown) which may be attached to the splitter
support bar 36.
The product discharge is by the hoppers 22 for the fine fractions
of mineral, however for the larger fraction sizes because the
hopper opening may be too small, continuous elevator bucket (not
shown) may be employed. The elevator bucket may be a separate
motorised unit mounted to the sub-frame with adjustable means for
controlling the positioning and the speed of rotation. The bucket
then extends from the hopper and catches the larger mineral
particles, to later deposit them onto a conveyor system. The drive
for the elevator may be attached to the top pulley of the elevator
system such that the lower pulley runs in the mineral fraction and
fluid. Needless to say all bearings should be suitably sealed
against entry of the fluid or solid to prevent damage.
The vibrating mechanism includes an eccentric shaft 13 which is of
robust constructions to prevent secondary vibration of the deck box
19 containing the base 21 and the screen 20. The shaft 13 is
mounted to the sub-frame via sealed anti-friction bearing and
housing arrangements 37. These shaft bearings 37 are located close
to each side of the two connecting rods 14 to aid in preventing
shaft deflections. The shaft 13 may also be fitted with two or more
anti-friction eccentric bearings and a driven sheave or coupling if
required.
The pivot arm arrangement consists of an outer arm 16 and an inner
arm 17, and the machine generally carries two or more sets of these
arms depending on size and weight of the deck box 19. One end of
each of the outer pivot arms 16 is attached to a connector rod 14.
One end of the inner pivot arms 17 is attached to the longitudinal
side of the deck box 19 via lugs 45. The other ends of the pivot
arms 16 and 17 are mounted to a common pivot shaft 28. The inner
arms 17 being firmly fixed to the shaft 28 while the outer arms 16
are mounted on bushes or bearings so that both the arms can be
adjusted inwardly or outwardly in relation to each other by means
of a pivot arm adjusting link 18, to provide variation for angle of
deck oscillation. The inner pivot arm 17 is yolked at the shaft
end, and acts as a thrust bearing for the outer pivot arm 16 which
is also fitted onto the pivot shaft 28 between the yolk of the
inner pivot arm 17.
The pivot arm shaft 28 is robust and should also be supported by
anti-friction bearings 37 on either side of each of the two or more
pivot arms 16 and 17 further at intermediate locations if necessary
on the large machines. As previously stated the shaft 28 is mounted
to the sub-frame such that one or more of the anti-friction thrust
bearings carry the thrust imposed by the longitudinal incline. By
appropriate adjustment of the pivot arms, incline of the deck 10
can be varied in the lateral direction i.e., angle ABC in FIG. 1
which controls the angle of oscillation can be varied.
The connecting rods 14 transmit the power and convert the motion
from the eccentric bearings 12 to the pivot arms 16 and 17, such
that the deck box 19 which contains the base 21 and screen 20 is
caused to oscillate. Preferably, also provision is made on the
connecting rods 14, for altering the point of attachment of the
outerarms 16 to provide the variation in amplitude of oscillation.
Alternatively and/or in addition, adjustable eccentric
anti-friction bearings (e.g., double eccentric) may also be
installed to further extend the adjusting range of the amplitude of
the deck box 19. The connecting rods 14 should be rigid and to
achieve the lightest weights, aluminium alloys, steel hollow or
I-sections may be used.
Left and right hand threaded adjustment rods 18 with a
corresponding nut and lock nut further provide means or power
transmission and angle of oscillation adjustment. The rods 18 are
made free from flex and are as light as possible but consistant
with strength and rigidity.
On the side of the deck box 19 opposite the pivot arms, are the
idler arms 26 which support the upper longitudinal side of the deck
box 19, via lugs 45. The other ends of the idler arms 26 are
connected to a support 27 which is adjustable by threaded rods and
nuts in the vertical and horizontal planes to provide variation in
the angle of deck incline and angle of oscillation respectively.
These arms 26 are in the form of rods with left and right hand
threads and they also include corresponding nuts and lock nuts to
provide adjustable variations in the radius of oscillation. The rod
attachments at the deck box 19 and support 27 include, again sealed
bearings or bushes and pins.
The centrifugal pump installation consists of a hopper, motor drive
and pump, control valves, by-pass lines and delivery piping
manifold and the like, all generally mounted to the main frame. The
hopper 31 receives liquid from the liquid outlet drain 30, from a
make up liquid supply mains via tubing 35 and from the pump closed
circuit by-pass line 34. The hopper 31 would generally be fitted
with a level control valve on the make up liquid supply mains to
stabilise the pressure head on the pump 32 thereby minimising
surging within the liquid distributor 23. The pump 32 should also
preferably be matched to the specific delivery specifications for
each application and would generally be a centrifugal type suitable
for slurry operations. The motor may be a constant speed type motor
or a D.C. variable speed type with controls to compliment the range
of fluid supply which would help minimise liquid surging by closely
matching the impeller speed required. The delivery pipeline 33
comprises a manifold arrangement with distributing baffles at each
inlet 25 to distribute the fluid more evenly throughout the
distributor 23.
Generally the machine can be fitted with calibrations and
instruments to enable setting of controls to known or trial
settings. For automatic control and computerisation, the machine
can be fitted with sensors for every variation such as flows,
speeds, linear measurements, geometric angles and such like.
Power supply is normally electric however provision can be made for
alternate sources. The motor 11 for the eccentric drive 13 can be
mounted to the sub-frame or elsewhere as appropriate. Transmission
of power is by conventional sheaves and belts (V, poly-V, gear
type) unless large designs demand direct shaft couplings via
running in oil reducer drive.
Referring now more specifically to FIGS. 3 and 4, this alternative
embodiment is aimed particularly for automation.
In this design, the base 21 is itself the distributor individually
and consists of a plurality of individually sealed channels (not
shown) each connected via flexible hosing and including volume
control valves to the pump discharge or mains manifold. The deck
box 19 is made as light as possible and constructed in steel,
aluminium or its alloys, fibreglass or the like. The deck box 19 is
connected to the base 21 by means of suitable quick release clamps
which in so doing, positions and seals the porous screen
therebetween. This arrangement facilitates quick changing of the
porous screens to meet any new desired needs or in the event the
screen becomes damaged.
In this arrangement also the pivot arms which are actually rear
idler arms 40, connect at one end to lugs 45 located on the upper
longitudinal side of the upper deck box 19, and at the other end to
base block 43. The opposite longitudinal side of the deck box 19 is
similarly supported by a front idler arm 39. The arms 39 and 40 are
hydraulic rams which do not transmit power but merely support the
deck box 19 and its load. The rams however, do provide a means for
variation of the radius of deck oscillation and lateral incline
angle of deck base 21 by variation of the idler arm length. It
should be noted that in this arrangement either the bases for the
idler arms 39, 40 can be made variable in the lateral direction by
hydraulic rams such as ram 41 while maintaining a fixed length on
the connecting rod 42; or the connecting rod 42 can be made
variable in length to achieve the same effect. In any case either
the front idler arm base (not shown), or the rear idler arm base 43
can be made variable to provide suitable means for variation of the
angle of oscillation of the deck box 19 via rams 39 and 40. Still
further variations in the angle of oscillation may be achieved by
manipulation of the hydraulic ram 42.
The above embodiment, then is particularly suitable for automation
because of the relative ease in which all the variables may be
controlled through say a programmed computor or such like central
control device.
Referring particularly to FIGS. 1 and 2; in operation then, the
sub-frame section is adjusted via the hydraulic means relative to
the mainframe to provide the desired longitudinal incline. Next,
the lateral incline is adjusted via the adjustable idler arms 26.
Then, the angle of oscillation is adjusted via the pivot arm
adjusting link 18 and the horizontal adjustment of support 27. In
the case of the embodiment of FIGS. 3 and 4 appropriate adjustments
are made via the hydraulic rams 39, 40, 41, 42 and 43. Fluid is
then cycled through the system, the splitters 38 set to divide the
appropriate sizes and the deck box 19 initiated to oscillate.
The mineral is fed to the upper lateral side of the screen. Due to
the oscillation motion of the deck box 19, that is, the angle DBC
of the screen and the angle ABC of the oscillation, the larger and
consequently heavier minerals are found to separate upwards towards
the right hand side of the screen 20 in FIG. 1, whilst the smaller
and lighter particles separate at the left hand side of the screen
20. The longitudinal incline of the deck box 19 including the base
21 and the screen 20 provides process flow and the fractions
separate into the various collecting hoppers.
The upward flow of the fluid tends to lower the relative specific
gravity of the minerals such that the lighter particles e.g.,
"slimes" are washed over the weir 29 and into the channel 30. These
slimes may then be fed through a cyclone to separate out the
heavier particles, before the remainder of the fluid is returned
into tank 31. It has been shown that a considerable economical
saving in minerals may be achieved by this procedure. As mineral
deposited in the hoppers 22 builds up, the fluid flow rate may be
reduced as required. As explained earlier, if the hopper capacity
is insufficient for the larger fractions a bucket elevator may be
used to collect and redirect this fraction onto a conveyor
system.
The third source of mineral fractions collected from the apparatus
is through outlet 24, whereby opening this outlet at the
appropriate intervals, very fine but dense particles that had
fallen through the screen 20 are collected, again achieving mineral
separation. The separated functions of minerals can further be
separated by the apparatus of the present invention into various
shapes of minerals. It has been found that longitudinal or
spherical particles tend to climb up the lateral incline more
readily than tabular particles which tend to gather at the
lowermost portion of the screen 20. By using appropriately designed
screens e.g., larger apertures at the high lateral inclines,
smaller spherical particles may be collected via outlet 24.
Since various changes may be made to the hereinbefore described
apparatus, it is intended that all matter contained in the above
description and as shown in the accompanying drawing shall be
interpreted merely as illustrative and not in a limiting sense.
* * * * *