[0001] The present invention generally relates to dry separation of particles, and in particular
to a method and a device for separating at least one particulate, electrically conductive,
non-magnetic material included as a constituent or as constituents in a mixture.
[0002] In recent years, the recovery of valuable materials, especially metals or metal alloys,
such as brass, copper, lead and aluminium, has become a major concern, primarily for
reasons of economy and environmental control. One example of a field where such recovery
has been constantly extended is that of data scrap. The reason for an intensive activity
in this particular field is of course the growing insight into the economic values,
especially of the metals which are recoverable from such scrap. The invention is applicable
particularly to the data scrap field, but is not restricted thereto.
[0003] Today's separation techniques rely on some property of the different materials to
be separated. Various devices are known in the art for separating magnetic materials
from non-magnetic ones, where magnetism is utilised, e.g. for "sucking" up the magnetic
material. There are also devices which rely on a difference in friction coefficient
or density, and in which a mechanical motion, such as vibration and rotation, affects
the mixture to be separated, thus producing a certain degree of separation.
[0004] Another technique for separating non-magnetic materials is disclosed in US-A-4,313,543,
and involves a device for separating electrically conductive particles of varying
sizes from particles which are not electrically conductive. A stream of particles
is applied to the upper part of a sloped surface, and juxtaposed, oppositely directed
magnetic fields of varying width are established adjacent the particle stream. When
the particles pass through the magnetic fields located underneath the particles, forces
are developed which act on the electrically conductive particles and so, these particles
are deflected from the stream so as to bring about particle separation.
[0005] EP-0,307,250 A2 describes a method for separating a mixture of flat metal alloy particles.
This separation method relies on differences in particle size and differences in electrical
conductivity or density. This publication states, by way of example, the use of a
vibrating separator table together with a rapidly alternating magnetic field which
in electrically conductive particles applied to the table induces eddy currents causing
the particles to be deflected to a varying extent. The magnetic field is provided
underneath the particles (cf. Fig. 3).
[0006] The prior-art separation techniques described above provide a degree of separation
which is insufficient in many applications, and suffer from a number of drawbacks.
The major drawback, especially reflected in the above-mentioned European patent publication
where the magnetic field is located below the particles, is that the greatest magnetic
force (magnetic flux density) is on the underside of the particles, this bringing
about a rotational direction of the electrically conductive particles that is oppositely
directed to the desired transport direction or direction of separation, which adversely
affects the separation.
[0007] The present invention overcomes the drawbacks of prior-art separation techniques,
and one object thereof is to provide such a high degree of separation that the separated
products, without further processing or purification, can be used as raw materials
in refining processes with high demands on the purity of the raw materials.
[0008] By subjecting, in accordance with the invention, the electrically conductive, non-magnetic
particles to a rotating, alternating magnetic field inducing electric eddy currents
in the particles while these are being repeatedly thrown up into the field in a direction
opposite to the direction of rotation of the magnets generating the magnetic field,
at a throwing angle α relative to the horizontal plane, where 0 < α < 90°, and by
arranging the rotary means above the particles, a very high degree of separation of
about 98% or more is achieved.
[0009] The invention thus relates to a method and a device for separating at least one particulate,
electrically conductive, non-magnetic material included as a constituent or as constituents
in a mixture, as recited in the preambles of the respective independent claims, the
method and the device having the features appearing from the characterising clauses
of the respective independent claims.
[0010] Preferred embodiments of the device for carrying out the method according to the
invention will be described in more detail hereinbelow with reference to the accompanying
drawings, in which
Fig. 1 is a schematic front view, with certain parts broken away, of a preferred embodiment
of the device,
Fig. 2 is a view similar to Fig. 1, illustrating another preferred embodiment of the
device,
Fig. 3 shows a separation means forming part of the device, and
Figs 4A-4C are diagrams further elucidating the invention.
[0011] Referring now to the drawings, the device shown in Fig. 1 has a feeding unit 1 including
a rotary disc 1a for supplying particles to a separation means 2 having a cover 3
and a bottom 4. The cover 3 has a central opening in which the feeding unit 1 opens.
Thus, the separation means is closed, with the exception of the central opening and
slots provided at the periphery of the separation means. The separation means 2 is
sloping downwards, counting from the centre, which implies a movement of the particles
towards the periphery of the separation means. Further, the device includes a means
5 for generating a magnetic field. In the embodiment shown in Fig. 1, the means 5
has an upper hood 6, whose inside is equipped with a plurality of magnets (not shown).
The separation means 2 is disposed underneath the means 5. The hood 6 is rotated by
means of a motor 8 (via a transmission 9). The separation means 2 is of plastic, its
cover and bottom having a thickness of about 2-5 mm. Thus, the magnetic field will
penetrate the separating means 2, thus affecting the particles present therein. An
apparatus 11 is adapted to throw up the particles into the magnetic field. The throwing
apparatus 11, illustrated only schematically, is of conventional type and comprises,
according to a preferred embodiment, a box-like structure whose top face forms the
bottom 4 of the separation means 2. The box-like structure, being suspended on leaf
springs, is set in motion, more specifically in a combined rotary/throwing motion
(restrained by the leaf springs) which can be defined as a helical motion, such that
the particles are repeatedly thrown up into the magnetic field, i.e. each particle
impinges on the bottom several times. This motion can be achieved by means of a piston
and cylinder assembly, an eccentric mechanism or the like. The throwing apparatus
11 is so designed that the particles are thrown up into the magnetic field in a direction
opposite to the direction of rotation of the hood 6. The throwing height and the throwing
angle are dependent on the particle material, particle type and particle size. Generally,
however, the throwing height varies from a few millimetres to several centimetres,
and the throwing angle relative to the horizontal plane is greater than zero and less
than 90°.
[0012] Fig. 2 illustrates another preferred embodiment in which two magnetic fields are
provided, namely a first (represented by the hood 6 internally equipped with magnets)
which is disposed above the separation means 2, and a second (represented by the hood
7 internally equipped with magnets) which is disposed below the separation means 2.
The hood 7 is driven by a motor 8 (via a transmission 9), the hood 6 being entrained
in the rotary movement as a result of the magnetic coupling between the hoods. This
embodiment is best suited for separating particles of a relatively small particle
size, e.g. 1-2 mm, whereas the embodiment in Fig. 1 is best suited for separating
particles of a larger particle size, e.g. 2-10 mm. The purpose of arranging a lower
magnetic field combined with the upper one merely is to intensify the magnetic field.
[0013] Fig. 3 illustrates the separation means 2 in more detail. The cover 3 (broken apart
in Fig. 3) and the bottom 4 are interconnected by radial webs 12 dividing the separation
means into sections 13. Deflecting members in the form of flanges 14 vertically projecting
from the bottom extend partially along imaginary centre radii in each section 13.
In the embodiment shown in Fig. 3, each section 13 is divided into two chambers 15,
16. Along the periphery of the separation means 2 there are provided collecting means
(not shown) in the form of pockets, one for each chamber, from which tubes extend,
opening into two large-size containers, namely one container for the tubes coming
from the chambers 15 of the sections 13, and another for the tubes coming from the
chambers 16 of the sections 13. According to other embodiments of the inventive device,
each section may of course be divided into more than two chambers. Similarly, an optional
number of tubes can be arranged which open into an optional number of large-size containers.
[0014] By providing, in accordance with the invention, a magnetic field above the particles,
as in the embodiment shown in Fig. 1, the force acting on each particle because of
the magnetic field becomes greater on the upper side of the particle than on the underside
as a result of the magnetic field density distribution in the space concerned, which
in turn means that to each particle in the field is imparted a rotary movement coinciding
with the desired direction of movement of the particle (transport direction). This
is illustrated in Fig. 4A. Should, however, the magnetic field be arranged only below
the particles (cf. European Patent Publication 307,250 mentioned above), the particles
would have a direction of movement opposite to the transport direction. This is illustrated
more specifically in Fig. 4B. It should be noted that when both an upper and a lower
magnetic field are provided, the purpose of the lower one merely is to intensify the
magnetic field.
[0015] Fig. 4C shows how individual particles behave in the magnetic field. At the top of
Fig. 4C there are schematically shown magnets which are rotated in order to induce
eddy currents in the electrically conductive particles, the direction of rotation
being indicated by the arrow A. Below the magnets there is an air gap and under it
a plastic element forming the cover of the separation space provided thereunder and
further defined by the bottom. When a weakly or non-electrically conductive particle
is thrown up into the magnetic field by means of the apparatus 11 producing the throwing
motion (not shown in this Figure), this particle will follow the trajectory illustrated
to the left in the Figure. On the other hand, an electrically conductive particle
(to the right in Fig. 4C) will, according to the discussion with respect to Fig. 4A,
move under acceleration in the direction of separation as a result of the rotary movement.
Each single particle will be repeatedly thrown up into the magnetic field while being
set in a rotary motion whose main component force cooperates with the magnetic force
acting on the particle. This cooperation produces an additive effect, improving the
degree of separation.
[0016] The operation of the device will now be described in more detail with reference to
a practical embodiment. A mixture of electrically conductive, non-magnetic particles
of two different materials, in this case copper and lead, is supplied to the device
through the feeding unit 1. By means of the disc 1a, the feeding unit randomly distributes
the particles into the different sections 13 of the separation means 2. The slope
of the separation means 2 implicates a displacement of the particles towards the periphery
thereof. As a result of the particles being thrown up into the magnetic field in a
direction opposite to the direction of rotation of the magnets, along with the fact
that the particles are given a positive rotary motion (see Fig. 4A) coinciding with
the desired direction of separation, improved separation is achieved. By correctly
selecting the frequencies/velocities for the motions of the throwing apparatus 11
and for the rotation of the hood 6 or hoods 6, 7, respectively, good separation of
the constituents of the mixture is achieved, each constituent being collected separately
at each side of each section, and when the particles in each section 13 during their
displacement towards the periphery of the separation means pass the inner edge of
the flange 14, the degree of separation is almost 100%. The final products are collected
in the collecting pockets described above and passed on to the containers.
[0017] It has been found that a suitable size of the particles included in the mixture is
1-10 mm, preferably 1-8 mm. To achieve a degree of separation of about 98-99.5%, it
has been found advantageous according to a preferred embodiment to rotate the hood
6, 7 at a speed of 20-50 m/sec. There is a certain relationship between the speed
of rotation and the particle size. Generally, small particles require rotational speeds
in the upper region of the range, whereas larger particles require rotational speeds
in the lower region of the range. Optimal ratios are obtainable by simple tests.
[0018] The shape of the particles is not critical in the invention. However, it is preferred
to use substantially granular particles, which means particles of a shape varying
from spherical to polygonal.
[0019] According to the invention, it is convenient to separate particles which are affected
differently by the magnetic field, substantially as a consequence of a difference
in resistivity. Non-restricting examples of mixtures which have been successfully
separated according to the invention are mixtures containing at least one of the following
constituents: copper, lead, glass, plastic, cellulose etc. A condition for a successful
separation according to the invention is that the mixture contains at least one electrically
conductive, non-magnetic material.
[0020] Although a preferred embodiment of the invention has been described above, it is
obvious to those skilled in the art that different modifications are conceivable within
the scope of the invention.
1. Method for separating at least one particulate, electrically conductive, non-magnetic
material which is included as a constituent or as constituents in a mixture, the separation
being performed in a space which is permeable to magnetic waves, and the mixture present
in said space being subjected to an alternating magnetic field generated by a rotating
means equipped with magnets, characterised by throwing the particles up from the bottom of said space in a direction opposite
to the direction of rotation of said means generating the magnetic field, and corresponding
to a throwing angle α relative to the horizontal plane, 0 < α < 90°, and arranging
said means over said space.
2. Method as claimed in claim 1, characterised in that the magnetic field is generated by means arranged both above and below said
space.
3. Method as claimed in claim 1 or 2, characterised in that said space is closed.
4. Device for separating at least one electrically conductive, non-magnetic material
which is included as a constituent or as constituents in a mixture, comprising a separation
space (2, 3, 4) permeable to magnetic waves, means (5) for generating an alternating
magnetic field, and feeding and discharging means, characterised in that the means (5) is a rotating means equipped with magnets, and that a throwing
apparatus (11) is provided for throwing up the particles in said space in a direction
opposite to the direction of rotation of said means (5), which is disposed above said
space.
5. Device as claimed in claim 4, characterised in that additional means for generating an alternating magnetic field is disposed
below said space.
6. Device as claimed in claim 4 or 5, characterised in that the bottom (4) of the separation space is formed by the top face of the throwing
apparatus (11).
7. Device as claimed in any one of claims 4-6, characterised in that the separation means (2) is divided into sections by means of webs (12) extending
from its centre radially outwards towards its periphery, and that deflecting elements
in the form of flanges (14) extend partially along imaginary centre radii in each
section (13) for dividing each section (13) into at least two chambers (15, 16).
8. Device as claimed in claim 7, characterised in that the discharging means is connected to the periphery of the separation means
(2) for discharging the separated material from the respective chamber (15, 16).