GB2265322A - Sorting particles - Google Patents
Sorting particles Download PDFInfo
- Publication number
- GB2265322A GB2265322A GB9306342A GB9306342A GB2265322A GB 2265322 A GB2265322 A GB 2265322A GB 9306342 A GB9306342 A GB 9306342A GB 9306342 A GB9306342 A GB 9306342A GB 2265322 A GB2265322 A GB 2265322A
- Authority
- GB
- United Kingdom
- Prior art keywords
- particles
- mass
- sorting
- magnetic
- oil
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/02—Froth-flotation processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B1/00—Conditioning for facilitating separation by altering physical properties of the matter to be treated
- B03B1/04—Conditioning for facilitating separation by altering physical properties of the matter to be treated by additives
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/32—Magnetic separation acting on the medium containing the substance being separated, e.g. magneto-gravimetric-, magnetohydrostatic-, or magnetohydrodynamic separation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/08—Subsequent treatment of concentrated product
- B03D1/082—Subsequent treatment of concentrated product of the froth product, e.g. washing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/24—Pneumatic
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/08—Subsequent treatment of concentrated product
- B03D1/087—Subsequent treatment of concentrated product of the sediment, e.g. regrinding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/1443—Feed or discharge mechanisms for flotation tanks
- B03D1/1462—Discharge mechanisms for the froth
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/1443—Feed or discharge mechanisms for flotation tanks
- B03D1/1468—Discharge mechanisms for the sediments
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/1443—Feed or discharge mechanisms for flotation tanks
- B03D1/1475—Flotation tanks having means for discharging the pulp, e.g. as a bleed stream
Landscapes
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biotechnology (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Glanulating (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
- Compounds Of Iron (AREA)
- Combined Means For Separation Of Solids (AREA)
Abstract
In a method of sorting a particulate mass, eg. diamonds and gangue, according to the oleophilicity of the particles of the mass, the particles (24, 26) of the mass are treated with an oil-containing substance (22) in such a manner that oleophilic particles (24), eg. the diamonds, of the mass are at least partially coated with the substance (22). Next, the particles (24, 26) are exposed to a material (12) having specific properties so that the material adheres to the coated particles (24). Finally, the particles (24, 26) can be sorted according to whether they exhibit the specific properties. The material may comprise an aqueous magnetite suspension and/or air bubbles, so that the particles can be sorted using magnetic separation and/or flotation. <IMAGE>
Description
SORTING PROCESS AND APPARATUS
THIS invention relates to a sorting process and apparatus. In particular, the invention relates to a process and apparatus for sorting particles according to their oleophilicity.
In one application of the invention, it may be used to sort diamond
particles, which have oleophilic properties, from non-diamond or gangue
particles which are not oleophilic, in a diamond bearing gravel.
Grease tables have already been used to separate diamond particles
from gangue particles. These utilised a continuous layer of grease to
which diamond particles would stick by virtue of the contact angles
A first aspect of the invention provides a method of sorting a particulate mass according to the oleophilicity of the particles of the mass, the method comprising the steps of treating the particles of the mass with an oil-containing substance in such a manner that oleophilic particles of the mass are at least partially coated with the substance, causing a material having specific properties to become associated with the coated particles, and sorting the particles according to whether they exhibit the specific properties.
In one version of the invention, the material having specific properties is a material having magnetic properties and the particles are sorted in a magnetic separator. The particles may, for instance, be treated by causing them to pass through a body of a molten oil-containing substance. Preferably, this version of the invention includes the following steps: - treating the particles of the mass with a molten, oil-containing
substance so that oleophilic particles are at least partially coated
with the substance; - exposing the particles to a particulate, magnetic material so that
magnetic particles adhere to the coatings of the coated particles,
and - sorting the particles into magnetic and non-magnetic fractions in
a magnetic separator.
The method may include the further step, after exposure of the particles to the magnetic material and prior to sorting, of subjecting the particles to a low temperature to congeal the coatings of the coated particles and adhere the magnetic particles firmly thereto.
In another version of the invention, the material which is caused to adhere to the coated particles is a gas, typically air. This version of the invention preferably includes the following steps: - the particles are introduced into the upper end of a body of
liquid and are allowed to settle in the body of liquid, - a molten oil-containing substance in droplet form and air bubbles
are caused to rise in the body of liquid in opposition to the
settling particles, - oleophilic particles are allowed to acquire an at least partial
coating of the oil-containing substance, - air bubbles are allowed to adhere to the coatings of the coated
particles, thereby to increase the buoyancy of those particles, and - the particles are sorted according to their buoyancy.
Either version of the invention can be used to sort diamonds from other particles.
A second aspect of the invention provides an apparatus for sorting a particulate mass according to the oleophilicity of the particles of the mass, the apparatus comprising: - means for treating the particles of the particulate mass with an
oil-containing substance so that oleophilic particles acquire an at
least partial coating of the oil-containing substance, - means thereafter for causing the treated particles to contact a
material having specific properties, and - means for sorting the particles according to whether or not they
exhibit the specific properties.
BRIEF DESCRIPTION OF THE DRAWINGS
The invention will now be described in more detail, by way of example only, with reference to the accompanying drawings in which Figures 1 and 2 diagrammatically illustrate two embodiments of the invention.
DESCRIPTION OF EMBODIMENTS
The illustrated embodiments can be used to sort diamond particles from gangue particles in a diamond-bearing gravel, the gravel typically being one recovered from diamond mining activities.
Figure 1 shows a vessel 10 containing, in a central region thereof, an aqueous magnetite suspension 12 which is recycled in a closed circuit 14 by means of a pump 16. A volume 18 of clear water lies above the suspension 12 and a further volume 20 of clear water lies beneath the suspension.
Floating on the upper surface of the upper volume 18 of water is a layer 22 of molten petroleum jelly. The molten state of the layer 22 is maintained by a suitable heating coil or the like (not shown). The numeral 24 indicates a feed stream of wet gravel which has been preheated to a temperature, in this case of around 80"C, but in any case higher than the congealing point of the petroleum jelly in the layer 22.
The feed stream sinks through the layer 22 and oleophilic particles in the feed stream, primarily diamond particles, acquire an at least partial coating of molten jelly during their passage through that layer.
Having sunk through the layer 22, the particles gravitate through the suspension 12. Magnetite particles become embedded in the jelly coatings of the relevant particles, i.e. the oleophilic particles 24. There is no such embedment in the essentially non-oleophilic, uncoated particles 26.
Having gravitated through the suspension 12, the particles enter the lower volume 20 of water, which is cooled by any appropriate means to a temperature below the congealing point of the petroleum jelly. During their gravitational passage through the lower volume of water, the jelly coatings congeal to adhere the embedded particles securely to the oleophilic particles 24.
From the lower end of the vessel 10, the particles 24 and 26 are transferred to a magnetic separator, indicated generally with the numeral 28. The magnetic separator, which may be of conventional type, separates the particles into a magnetic fraction, composed of particles 24 and a non-magnetic fraction composed of particles 26. It will be appreciated that the process can operate substantially continuously with magnetic, i.e. primarily diamond particles, reporting in the magnetic fraction and non-magnetic, i.e. gangue particles, reporting in the nonmagnetic fraction.
It will also be appreciated that passage of the particles through the suspension 12 and subsequent water volume will wash any weakly adheringjelly from the non-oleophilic particles. Although petroleum jelly has been specifically mentioned, it will also be appreciated that many other oil-containing substances could also be used to provide the required coating on the oleophilic particles. Heating of the layer 22 may or may not be required, depending on the prevailing ambient temperature, to ensure that the layer exists in liquid form. Similarly, cooling of the water volume may or may not be required, depending on the ambient temperature and choice of substance used in the layer 22.
It will furthermore be understood that the particles may initially be preheated to avoid premature congealing of the jelly in the layer 22 before the particles reach the suspension 12.
In the example described above, the particles are treated with an oilcontaining substance, i.e. the jelly, so that the oleophilic particles, i.e. the diamonds, are at least partially coated with that substance. A material having specific properties, in this case a magnetic material in the form of magnetite, is then caused to adhere to the coated particles. Particle sorting can then take place on the basis of whether or not the particles exhibit magnetic properties.
Figure 2 illustrates a second embodiment of the invention. In this case, there is a vessel 100 containing liquid 102 in the form of water or an aqueous suspension. Fine particles are introduced into the liquid 102 through a feeder 104. Molten grease or another oil-containing substance is injected into the lower end of the vessel 100 through nozzles 106. The grease rises in the liquid 102 in droplet form in counter-current flow to the particles as the particles settle in the liquid.
Collision of the grease droplets with the settling particles causes the oleophilic particles 103, i.e. diamonds, to acquire an at least partial coating of grease, while non-oleophilic particles 105 are not so coated.
The grease which rises to the surface of the liquid 102 can be withdrawn by suitable means and then recirculated through a circuit 108 containing a heater 110 that maintains the grease temperature high enough for it to remain the required molten state.
Located adjacent the nozzles 106 is an air sparging head 112 through which air is injected into the vessel 100 simultaneously with injection of the grease. Thus air bubbles 113 rise through the liquid 102 along with the grease droplets. The air bubbles become attached to the greasecoated particles and increase the buoyancy of those particles.
The smaller particles become sufficiently buoyant to float to the top of the vessel where they can be removed as a diamond rich fraction.
Heavier particles may not acquire sufficient buoyancy to float to the top of the vessel, and these particles continue to settle through the liquid 102 onto a conveyor belt 114 which takes them to a dedicated flotation cell where the more buoyant diamond particles are separated from the other particles.
In this example of the invention, therefore, air is caused to adhere to the coated particles to give those particles the specific property of increased buoyancy.
In a refinement of the Figure 2 technique, it would be possible to inject fine magnetite particles along with the air or grease. In this case, the coated particles acquire both increased buoyancy as a result of air bubble adherence and magnetic properties as a result of adherence of the magnetite. Both flotation and magnetic separation techniques can then be used to separate the diamond particles from the other particles.
In the last-mentioned version it may prove necessary to precondition the particle feed to remove lightly magnetic particles.
In each of the embodiments discussed above the particles are preconditioned if necessary to expose the surfaces of the diamond particles. This may, for instance, be done by attritioning the particles in an abrasive suspension such as a suspension of ferrosilicon.
Claims (12)
1.
A method of sorting a particulate mass according to the oleophilicity of the particles of the mass, the method comprising the steps of treating the particles of the mass with an oil-containing substance in such a manner that oleophilic particles of the mass are at least partially coated with the substance, causing a material having specific properties to become associated with the coated particles, and sorting the particles according to whether they exhibit the specific properties.
2.
A method according to claim 1 wherein the material having specific properties is a material having magnetic properties and the particles are sorted in a magnetic separator.
3.
A method according to claim 1 or 2 wherein the particles are treated by causing them to pass through a body of a molten oil-containing substance.
4.
A method according to claim 1 which includes the following steps: - treating the particles of the mass with a molten, oil-containing
substance so that oleophilic particles are at least partially coated
with the substance; - exposing the particles to a particulate, magnetic material so that
magnetic particles adhere to the coatings of the coated particles,
and - sorting the particles into magnetic and non-magnetic fractions in
a magnetic separator.
5.
A method according to claim 4 wherein, after exposure to the magnetic material and prior to sorting, the particles are subjected to a low temperature to congeal the coatings of the coated particles and adhere the magnetic particles firmly thereto.
6.
A method according to claim 1 wherein the material which is
caused to become associated with the coated particles is a
gas which is caused to adhere to the coated particles.
7.
A method according to claim 6 wherein the gas is air.
8.
A method according to claim 6 or claim 7 wherein: - the particles are introduced into the upper end of a body of
liquid and are allowed to settle in the body of liquid, - a molten oil-containing substance in droplet form and air bubbles
are caused to rise in the body of liquid in opposition to the
settling particles, - oleophilic particles are allowed to acquire an at least partial
coating of the oil-containing substance, - air bubbles are allowed to adhere to the coatings of the coated
particles, thereby to increase the buoyancy of those particles, and - the particles are sorted according to their buoyancy.
9.
A method according to any one of the preceding claims when used to sort diamonds from other particles.
10.
An apparatus for sorting a particulate mass according to the oleophilicity of the particles of the mass, the apparatus comprising: means for treating the particles of the particulate mass with an
oil-containing substance so that oleophilic particles acquire an at
least partial coating of the oil-containing substance, - means thereafter for causing the treated particles to contact a
material having specific properties, and - means for sorting the particles according to whether or not they
exhibit the specific properties.
11.
A method of sorting a particulate mass according to the oleophilicity of the particles of the mass substantially as herein described with reference to Figure 1 or Figure 2 of the accompanying drawings.
12.
An apparatus for sorting a particulate mass according to the oleophilicity of the particles of the mass substantially as herein described with reference to Figure 1 or Figure 2 of the accompanying drawings.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ZA922206 | 1992-03-26 |
Publications (2)
Publication Number | Publication Date |
---|---|
GB9306342D0 GB9306342D0 (en) | 1993-05-19 |
GB2265322A true GB2265322A (en) | 1993-09-29 |
Family
ID=25581536
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB9306342A Withdrawn GB2265322A (en) | 1992-03-26 | 1993-03-26 | Sorting particles |
Country Status (5)
Country | Link |
---|---|
AU (1) | AU3553293A (en) |
BR (1) | BR9301333A (en) |
CA (1) | CA2092502A1 (en) |
GB (1) | GB2265322A (en) |
ZA (1) | ZA932166B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997023293A1 (en) * | 1995-12-21 | 1997-07-03 | University Of Southampton | Magnetic separation in a magnetic fluid |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB970841A (en) * | 1962-07-14 | 1964-09-23 | Pierre Boutin | Method and apparatus for the froth flotation of ores |
WO1982000602A1 (en) * | 1980-08-25 | 1982-03-04 | American Clays Corp Anglo | Magnetic beneficiation of clays utilizing magnetic seeding and flotation |
GB2102301A (en) * | 1981-07-23 | 1983-02-02 | Norman Clark | Solids extraction process |
WO1984004701A1 (en) * | 1983-05-21 | 1984-12-06 | British Petroleum Co Plc | Beneficiation of carbonaceous fuels |
GB2143155A (en) * | 1983-06-27 | 1985-02-06 | Conoco Inc | A method of separating fine coal particles from refuse |
GB2258829A (en) * | 1991-08-20 | 1993-02-24 | De Beers Ind Diamond | Froth separation of particles |
-
1993
- 1993-03-25 CA CA002092502A patent/CA2092502A1/en not_active Abandoned
- 1993-03-26 AU AU35532/93A patent/AU3553293A/en not_active Abandoned
- 1993-03-26 GB GB9306342A patent/GB2265322A/en not_active Withdrawn
- 1993-03-26 ZA ZA932166A patent/ZA932166B/en unknown
- 1993-03-26 BR BR9301333A patent/BR9301333A/en not_active Application Discontinuation
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB970841A (en) * | 1962-07-14 | 1964-09-23 | Pierre Boutin | Method and apparatus for the froth flotation of ores |
WO1982000602A1 (en) * | 1980-08-25 | 1982-03-04 | American Clays Corp Anglo | Magnetic beneficiation of clays utilizing magnetic seeding and flotation |
GB2102301A (en) * | 1981-07-23 | 1983-02-02 | Norman Clark | Solids extraction process |
WO1984004701A1 (en) * | 1983-05-21 | 1984-12-06 | British Petroleum Co Plc | Beneficiation of carbonaceous fuels |
GB2143155A (en) * | 1983-06-27 | 1985-02-06 | Conoco Inc | A method of separating fine coal particles from refuse |
GB2258829A (en) * | 1991-08-20 | 1993-02-24 | De Beers Ind Diamond | Froth separation of particles |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997023293A1 (en) * | 1995-12-21 | 1997-07-03 | University Of Southampton | Magnetic separation in a magnetic fluid |
Also Published As
Publication number | Publication date |
---|---|
BR9301333A (en) | 1993-09-28 |
AU3553293A (en) | 1993-09-30 |
ZA932166B (en) | 1993-10-28 |
CA2092502A1 (en) | 1993-09-27 |
GB9306342D0 (en) | 1993-05-19 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
WAP | Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1) |