WO2002028537A1 - Electro-static separation apparatus and method - Google Patents
Electro-static separation apparatus and method Download PDFInfo
- Publication number
- WO2002028537A1 WO2002028537A1 PCT/AU2001/001207 AU0101207W WO0228537A1 WO 2002028537 A1 WO2002028537 A1 WO 2002028537A1 AU 0101207 W AU0101207 W AU 0101207W WO 0228537 A1 WO0228537 A1 WO 0228537A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- electrode
- separation device
- electrostatic separation
- electrostatic
- electrodes
- Prior art date
Links
- 238000000926 separation method Methods 0.000 title claims abstract description 67
- 238000000034 method Methods 0.000 title claims description 10
- 239000000463 material Substances 0.000 claims abstract description 57
- 239000002245 particle Substances 0.000 claims abstract description 16
- 239000011236 particulate material Substances 0.000 claims description 16
- 230000000694 effects Effects 0.000 claims description 5
- 238000005070 sampling Methods 0.000 claims description 5
- 229920002430 Fibre-reinforced plastic Polymers 0.000 claims description 4
- 239000011151 fibre-reinforced plastic Substances 0.000 claims description 4
- 239000011152 fibreglass Substances 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 20
- 239000000377 silicon dioxide Substances 0.000 abstract description 7
- 239000004576 sand Substances 0.000 abstract description 6
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 4
- 239000011707 mineral Substances 0.000 abstract description 4
- 239000000470 constituent Substances 0.000 abstract description 3
- 239000010433 feldspar Substances 0.000 abstract description 3
- 235000019738 Limestone Nutrition 0.000 abstract description 2
- 239000006028 limestone Substances 0.000 abstract description 2
- 239000002184 metal Substances 0.000 description 7
- 229910052751 metal Inorganic materials 0.000 description 7
- 239000004020 conductor Substances 0.000 description 6
- 230000005686 electrostatic field Effects 0.000 description 4
- 239000011810 insulating material Substances 0.000 description 4
- 238000009413 insulation Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 230000003190 augmentative effect Effects 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000000615 nonconductor Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 241000239290 Araneae Species 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000005253 cladding Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
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
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C7/00—Separating solids from solids by electrostatic effect
- B03C7/02—Separators
-
- 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
- B03C7/00—Separating solids from solids by electrostatic effect
- B03C7/006—Charging without electricity supply, e.g. by tribo-electricity or pyroelectricity
-
- 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
- B03C7/00—Separating solids from solids by electrostatic effect
- B03C7/02—Separators
- B03C7/12—Separators with material falling free
Definitions
- the present invention relates to an apparatus and method for electrostatic separation of particulate material, and in particular, the present invention relates to an 'insulated' electrode therefor, which includes an electrically conductive element, having an insulative covering.
- Tribo-static and electrostatic separators are known to be used for the separation of particulate feedstock materials into two or more constituent streams. Such known devices generate a static charge on the feedstock material by tribo-static action, and then pass this material between oppositely charged electrodes, to effect separation.
- a typical application is for beneficiation of minerals such as the removal of silica sand from shell sand or lime stone and the removal of silica sand from feldspar.
- Tribo-static separation itself is not new and is well reported in the literature.
- tribo-static separation occurs when two different substances (for example a granular mineral stream with two or more components) are rubbed together to generate opposing electrostatic charges, and are then subjected to an electric field which polarises the components in opposite directions, hence creating a physical separation.
- Particle types that lend themselves to tribo-static charging tend to be 'non conductors' with differing dielectric constants.
- a granular stream is charged by a transportation device such as a screw conveyor, tumbler, cyclone, impingement mixer etc. which mixes the stream, causing the particles to rub against each other, thus generating electrostatic charge.
- the magnitude of the charge is related to the dielectric constants of the constituent particles. Generally the greater the differential in these constants the greater the charge generated.
- Non conductive particles tend to charge more easily than conductive particles (e.g. metals etc.) as surface resistivity prevents the dissipation of charge.
- tribo-static separations examples include silica from lime, and silica from feldspar. Many valuable minerals can be beneficiated (ie purified) by using tribo-static separation, to remove impurities such as silica and other contaminants.
- the process has wide application and, for example, it can be used for purifying foodstuffs such as removing chaff from grain, shells from nuts etc. or for recycling by separating different types of plastic, or, plastic from metals.
- the electrodes are bare conductors so that a high electrostatic field can be generated.
- feed material attracted to the electrode of opposite polarity to its own charge, on contact with the electrode looses all or some of its opposite charge and may gain the same polarity as the electrode.
- This can be a disadvantage in that material which has lost charge may then be attracted away from the electrode and re-mixed with the general stream, resulting in a lower grade of product. The extent to which this occurs depends on a number of factors but in particular depends on the conductivity of the feed particles.
- the present invention seeks to overcome or at least provide an alternative to the disadvantages of the prior art.
- the present invention seeks to provide a method and apparatus for electrostatic separation of particulate material using 'insulated' electrodes.
- the present invention provides an electrostatic separation device including at least one electrode, wherein each electrode includes an electrically conductive element having an insulative covering.
- each electrically conductive element is embodied in the form of a plate like member.
- said insulative covering is supplied over at least one surface of said plate like member.
- said insulative covering substantially surrounds said electrically conductive element(s).
- said insulative material is additionally thermally insulative material.
- each electrode is adapted to be vibrated or shaken.
- each electrode is adapted to have the voltage/charging thereon removed or reversed in polarity.
- the orientation and/or spacing of said electrodes in said device is selected to optimise the separation effects of the particulate material being processed.
- said orientation and/or spacing of said electrodes in said device is adjustable.
- said electrode(s) are of linear, curved (convergent or divergent) or other shape.
- said electrode(s) include one or a plurality of slots to permit at least some of the particulate material to pass therethrough.
- said insulating covering is fibre reinforced polymer (fibreglass) or other material having similar insulative characteristics thereto.
- said device includes charging means, to apply a charge to the particulate material being processed prior to separation thereof using said electrodes.
- said charging means includes a tribo-static charging means.
- said charging means includes one or a plurality of cascading plates.
- said cascading plates are vibrated / shaken.
- said charging means includes a corona discharge device.
- each chamber having a charging means and an electrode.
- a distributor means to divide a supply of particulate material to be processed between the separation chambers.
- said distributor means includes a primary hopper having a plurality of streams associated therewith, each stream providing particulate material to be processed into one of a plurality of secondary hoppers ready for supply of the particulate material to a respective separation chamber.
- said device further includes a splitter/launder means, to receive the separated particulate material processed from each of said separation chambers and to combine material of similar gradings therefrom (e.g. 'products', 'middlings' and 'rejects').
- a splitter/launder means to receive the separated particulate material processed from each of said separation chambers and to combine material of similar gradings therefrom (e.g. 'products', 'middlings' and 'rejects').
- said splitter/ launder means includes sampling means.
- the present invention provides a method of electrostatically separating particulate feedstock materials, including the steps of: applying a charge to said materials; and passing said materials past at least one charged electrode means, said electrode means having an electrically conductive element having an insulative covering; such that, the materials are separated according to the individual conductivity or charge of the individual feed particles.
- the present invention provides an electrode for an electrostatic separation device, said electrode including an electrically conductive element having an insulative covering.
- said electrically conductive element is embodied in the form of a plate-like configuration.
- said insulative covering is supplied over at least one surface of said plate-like element.
- said insulative covering substantially surrounds said plate-like element.
- said electrically conductive element is embodied in the form of one or more wires or like configuration.
- said insulative covering substantially surrounds said wire(s).
- Figure 1 shows an elevational view of an electrostatic separation apparatus in accordance with the present invention
- Figure 2 illustrates, in Figures 2(a) and 2(b), various embodiments of insulated electrodes which may be used in the apparatus of the present invention
- Figure 3 shows an exploded perspective view of the apparatus of the present invention
- Figure 4 illustrates, in Figures 4(a) to 4(f), various alternative arrangements of the walls of the separating chambers, in accordance with various preferred embodiments of the present invention
- FIG. 5 illustrates, in Figures 5(a) to 5(c), various alternatively preferred embodiments of slotted electrodes which may be used in the apparatus of the present invention.
- FIG. 6 in Fig. 6(a) and Fig. 6(b) side and front views, respectively, shows the configuration of sampling hatches in use with the apparatus of the present invention.
- FIG. 1 An electrostatic separation device, constructed in accordance with the present invention is shown in cross-sectional view in Figure 1, with Figure 3 detailing an exploded perspective view thereof.
- the device generally designated by the numeral 1 includes distributor means 2, for distributing the feedstock, charge applications means 3, separation means 4 and recombining means 5.
- the distributor 2 splits the feed material stream into several smaller streams 6 which are ultimately fed to multiple separating chambers 7.
- Each hopper 8 is used to hold a bed of feed material and supply a respective feeder 9, which dispenses a controlled flow of feed material to a respective separator 4.
- the feeder 9 has a motor driven roll, the speed of which can be controlled.
- Each feeder 9 presents material to a respective tribo- static charging device, such as a cascader 10.
- tribo-static charging devices such as cyclones or screw conveyors can be used.
- Tribo-static generators such as the 'cascade' type, are used to generate electrostatic charge on the feed material.
- the 'cascade' plates can optionally be vibrated in order to increase their effectiveness in generating charge.
- This charge can optionally be augmented using a 'corona discharge' 11, before or after the cascade device.
- Applying a high voltage to a small diameter tungsten wire typically generates the corona discharge.
- Insulated plate electrodes 12, with adjustable plate separation distance and adjustable angle may be used to create electrostatic fields in each separation chamber 7.
- a vibrating device can be attached to the electrode plates, which can be operated intermittently to aid the removal of separated material from the surface of the electrode plates.
- a splitter plate 13 may be used at the outlet of each separating chamber 7 to divide the stream into 'product', 'middling' and 'reject', or other splits.
- a launder 14 may be used to re-combine similar streams, e.g. 'products', 'middlings' and 'rejects'.
- Sampling hatches 16 may be optionally incorporated into the combined outlet streams to allow for product sampling for analysis, such as shown in Fig. 6, Fig. 6(a) illustrating a side view thereof, and Fig. 6(b) illustrating a front view thereof.
- control circuits can be configured to control main process variables such as voltage, roll speed, electrode gap and angle, splitter position, cascade and electrode plate vibrators, voltage interruption and polarity reversal, etc.
- electrodes in tribo-static and other electrostatic devices have been bare metal plates or bars, ie with surface conductivity.
- the tribo-static units have insulated electrodes.
- the electrodes are insulated to the extent that when feed particles contact the electrode they do not lose their charge. Should feed material tend to adhere to the electrode due to electrostatic forces, then the accumulation of material is limited by the action of a mechanical vibrating device or shaker acting on the electrode. The combination of inertial forces and gravitation forces acting on the feed particles are sufficient to overcome the electrostatic and frictional shear forces on feed material in the outer layers of the accumulated bed. If preferred, the polarity of the voltage on the plate can be momentarily reversed or neutralised during the plate cleaning operation.
- One of the advantages of using insulted electrodes, in accordance with the present invention is that, when material makes contact with an uninsulated electrode (attracted by the opposite charge) it loses its charge to the electrode and hence loses the associated electrostatic separating force. Consequently 're-mixing' of separated components can occur due to factors such as turbulence, and the quality of the final separation will be impaired ie the 'product grade' is reduced.
- insulated electrodes When insulated electrodes are used the particles retain their charge when contacting the electrode and hence the quality of separation is high.
- insulated electrodes in accordance with the present invention are that, for good separation, the electrodes have to be charged to a high voltage which constitutes an operating hazard (for example accidental electric shock and arcing or surface tracking between the electrodes and the earthed frame of the machine).
- the insulated electrodes are much safer, and although against recommendations, it is possible to touch the insulated electrode charged to 30 kN or higher without receiving an electric shock.
- the use of insulation on the electrode reduces the tendency of the device to produce arcing between the electrodes.
- FIG. 2(a) is shown an intermediate electrode 17 which would divide two separating chambers. The electrode attracts like material on both sides.
- a boundary electrode 18 which may have increased insulation thickness on its external face.
- these boundary electrodes can have a conductive coating on their external faces or alternatively be laminated with a metallic or conductive material for the purpose of external earthing of the device.
- the insulated electrodes can be constructed using any suitable conductor embedded in a suitable insulating material.
- Typical conductors are plate steel or metal wires or metal mesh, graphite powder or carbon fibre laminated in the composite structure can also be used as a conductor.
- the insulating material can be any of a range of non-conductors including polymers, fibre reinforced polymers, glass, ceramics etc.
- An embedded metal rod or wire is used to connect the embedded electrode to the high voltage source.
- the present invention may be embodied as a multi-chamber device. The embodiment illustrated shows a four-chamber device 1.
- the device 1 is designed with multiple electrode chambers with a spider feed arrangement to distribute to the separate chambers and a multiple channel launder to combine the separated streams into 'product' and reject' streams.
- the combination of these features allows for a high capacity unit, and a high quality of separation ,i.e., high product grades, being obtained.
- the multi-chamber configuration allows for operation of a proportion of capacity, e.g. 25% or 50% or 75% or 100%, thus maintaining a high quality of separation over the full range of throughput ( ie mass flow rate) .
- the device of the present invention is preferably embodied in a modular construction, using a structural insulating material such as fibre reinforced polymer or other, to create a series of separating chambers, such as shown in Figure 3, for example, a series of rectangular 'fibreglass' tubes.
- the walls of the fibreglass tubes have embedded electrodes at appropriate locations which can be charged, as illustrated in Figure 2.
- Such an embodiment provides a fully insulated machine of highly modular construction, which is thermally insulated and of light weight.
- the walls of the separating chambers can be angled either in a convergent or divergent manner, in side elevation or in plan view. Otherwise, the plates and chamber can be inclined to the horizontal thus generating an electrostatic field gradient. In a further embodiment the wall angles can be made adjustable. Examples of particular embodiments are illustrated in Figures 4(a) to 4(f).
- the insulated electrodes are slotted to facilitate the passage of already separated material to a collection duct outside the main separation chamber so that the stream of feed material is progressively reduced.
- the particular features pertaining to this embodiment are illustrated in Figures 5(a) to 5(c).
- the advantage of this embodiment are that, by progressively removing the material already separated from the separating chamber, the remaining material (which is likely to be 'more difficult to separate') can be acted on by the combination of forces as described above without interference from material already separated and removed. Hence the outcome is an improved final separation.
- the electrostatic separator device of the present invention therefore utilises a 'plate cascade' over which the feed material is passed to effect tribo-static charging.
- the cascade plates may be vibrated either horizontally, vertically or in-plane in order to enhance friction between particles.
- the tribo-static charge can be augmented by utilising a 'corona discharge' device close to the cascade outlet and prior to the electrostatic field.
- the device uses insulated electrodes, consisting of conducting electrode material embedded in a non-conductive structural material.
- the conductive material can be selectively placed in order to give optimum separating effects on the material stream being processed.
- the 'insulated electrodes' can therefore be used to form the structure of the separator thereby combining the electrode with the machine enclosure, thus consolidating two essential components into one.
- the electrode insulating material can additionally be thermally insulating thus reducing heat losses from the device and reducing or eliminating the need for separate thermal insulation.
- the electrodes can be fitted with a shaking or vibrating device to assist in the removal of material adhering to the surface of the electrodes due to electrostatic forces. The voltage on the electrode can be temporarily removed or reversed in polarity in assist in particle removal.
- the insulated electrodes may be selectively orientated so as to create modular separation compartments in which electrodes can be sequentially of alternating polarity so that a modular separator can be effected which may be used for treating incremental flow rates of material.
- the insulating electrodes may be orientated at selective angles, e.g. convergent or divergent, in side elevation, or in plan, as shown in Figure 4.
- the device may also be configured, so that the plate angles are adjustable.
- the insulated electrodes may incorporate a series of slots to allow the separated material to pass through to a collection channel outside the main separating chamber. In this manner, the feed material is incrementally separated and collected so that the stream of feed material progressively reduces through the separating chamber from inlet to outlet.
- the present invention provides a device using insulated electrodes so that particles retain their charge on contact and incorporating a reciprocating action vibration generator to aid removal of material from the electrodes.
- a modular device with single or multiple separation chambers wherein the walls of the device may be made from the same material as the electrodes themselves.
Landscapes
- Electrostatic Separation (AREA)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2001291496A AU2001291496A1 (en) | 2000-10-05 | 2001-09-27 | Electro-static separation apparatus and method |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AUPR0576A AUPR057600A0 (en) | 2000-10-05 | 2000-10-05 | Electrostatic separation apparatus and method |
AUPR0576 | 2000-10-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2002028537A1 true WO2002028537A1 (en) | 2002-04-11 |
Family
ID=3824634
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/AU2001/001207 WO2002028537A1 (en) | 2000-10-05 | 2001-09-27 | Electro-static separation apparatus and method |
Country Status (2)
Country | Link |
---|---|
AU (1) | AUPR057600A0 (3Den) |
WO (1) | WO2002028537A1 (3Den) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2273525C1 (ru) * | 2004-11-18 | 2006-04-10 | Евгений Яковлевич Федоров | Электростатический сепаратор для отделения частиц твердых материалов, различающихся по их удельному весу |
WO2008067589A1 (en) * | 2006-12-04 | 2008-06-12 | The University Of Queensland | A particle sorting apparatus and method |
US8083165B2 (en) | 2005-05-20 | 2011-12-27 | Omya Gmbh | Method and device for manufacturing dispersed mineral products |
CN103537378A (zh) * | 2013-11-06 | 2014-01-29 | 宁夏新航能源环境科技有限公司 | 一种节能型分离装置 |
CN108480054A (zh) * | 2018-02-10 | 2018-09-04 | 中国矿业大学 | 一种壁面摩擦材料旋转可调的粉体电选环保收集装置 |
CN112547311A (zh) * | 2020-12-15 | 2021-03-26 | 无锡宝德金装备科技有限公司 | 硅片切割废渣电荷分离器 |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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SU1297912A2 (ru) * | 1985-07-23 | 1987-03-23 | Kovalev Sergej | Устройство дл сепарации влажного зерна |
SU1375181A1 (ru) * | 1985-07-22 | 1988-02-23 | Дагестанский Сельскохозяйственный Институт | Устройство дл разделени сем н по длине |
SU1553180A1 (ru) * | 1988-06-27 | 1990-03-30 | Московский институт инженеров сельскохозяйственного производства им.В.П.Горячкина | Диэлектрический сепаратор |
RU2098193C1 (ru) * | 1995-07-26 | 1997-12-10 | Челябинский государственный технический университет | Установка для извлечения веществ и частиц из суспензий и растворов |
WO1998028080A1 (de) * | 1996-12-23 | 1998-07-02 | Hamos Gmbh Recycling- Und Separationstechnik | Vorrichtung zum elektrostatischen sortieren von gemischen aus teilchen unterschiedlicher kunststoffe |
-
2000
- 2000-10-05 AU AUPR0576A patent/AUPR057600A0/en not_active Abandoned
-
2001
- 2001-09-27 WO PCT/AU2001/001207 patent/WO2002028537A1/en active Application Filing
Patent Citations (5)
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SU1375181A1 (ru) * | 1985-07-22 | 1988-02-23 | Дагестанский Сельскохозяйственный Институт | Устройство дл разделени сем н по длине |
SU1297912A2 (ru) * | 1985-07-23 | 1987-03-23 | Kovalev Sergej | Устройство дл сепарации влажного зерна |
SU1553180A1 (ru) * | 1988-06-27 | 1990-03-30 | Московский институт инженеров сельскохозяйственного производства им.В.П.Горячкина | Диэлектрический сепаратор |
RU2098193C1 (ru) * | 1995-07-26 | 1997-12-10 | Челябинский государственный технический университет | Установка для извлечения веществ и частиц из суспензий и растворов |
WO1998028080A1 (de) * | 1996-12-23 | 1998-07-02 | Hamos Gmbh Recycling- Und Separationstechnik | Vorrichtung zum elektrostatischen sortieren von gemischen aus teilchen unterschiedlicher kunststoffe |
Non-Patent Citations (4)
Title |
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DATABASE WPI Derwent World Patents Index; Class J01, AN 1998-360901/31 * |
DATABASE WPI Derwent World Patents Index; Class P12, AN 1988-248663/35 * |
DATABASE WPI Derwent World Patents Index; Class P41, AN 1987-297180/42 * |
DATABASE WPI Derwent World Patents Index; Class P41, AN 1991-056467/08 * |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2273525C1 (ru) * | 2004-11-18 | 2006-04-10 | Евгений Яковлевич Федоров | Электростатический сепаратор для отделения частиц твердых материалов, различающихся по их удельному весу |
US8083165B2 (en) | 2005-05-20 | 2011-12-27 | Omya Gmbh | Method and device for manufacturing dispersed mineral products |
US8177150B2 (en) | 2005-05-20 | 2012-05-15 | Omya Gmbh | Method and device for manufacturing dispersed mineral products |
WO2008067589A1 (en) * | 2006-12-04 | 2008-06-12 | The University Of Queensland | A particle sorting apparatus and method |
CN103537378A (zh) * | 2013-11-06 | 2014-01-29 | 宁夏新航能源环境科技有限公司 | 一种节能型分离装置 |
CN108480054A (zh) * | 2018-02-10 | 2018-09-04 | 中国矿业大学 | 一种壁面摩擦材料旋转可调的粉体电选环保收集装置 |
CN108480054B (zh) * | 2018-02-10 | 2019-12-03 | 中国矿业大学 | 一种壁面摩擦材料旋转可调的粉体电选环保收集装置 |
CN112547311A (zh) * | 2020-12-15 | 2021-03-26 | 无锡宝德金装备科技有限公司 | 硅片切割废渣电荷分离器 |
Also Published As
Publication number | Publication date |
---|---|
AUPR057600A0 (en) | 2000-10-26 |
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