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CN104941812A - Micro-fine particle material friction electric separation method and device adopting lateral negative pressure adsorption - Google Patents

Micro-fine particle material friction electric separation method and device adopting lateral negative pressure adsorption Download PDF

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CN104941812A
CN104941812A CN201510423931.7A CN201510423931A CN104941812A CN 104941812 A CN104941812 A CN 104941812A CN 201510423931 A CN201510423931 A CN 201510423931A CN 104941812 A CN104941812 A CN 104941812A
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electrostatic field
voltage electrostatic
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negative pressure
pressure chamber
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CN104941812B (en
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李海生
陈英华
李超永
章新喜
何鑫
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China University of Mining and Technology CUMT
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Abstract

本发明涉及侧向负压吸附的微细粒物料摩擦电选方法和装置,微细粒物料在气流携带作用下经过摩擦带电器时,不同组分的颗粒间产生摩擦、碰撞作用,从而携带了极性不同、电量不等的电荷,并被喷入高压静电场;异性带电物料进入高压静电场内受到不同电场力的作用,带电物料向极性相反的电场方向偏移,并且由于罗茨风机供风时对连通高压静电场两侧的管道抽吸,使高压静电场内的带孔挡板与两侧电极板之间形成负压室,在负压室的吸附作用下,异性带电颗粒运动方向快速偏转进入负压室内,实现物料的快速分离。

The invention relates to a method and device for triboelectric separation of fine-grained materials adsorbed by lateral negative pressure. When the fine-grained materials pass through a friction charger under the action of airflow, friction and collision will occur between particles of different components, thereby carrying polarity. Charges with different electric quantities are sprayed into the high-voltage electrostatic field; heterosexually charged materials enter the high-voltage electrostatic field and are affected by different electric field forces. At the same time, the pipeline connected to both sides of the high-voltage electrostatic field is sucked, so that a negative pressure chamber is formed between the perforated baffle in the high-voltage electrostatic field and the electrode plates on both sides. The deflection enters the negative pressure chamber to realize the rapid separation of materials.

Description

侧向负压吸附的微细粒物料摩擦电选方法和装置Method and device for triboelectric separation of fine-grained materials by lateral negative pressure adsorption

技术领域 technical field

本发明涉及侧向负压吸附的微细粒物料摩擦电选方法和装置,为了实现异性带电颗粒在高压静电场内的快速、高效分离,属于矿物加工工程和农业工程领域,主要用于复杂矿物成分的分离,还可以用于农产品与杂质的分离过程。 The invention relates to a triboelectric separation method and device for fine-grained materials adsorbed by lateral negative pressure. In order to realize the rapid and efficient separation of heterosexually charged particles in a high-voltage electrostatic field, it belongs to the fields of mineral processing engineering and agricultural engineering, and is mainly used for complex mineral components. It can also be used in the separation process of agricultural products and impurities.

背景技术 Background technique

摩擦电选技术可以用于微细粒物料颗粒多组分物理分离。微细粒物料颗粒在摩擦碰撞带电后,不同组分携带了极性不同、电量不等的电荷。在高压静电场中,带电物料在电场力作用下产生运动偏转而相互分离。带电颗粒在气流的携带下进入高压电场,受到气体力作用较强,而高压静电场电极板间距较大,导致带电颗粒不能及时偏转和分离,降低了分离效率。这对于带电荷质比较小的颗粒尤为显著。而且在高压静电场中,异性带电的颗粒并不能按照理想状况实现运动偏转和分离,主要是带电颗粒间、颗粒与壁面存在相互摩擦、碰撞和接触,导致颗粒表面电荷产生了转移或中和,影响了带电颗粒的运动方向和分离过程。 Triboelectric separation technology can be used for the physical separation of multi-component particles of fine-grained materials. After the fine-grained material particles are charged by friction and collision, different components carry charges with different polarities and different electric quantities. In the high-voltage electrostatic field, the charged materials are deflected and separated from each other under the action of the electric field force. The charged particles enter the high-voltage electric field under the airflow, and are strongly affected by the gas force. However, the distance between the electrode plates in the high-voltage electrostatic field is relatively large, so that the charged particles cannot be deflected and separated in time, and the separation efficiency is reduced. This is especially noticeable for particles with relatively small charges. Moreover, in the high-voltage electrostatic field, the oppositely charged particles cannot achieve motion deflection and separation according to the ideal situation, mainly because there is mutual friction, collision and contact between the charged particles, particles and the wall surface, resulting in the transfer or neutralization of the surface charges of the particles. It affects the direction of movement and separation process of charged particles.

发明内容 Contents of the invention

为了克服上述现有技术的不足,本发明提供了侧向负压吸附的微细粒物料摩擦电选方法和装置,能够使带电颗粒在高压电场运动过程中,受到与电场力方向相同的负压吸附作用力,从而实现了异性带电物料的快速、高效地分离。 In order to overcome the deficiencies of the above-mentioned prior art, the present invention provides a triboelectric separation method and device for fine-grained materials with lateral negative pressure adsorption, which can make the charged particles receive negative pressure adsorption in the same direction as the electric field force during the movement process of the high-voltage electric field Force, so as to realize the rapid and efficient separation of oppositely charged materials.

本发明通过下述技术方案获得的:一种侧向负压吸附的微细粒物料摩擦电选方法,包括以下步骤:微细粒物料在气流携带作用下经过摩擦带电器时,不同组分的颗粒间产生摩擦、碰撞作用,从而携带了极性不同、电量不等的电荷,并被喷入高压静电场;异性带电物料进入高压静电场内受到不同电场力的作用,带电物料向极性相反的电场方向偏移,并且由于罗茨风机供风时对连通高压静电场两侧的管道抽吸,使高压静电场内的带孔挡板与两侧电极板之间形成负压室,在负压室的吸附作用下,异性带电颗粒运动方向快速偏转进入负压室内,实现物料的快速分离;负压室内的带电物料,粒径较大的落入收料器中,粒径较小的通过负压管道进入旋风分离器被分离收集,没有进入负压室的物料从高压静电场底部排出。 The present invention is obtained through the following technical scheme: a method for triboelectric separation of fine-grained materials by lateral negative pressure adsorption, comprising the following steps: when the fine-grained materials pass through the friction charger under the action of air flow, the particles of different components Friction and collision effects are generated, thereby carrying charges with different polarities and unequal electric quantities, and are sprayed into the high-voltage electrostatic field; heterosexually charged materials enter the high-voltage electrostatic field and are affected by different electric field forces, and the charged materials move toward the electric field of opposite polarity. The direction is offset, and because the Roots blower sucks the pipes connected to the two sides of the high-voltage electrostatic field when supplying air, a negative pressure chamber is formed between the perforated baffle in the high-voltage electrostatic field and the electrode plates on both sides. Under the action of adsorption, the moving direction of opposite charged particles is quickly deflected into the negative pressure chamber to realize the rapid separation of materials; in the negative pressure chamber, the charged materials with larger particle size fall into the receiver, and the smaller particle size passes through the negative pressure chamber. The pipe enters the cyclone separator and is separated and collected, and the material that does not enter the negative pressure chamber is discharged from the bottom of the high-voltage electrostatic field.

一种侧向负压吸附的微细粒物料摩擦电选装置,包括罗茨风机,与罗茨风机顺次连接的给料装置、摩擦带电器和高压静电场,与高压静电场连接的调压器和高压电源;高压静电场包括绝缘外壳,壳体的顶部和底部中心对应设有进料口和出料口,壳体的两侧连接有电极板,两电极板的下方分别设有收料器;壳体内设有两块与电极板平行的带孔挡板,挡板与电极板之间形成负压室,两挡板之间形成连通出料口和进料口的物料下落通道;高压静电场的两侧分别连接有粉尘过滤器,粉尘过滤器的外端连接有负压管,负压管的另一端连接旋风除尘器,旋风除尘器的出口与罗茨风机的吸气口相连。 A triboelectric separation device for fine-grained materials with lateral negative pressure adsorption, including a Roots blower, a feeding device sequentially connected to the Roots blower, a friction charger and a high-voltage electrostatic field, and a voltage regulator connected to the high-voltage electrostatic field and high-voltage power supply; the high-voltage electrostatic field includes an insulating shell, and the top and bottom centers of the shell are respectively equipped with a feed inlet and a discharge port, and the two sides of the shell are connected with electrode plates, and the bottom of the two electrode plates is respectively equipped with a material receiver. ; There are two perforated baffles parallel to the electrode plate inside the shell, a negative pressure chamber is formed between the baffles and the electrode plate, and a material falling channel connecting the discharge port and the feed port is formed between the two baffles; Dust filters are connected to both sides of the field, the outer end of the dust filter is connected to a negative pressure pipe, the other end of the negative pressure pipe is connected to a cyclone dust collector, and the outlet of the cyclone dust collector is connected to the suction port of the Roots blower.

所述挡板沿其高度方向等间距的加工有多道长方形通孔,通孔的两端为半圆形。 The baffle is processed with multiple rectangular through holes at equal intervals along its height direction, and the two ends of the through holes are semicircular.

所述挡板采用有机玻璃材料制成。 The baffle is made of plexiglass material.

所述粉尘过滤器的里端凸出于电极板设置。 The inner end of the dust filter protrudes from the electrode plate.

所述挡板与收料器的顶口通过倾斜支撑板连接。 The baffle is connected with the top port of the receiver through an inclined support plate.

所述高压静电场的出料口连通输送管道。 The discharge port of the high-voltage electrostatic field is connected with the conveying pipeline.

所述负压管上安装阀门,用于调节负压室压力。 A valve is installed on the negative pressure pipe for adjusting the pressure of the negative pressure chamber.

所述给料装置包括振动给料机和入料斗,振动给料机的出料口位于入料斗上方,通过入料斗持续向摩擦带电器送料。 The feeding device includes a vibrating feeder and a hopper. The outlet of the vibrating feeder is located above the hopper, and the material is continuously fed to the friction charger through the hopper.

所述罗茨风机的出风口设置转子流量计。 The air outlet of the Roots blower is provided with a rotameter.

本发明的有益效果是:微细粒物料在摩擦带电后进入高压静电场,由于挡板侧面存在负压吸附作用,带电颗粒在受到电场力作用的同时,还受到与电场力方向相同的负压吸附力作用,有助于异性带电颗粒的运动偏转,降低了带电颗粒间摩擦碰撞的概率,减小了相互接触的时间,从而实现了微细粒物料摩擦电选的高效分离。 The beneficial effects of the present invention are: the microfine material enters the high-voltage electrostatic field after being frictionally charged, and due to the negative pressure adsorption effect on the side of the baffle plate, the charged particles are also subjected to the negative pressure adsorption in the same direction as the electric field force while being acted on by the electric field force The action of force helps the motion deflection of oppositely charged particles, reduces the probability of frictional collision between charged particles, and reduces the time of mutual contact, thus realizing the efficient separation of fine-grained materials by triboelectric separation.

附图说明 Description of drawings

图1 是本发明侧向负压吸附的微细粒物料摩擦电选装置的实施例结构示意图。 Fig. 1 is a schematic structural view of an embodiment of a triboelectric separation device for fine-grained materials adsorbed by lateral negative pressure in the present invention.

图2是挡板结构示意图。 Figure 2 is a schematic diagram of the baffle structure.

图3 是电极板与粉尘过滤器安装示意图。 Figure 3 is a schematic diagram of the installation of electrode plates and dust filters.

图4是图3的侧视图。 FIG. 4 is a side view of FIG. 3 .

附图中各部件的标记如下:1.罗茨风机,2.转子流量计,3.入料斗,4.振动给料机,5.摩擦带电器,6.收料器,7.倾斜支撑板,8.挡板,9.粉尘过滤器,10.控制阀,11.电极板,12.螺钉,13.控制阀,14.旋风分离器,15.调压器,16.高压电源。 The marks of the components in the attached drawings are as follows: 1. Roots blower, 2. Rotameter, 3. Feeder hopper, 4. Vibrating feeder, 5. Friction charger, 6. Receiver, 7. Inclined support plate , 8. Baffle plate, 9. Dust filter, 10. Control valve, 11. Electrode plate, 12. Screw, 13. Control valve, 14. Cyclone separator, 15. Voltage regulator, 16. High voltage power supply.

具体实施方式 Detailed ways

侧向负压吸附的微细粒物料摩擦电选方法:通电情况下,微细粒颗粒通过振动给料机4均匀进入入料斗3,在自重作用下落入输送管道;罗茨风机1工作产生气流,微细粒物料经过摩擦带电器5时,不同组分的颗粒间产生摩擦、碰撞作用,从而携带了极性不同、电量不等的电荷,并被喷入高压静电场;异性带电物料进入高压静电场内受到不同电场力的作用,带电物料向极性相反的电场方向偏移,而带电量较小或不带电的物料下落;由于高压静电场的电极板11上安装有连通罗茨风机1吸气口的负压管,罗茨风机1供风时对负压管抽吸,使设于高压静电场内的带孔挡板8分别与两块电极板11之间形成负压室,在负压室的吸附作用下,使异性带电颗粒运动方向快速偏转进入负压室内,实现物料的快速分离;负压室内的带电物料,粒径较大的落入收料器6中,粒径较小的通过负压管道进入旋风分离器14被分离收集,没有进入负压室的物料落入高压静电场底部,通过管道进入物料输送管道中,重新进入电选工序。 The triboelectric separation method of fine-grained materials adsorbed by lateral negative pressure: under the condition of power on, the fine-grained particles enter the hopper 3 evenly through the vibrating feeder 4, and fall into the conveying pipeline under the action of their own weight; the Roots blower 1 works to generate airflow, and the fine When the granular material passes through the friction charger 5, friction and collision will occur between the particles of different components, thus carrying charges with different polarities and electric power, and sprayed into the high-voltage electrostatic field; heterosexually charged materials enter the high-voltage electrostatic field Affected by different electric field forces, the charged materials are shifted to the direction of the electric field with opposite polarity, while the materials with a small amount of charge or no charge fall down; because the electrode plate 11 of the high-voltage electrostatic field is installed with a suction port connected to the Roots blower 1 When the Roots blower 1 supplies air, it sucks the negative pressure pipe, so that the perforated baffle plate 8 in the high-voltage electrostatic field and the two electrode plates 11 form a negative pressure chamber respectively. Under the action of adsorption, the direction of movement of the charged particles of the opposite sex is quickly deflected into the negative pressure chamber to realize the rapid separation of materials; the charged materials in the negative pressure chamber fall into the receiver 6 with larger particle sizes, and the smaller particles pass through The negative pressure pipeline enters the cyclone separator 14 to be separated and collected, and the material that does not enter the negative pressure chamber falls to the bottom of the high-voltage electrostatic field, enters the material conveying pipeline through the pipeline, and enters the electric separation process again.

侧向负压吸附的微细粒物料摩擦电选装置,如附图1、2、3和4所示,该装置包括罗茨风机1,罗茨风机1的吹风口连接物料输送管道,输送管道靠近罗茨风机1的部位安装有转子流量计2,罗茨风机1运转时,提供了一定压力和流量的压缩空气,可以通过转子流量计2测得流量;物料输送管道通过法兰与摩擦带电器5以及高压静电场顺次连接;在罗茨风机1和摩擦带电器5之间设有振动给料机4,振动给料机4的出料口下方设有与物料输送管道连接的入料斗3,微细粒颗粒通过振动给料机4均匀进入入料斗3,在自重作用下落入输送管道;物料被罗茨风机1产生的气流带入摩擦带电器5中摩擦带电后进入高压静电场;高压静电场两侧设有电极板11,电极板11由螺栓与高压静电场的绝缘外壳连接,其中一块电极板11接地,另一块电极板11连接高压电源16,高压电源16连接调压器15;高压静电场的底部两侧设有收料器6;两块电极板11的中部和壳体的侧壁分别对称设有通孔,通孔中插入连接粉尘过滤器9,粉尘过滤器9的一端凸出于电极板11壁面,有助于被吸附物料颗粒的自由滑落,另一端凸出于壳体的侧壁并连接有负压管,两路负压管上分别设有控制阀10、13,两路负压管相交于一处后与一旋风分离器14的入口连接,旋风分离器14的出口与罗茨风机1的吸气口连接;电场内设有两块与电极板11平行的有机玻璃带孔挡板8,所述挡板8沿其高度方向等间距的加工有多道长方形通孔,通孔的两端为半圆形;挡板8分别与两块电极板11之间形成负压室,两挡板8之间形成连通出料口和进料口的物料下落通道,所述出料口通过法兰连接一出料管,出料管的另一端与入料斗3下方的物料输送管连接;挡板8与收料器6的顶口之间通过倾斜支撑板7连接,便于带电物料自由滑落并被收料器6收集。 The triboelectric separation device for fine-grained materials adsorbed by lateral negative pressure is shown in Figures 1, 2, 3 and 4. The device includes a Roots blower 1. The blower port of the Roots blower 1 is connected to a material delivery pipeline, and the delivery pipeline is close to Rotor flowmeter 2 is installed on the part of Roots blower 1. When Roots blower 1 is running, it provides compressed air with a certain pressure and flow rate, and the flow rate can be measured by rotameter 2; the material conveying pipeline passes through the flange and the friction charger. 5 and the high-voltage electrostatic field are connected in sequence; a vibrating feeder 4 is provided between the Roots blower 1 and the friction charger 5, and a hopper 3 connected to the material conveying pipeline is provided below the discharge port of the vibrating feeder 4 , the fine particles enter the hopper 3 evenly through the vibrating feeder 4, and fall into the conveying pipeline under the action of its own weight; the material is brought into the friction charger 5 by the airflow generated by the Roots blower 1 and then enters the high-voltage electrostatic field; There are electrode plates 11 on both sides of the field, and the electrode plates 11 are connected with the insulating shell of the high-voltage electrostatic field by bolts, one of the electrode plates 11 is grounded, and the other electrode plate 11 is connected to the high-voltage power supply 16, and the high-voltage power supply 16 is connected to the voltage regulator 15; Both sides of the bottom of the electrostatic field are provided with a material receiver 6; the middle part of the two electrode plates 11 and the side wall of the housing are respectively symmetrically provided with through holes, and the dust filter 9 is inserted and connected in the through holes, and one end of the dust filter 9 protrudes Out of the wall of the electrode plate 11, it is helpful for the particles of the adsorbed material to slide freely. The other end protrudes from the side wall of the housing and is connected with a negative pressure tube. The two negative pressure tubes are respectively provided with control valves 10 and 13. After the two-way negative pressure pipes intersect at one place, they are connected to the inlet of a cyclone separator 14, and the outlet of the cyclone separator 14 is connected to the suction port of the Roots blower 1; A glass perforated baffle 8, the baffle 8 is processed with multiple rectangular through holes at equal intervals along its height direction, and the two ends of the through holes are semicircular; the baffle 8 is formed between the two electrode plates 11 respectively Negative pressure chamber, between the two baffles 8 forms a material drop channel that communicates with the discharge port and the feed port, the discharge port is connected to a discharge pipe through a flange, the other end of the discharge pipe is connected to the bottom of the feed hopper 3 The material conveying pipe is connected; the baffle plate 8 and the top port of the receiver 6 are connected by an inclined support plate 7, which is convenient for the charged material to slide freely and be collected by the receiver 6.

Claims (10)

1. the fine granule material friction electrical selection method of a side direction negative-pressure adsorption, it is characterized in that, comprise the following steps: fine granule material under air-flow rolling action through friction belt electrical equipment, friction, collision effect is produced between the particle of different component, thus carry polarity difference, electricity electric charge not etc., and be injected into high-voltage electrostatic field; The charged material of the opposite sex enters in high-voltage electrostatic field the effect being subject to different electric field force, charged material offsets to opposite polarity direction of an electric field, and owing to aspirating the pipeline being communicated with both sides, high-voltage electrostatic field during roots blower air feed, make the baffle of porous baffle in high-voltage electrostatic field and form negative pressure chamber between the battery lead plate of both sides, under the suction-operated of negative pressure chamber, the opposite sex charged particle direction of motion deflects fast and enters in negative pressure chamber, realizes the quick separating of material; Charged material in negative pressure chamber, what particle diameter was larger falls into collector, and what particle diameter was less enters the separated collection of cyclone separator by negative-pressure pipeline, and the material not entering negative pressure chamber is discharged bottom high-voltage electrostatic field.
2. the fine granule material friction electrical selection method of a kind of side direction negative-pressure adsorption according to claim 1, is characterized in that, the material not entering negative pressure chamber is discharged to material conveying pipe bottom high-voltage electrostatic field, reenters electric separation operation.
3. a fine granule material friction electrical selection device for side direction negative-pressure adsorption, is characterized in that, comprise roots blower, the charging gear be connected in turn with roots blower, friction belt electrical equipment and high-voltage electrostatic field, the pressure regulator be connected with high-voltage electrostatic field and high voltage source; High-voltage electrostatic field comprises insulation crust, and top and bottom centre's correspondence of housing are provided with charging aperture and discharging opening, and the both sides of housing are connected with battery lead plate, and the below of two battery lead plates is respectively equipped with collector; Be provided with two pieces of baffle of porous baffles parallel with battery lead plate in housing, between baffle plate and battery lead plate, form negative pressure chamber, between two baffle plates, form the material dropping channel being communicated with discharging opening and charging aperture; The both sides of high-voltage electrostatic field are connected to dust filter unit, and the outer end of dust filter unit is connected with negative tube, and the other end of negative tube connects cyclone dust collectors, and the outlet of cyclone dust collectors is connected with the air entry of roots blower.
4. the fine granule material friction electrical selection device of a kind of side direction negative-pressure adsorption according to claim 3, is characterized in that, described baffle plate is processed with multiple tracks rectangular through holes along its short transverse is equally spaced, and the two ends of through hole are semicircle; Described baffle plate adopts pmma material to make.
5. the fine granule material friction electrical selection device of a kind of side direction negative-pressure adsorption according to claim 3, is characterized in that, the inner end of described dust filter unit protrudes from battery lead plate and arranges.
6. the fine granule material friction electrical selection device of a kind of side direction negative-pressure adsorption according to claim 3, is characterized in that, described baffle plate is connected by inclined support panel with the top mouth of collector.
7. the fine granule material friction electrical selection device of a kind of side direction negative-pressure adsorption according to claim 3, is characterized in that, the discharging opening of described high-voltage electrostatic field is communicated with conveyance conduit.
8. the fine granule material friction electrical selection device of a kind of side direction negative-pressure adsorption according to claim 3, is characterized in that, mounted valve on described negative tube, for regulating negative pressure chamber's pressure.
9. the fine granule material friction electrical selection device of a kind of side direction negative-pressure adsorption according to claim 3, it is characterized in that, described charging gear involving vibrations batcher and material bin, the discharging opening of oscillating feeder is positioned at above material bin, is continued to the feeding of friction belt electrical equipment by material bin.
10. the fine granule material friction electrical selection device of a kind of side direction negative-pressure adsorption according to claim 3, it is characterized in that, the air outlet of described roots blower arranges spinner flowmeter.
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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105903570A (en) * 2016-05-20 2016-08-31 昆明理工大学 Impact type friction electric separator
CN106000654A (en) * 2016-05-23 2016-10-12 中国矿业大学 Reverse-feed friction electric separation separating device for particles
CN106890729A (en) * 2017-03-14 2017-06-27 昆明理工大学 The friction charged method and device of one kind classification
CN107684978A (en) * 2017-10-12 2018-02-13 宁波工程学院 A kind of circulating frictional static dust arrester
CN108940599A (en) * 2018-08-01 2018-12-07 中国矿业大学 A kind of particle electrification separation system
CN109675743A (en) * 2017-08-24 2019-04-26 太仓市众翔精密五金有限公司 A kind of spray painting powder recovering device and its way of recycling
CN111420192A (en) * 2020-04-09 2020-07-17 上海新黄河制药有限公司 Inhalation device for in-situ preparation of negatively charged powder
CN113731632A (en) * 2021-09-02 2021-12-03 江西金泰源陶瓷有限公司 Ceramic dry powder making, dust collecting and impurity removing integrated device

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3493109A (en) * 1967-08-04 1970-02-03 Consiglio Nazionale Ricerche Process and apparatus for electrostatically separating ores with charging of the particles by triboelectricity
JPS5742355A (en) * 1980-08-23 1982-03-09 Senichi Masuda Electrostatic separator
DE3921072A1 (en) * 1989-06-28 1991-01-10 Kali & Salz Ag Electrostatic processing of crude potash with no wet stage - using free fall separator in which vertical air flow is maintained
CN2304472Y (en) * 1997-10-01 1999-01-20 中国矿业大学 Friction electrostatic sorting device
US5944875A (en) * 1996-10-22 1999-08-31 University Of Kentucky Research Foundation Triboelectric separator with mixing chamber and pre-separator
JP2002177820A (en) * 2000-12-12 2002-06-25 Matsushita Electric Ind Co Ltd Method and apparatus for feeding / transferring plastic pulverized material and electrostatic sorting apparatus for plastic pulverized material
CN101011681A (en) * 2006-02-05 2007-08-08 中国矿业大学 Fine granule material friction electrical selection method and device
CN202921425U (en) * 2012-12-04 2013-05-08 海南文盛新材料科技有限公司 Wool stripping device of electric separator
CN103721871A (en) * 2013-12-24 2014-04-16 辽宁中邦高新技术发展有限公司 Environment-friendly cement water-reducing agent sorting system

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3493109A (en) * 1967-08-04 1970-02-03 Consiglio Nazionale Ricerche Process and apparatus for electrostatically separating ores with charging of the particles by triboelectricity
JPS5742355A (en) * 1980-08-23 1982-03-09 Senichi Masuda Electrostatic separator
DE3921072A1 (en) * 1989-06-28 1991-01-10 Kali & Salz Ag Electrostatic processing of crude potash with no wet stage - using free fall separator in which vertical air flow is maintained
US5944875A (en) * 1996-10-22 1999-08-31 University Of Kentucky Research Foundation Triboelectric separator with mixing chamber and pre-separator
CN2304472Y (en) * 1997-10-01 1999-01-20 中国矿业大学 Friction electrostatic sorting device
JP2002177820A (en) * 2000-12-12 2002-06-25 Matsushita Electric Ind Co Ltd Method and apparatus for feeding / transferring plastic pulverized material and electrostatic sorting apparatus for plastic pulverized material
CN101011681A (en) * 2006-02-05 2007-08-08 中国矿业大学 Fine granule material friction electrical selection method and device
CN202921425U (en) * 2012-12-04 2013-05-08 海南文盛新材料科技有限公司 Wool stripping device of electric separator
CN103721871A (en) * 2013-12-24 2014-04-16 辽宁中邦高新技术发展有限公司 Environment-friendly cement water-reducing agent sorting system

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105903570A (en) * 2016-05-20 2016-08-31 昆明理工大学 Impact type friction electric separator
CN105903570B (en) * 2016-05-20 2017-08-29 昆明理工大学 A kind of impact type triboelectric separator
CN106000654A (en) * 2016-05-23 2016-10-12 中国矿业大学 Reverse-feed friction electric separation separating device for particles
CN106000654B (en) * 2016-05-23 2017-10-27 中国矿业大学 A kind of particle reversely feeds friction electrical selection separator
CN106890729A (en) * 2017-03-14 2017-06-27 昆明理工大学 The friction charged method and device of one kind classification
CN109675743A (en) * 2017-08-24 2019-04-26 太仓市众翔精密五金有限公司 A kind of spray painting powder recovering device and its way of recycling
CN107684978A (en) * 2017-10-12 2018-02-13 宁波工程学院 A kind of circulating frictional static dust arrester
CN108940599A (en) * 2018-08-01 2018-12-07 中国矿业大学 A kind of particle electrification separation system
CN111420192A (en) * 2020-04-09 2020-07-17 上海新黄河制药有限公司 Inhalation device for in-situ preparation of negatively charged powder
CN113731632A (en) * 2021-09-02 2021-12-03 江西金泰源陶瓷有限公司 Ceramic dry powder making, dust collecting and impurity removing integrated device

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