WO2010109096A1 - Procédé de séparation électrostatique d'un mélange de granules de matériaux différents et dispositif de mise en oeuvre - Google Patents
Procédé de séparation électrostatique d'un mélange de granules de matériaux différents et dispositif de mise en oeuvre Download PDFInfo
- Publication number
- WO2010109096A1 WO2010109096A1 PCT/FR2010/000245 FR2010000245W WO2010109096A1 WO 2010109096 A1 WO2010109096 A1 WO 2010109096A1 FR 2010000245 W FR2010000245 W FR 2010000245W WO 2010109096 A1 WO2010109096 A1 WO 2010109096A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- granules
- air
- electrodes
- air stream
- separation
- Prior art date
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
- 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
-
- 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
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/02—Plant or installations having external electricity supply
- B03C3/04—Plant or installations having external electricity supply dry type
- B03C3/14—Plant or installations having external electricity supply dry type characterised by the additional use of mechanical effects, e.g. gravity
-
- 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
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/28—Plant or installations without electricity supply, e.g. using electrets
- B03C3/30—Plant or installations without electricity supply, e.g. using electrets in which electrostatic charge is generated by passage of the gases, i.e. tribo-electricity
-
- 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
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/36—Controlling flow of gases or vapour
- B03C3/368—Controlling flow of gases or vapour by other than static mechanical means, e.g. internal ventilator or recycler
-
- 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, pyroelectricity
Definitions
- the invention relates to a method for the electrostatic separation of granular materials and to an implementation device.
- Electrostatic separation processes are already used to sort mixed granular materials from, for example, industrial waste grinding. Preferably, these materials are insulating.
- the recycling of electrical and / or electronic waste requires the separation of the various components before valuing the materials obtained. This separation must be as effective as possible to obtain a substantially constant quality of the materials obtained. It is then conceivable to create and sustain a downstream value chain for these materials.
- plastic materials recovered from electrical and / or electronic waste can be used for the manufacture of terrace decking boards. To sustain this activity, the boards must have a quality and a substantially constant color.
- the negative electrode while the negatively charged granules are attracted to the cathode (the positive electrode).
- the granules thus deviated in their fall are separated and fall into two different collectors arranged at the bottom of the device and at the right of the electrodes.
- Granules that have not been attracted to the electrodes fall into a third central collector where they are recovered. They can then be recirculated in the sorting device.
- These granules may have lost their charge during conveying between the triboelectric charging device and the sorting device. They may also have acquired a charge too low to be attracted to an electrode.
- the electrical charge acquired by the granules in the aforementioned devices is not homogeneous. Some granules are able to charge properly and can be separated in a fairly intense electric field, while others leave the triboelectric charging devices with insufficient charge to allow their separation. As a result, a large quantity of unseparated granules must be recovered and then returned to the triboelectric charging device. The productivity of the process is low since the return of the granules in the triboelectric charging device limits the loading of new granules.
- the state of charge of the granules could be improved by increasing the duration of the triboelectric charging process.
- productivity of the process would not be improved since the granules would remain longer in the triboelectric charging device, which consumes time and energy.
- the amount of charge actually acquired by the granules can vary significantly with the surface condition of the granules and, more particularly, their size. Indeed, when two granules of different sizes collide, they acquire two opposite electric charges and of the same value. However, if this value is sufficient for the smaller granule to be attracted to one electrode, it is insufficient for the larger granule to be attracted to the other electrode.
- the known installations therefore preferably have a size sieving means of the granules, arranged upstream of the triboelectric charging device. Then each type of granule is loaded and then electrically separated. The amount of filler actually acquired by the granules can also vary significantly with ambient temperature and humidity.
- the present invention aims to overcome the above drawbacks and proposes a method of electrostatic separation of granular insulating materials and an implementation device, performing in terms of quality and productivity of the triboelectric charge and sorting. They are also versatile, energy efficient and easily adapt to ambient atmospheric conditions and physicochemical properties of the granules to be separated.
- the invention provides a method and a device for simultaneously, within a single chamber, the electrical charge of the granules and their electrostatic separation.
- the subject of the invention is a process for the electrostatic separation of a mixture of granules of different materials, comprising the following steps: a) between two electrodes in a separation chamber delimited by walls and provided with an inlet and a an air outlet, injection of a fluidization air stream; b) introducing the mixture of granules of different materials into the fluidization air stream; c) controlling the flow of fluidization air, so that the granules levitate in the air stream in a turbulent regime and charge electrically by contacts between them and / or the walls of the separation chamber; d) generating an electric field between the two electrodes, substantially perpendicular to the direction of the air current, such as the granules charged in step c), move in the direction of the electric field if they are charged positively, or in opposite directions if their load is negative; e) adhesion of charged granules to the surface of the electrodes; f) evacuation and collection of granules adhered to each electrode.
- the fluidization air stream can be injected substantially in the upward vertical direction, and in step b), the granule mixture can be introduced by free fall and countercurrently by relative to the fluidizing air stream;
- the stream of fluidization air, injected into the separation chamber in step a), may have a negative pressure gradient in the upward vertical direction;
- the introduction of the mixture of granules in step b) can be carried out according to a flow rate, expressed as mass of granules introduced per unit of time, regulated to a value substantially equal to the mass of granules collected in step f) per unit of time;
- the air stream can be preheated before entering the separation chamber; • the air stream can be homogenized by entering the separation chamber;
- Step f) may be implemented by means of treadmill-type electrically conductive electrodes, the discharge of the granules being carried out by translating the treadmills, and the collection being carried out by scraping; and or
- the method may further comprise a step g), subsequent to step f), of cleaning the electrodes.
- the invention also relates to a device for electrostatically separating a mixture of granules of different materials, characterized in that it comprises:
- a separation chamber delimited by walls and provided with an inlet and an air outlet;
- a means for controlling the fluidization air stream such that, in use, the granules levitate in the air stream in a turbulent regime and are electrically charged by contacts between them and / or with the walls of the separation chamber ; means for generating, between the two electrodes, an electric field substantially perpendicular to the direction of the air current;
- the air inlet can be arranged in such a way that the air flow is
- the means for introducing the mixture of granules can be arranged to introduce the granules, into the separation chamber, by free fall and countercurrently with respect to the stream of fluidization air;
- the electrodes can be arranged divergently from the air inlet to the air outlet;
- the separation device may comprise a heating means of the air stream arranged upstream of the air inlet of the separation chamber;
- the separation device may comprise an air chamber arranged downstream of the air inlet of the separation chamber and comprising means for homogenizing the air stream;
- the homogenization means of the air stream may be glass balls;
- the separation device may comprise a means for controlling the rate of introduction of the granules
- the separation device may comprise a means for measuring the mass of collected granules connected to the flow control means, the latter being adapted to control the rate of introduction of the granules as a function of the mass measured by the measuring means. ;
- the means for collecting the granules may be a doctor blade
- the separation device may comprise a means for cleaning the electrodes;
- the electrodes may be of the treadmill type; and or
- the means for generating the electric field can be adjustable.
- the method and the device according to the invention make it possible to remedy the aforementioned drawbacks by simultaneously carrying out the charging of the granules by triboelectric effect and their separation in an electric field.
- the granules can not lose their charge between the moment they are charged and the moment when they are subjected to the electric field.
- the air stream separates the granules by size, so the triboelectric charge is optimal because it is made on granules of substantially the same size.
- each granule remains in the air stream only the minimum time necessary to acquire a triboelectric charge sufficient to be attracted to one of the electrodes.
- the uncharged granules can not leave the air stream, which guarantees the purity of the granules collected.
- the method and the device according to the invention optimize the sorting efficiency and adapt naturally to each granule.
- a device according to the invention has a significantly improved efficiency and quality of sorting compared to a device of the state of the art of equivalent useful dimensions.
- FIG. 1 is a schematic longitudinal sectional view of a first embodiment of an electrostatic separation device according to the invention.
- an electrostatic separation device according to the invention comprises a separation chamber 100 delimited by side walls 101 (only two of which have been illustrated) and provided with an air inlet 102 and a air outlet 103 respectively for the admission and discharge of compressed air.
- the air inlet 102 is provided with an air diffuser 102a, and the air outlet 103 is provided with a filter 103a.
- Two electrodes 105-106 extend in the separation chamber between and on either side of the inlet and the air outlet. Thus, the flow of air flowing between the inlet and the air outlet is located between the electrodes 105-106. These electrodes are connected to a continuous high voltage generator 107, preferably adjustable: the electrode 105 is connected to the negative terminal of the generator 107, and the electrode 106 is connected to the positive terminal of the generator 107. This arrangement generates a electric field between the two electrodes 105-106 when the current flows.
- the electrodes are arranged divergently from the air inlet to the air outlet.
- the device also comprises an injection means 108, between the two electrodes 105-106, of a stream of air in a determined direction represented by the arrow F1.
- the air stream thus passes through the separation chamber 100 between the inlet 102 and the air outlet 103.
- This stream of air forms a fluidized bed.
- the air inlet 102 is advantageously arranged so that the air stream is, in use, substantially in an upward vertical direction.
- a means 109 is arranged to allow the introduction of a mixture M of granules into the stream of fluidization air.
- the introduction means 109 of the mixture of granules M is arranged to introduce the granules, in the separation chamber 100, by free fall and countercurrent with respect to the fluidization air stream.
- the means 109 is preferably variable rate controlled by flow control means (not shown).
- the mixture M comprises at least two different materials M1-M2, illustrated in the figures, by white disks M1 and black disks M2.
- the granules can be of different sizes.
- two sizes small size: M1p and M2p, and large size: M1g and M2g
- M1p and M2p small size
- M1g and M2g large size
- the means 108 for injecting the fluidization air stream is connected to a means for controlling the fluidization air stream such that, in use, the granules levitate in the air stream in a turbulent regime and charge electrically. by contact between them and / or with the walls
- the device according to the invention allows the implementation of the electrostatic separation process of the mixture of granules of different materials according to the invention. It includes the following steps.
- a stream of fluidizing air is injected between the two electrodes.
- This stream of air comes from the air inlet 102 and is discharged through the air outlet 103.
- the fluidization air stream is injected substantially in an upward vertical direction. .
- the divergent configuration of the electrodes creates a negative pressure gradient in the upward vertical direction. In other words, the air pressure decreases in the direction of the air flow.
- the air pressure at the air outlet 103 at the top of the chamber 100 is less than the air pressure at the air inlet.
- a step b) the mixture of granules M of different materials is introduced into the stream of fluidization air.
- the granule mixture is introduced by free fall and countercurrently with respect to the fluidization air stream.
- a step c) the flow of fluidizing air is controlled so that the granules levitate in the air stream according to a turbulent regime and charge electrically by contacts between them and / or with the walls of the separation chamber.
- the negative pressure gradient makes it possible to distribute the granules at different heights, in relation to their dimensions: the larger or heavier granules remain below, while the smaller or lighter granules rise more in the fluidized bed.
- the upper limit of the fluidized bed is established by the smaller or lighter granules, but the air flow is controlled so that this upper limit does not exceed, preferably, two thirds of the height of the separation chamber 100.
- the method and the device according to the invention therefore allow a natural distribution of the granules according to their mass within the chamber itself. It is therefore not necessary to carry out a size-screening of the mixture M before introduction into the separation chamber 100.
- the characteristic diameter of the granules of the mixture M may advantageously be between 0.5 and 5 mm.
- the method and the device according to the invention thus make it possible to obtain a dimensional homogeneity of the granules which come into contact with each other. This ensures the best triboelectric charging conditions because two granules of substantially the same mass, but of different materials, acquire two opposite charges of the same value. This allows the granules to be each attracted by an electrode.
- an electric field E is generated between the two electrodes, substantially perpendicular to the F1 direction. of the air stream, and directed from the cathode to the anode.
- the electric field necessary for the implementation of the invention is preferably greater than 1 kV / cm. It is typically between 4 and 5 kV / cm.
- the granules charged in step c) move either in the direction of the electric field if they are positively charged, or in the opposite direction if their charge is negative.
- the granules M1p and M 1g are negatively charged and move towards the cathode 106, in the opposite direction of the electric field E.
- the granules M2p and M2g are positively charged and move towards the anode 105, in the same direction as that of the electric field E. Submitted to the action of the electric image force, the granules
- the method according to the invention comprises a step f) of discharging and collecting the granules adhered to each electrode.
- this step f) is implemented using treadmill-type electrodes, advantageously in electrically conductive material such as a metal.
- the conveyor belt is made of stainless steel with a smooth surface. It is also possible to use treadmills made of plastic materials with metal inserts.
- the electrodes 105 and 106 are set in translation to discharge the granules deposited on their surface in a direction schematized by the arrow F2, substantially concurrent with the current of air. It is also possible to drive the treadmill in the opposite direction, that is to say substantially counter-current relative to the air stream. However, the granules adhered to the surface of the treadmills may be peeled off by the air stream.
- the tread convey the granules away from the air flow relative to the electrodes. Then, the granules are collected on the treadmill by scraping, using doctor blades 110. These take off the granules of the treadmill and direct them to a collector 111 - 112.
- the speed of the belt is correlated with the flow of granules from the means 109 for introducing the mixture M of granules, the initial composition of the granular mixture to be separated and the width of the belt. It must be sufficient for the granules attracted by the electrode to form a single layer on the surface of the carpet. Otherwise, the Electric image strength is not important enough to adhere the granules to the carpet.
- the granules would remain in contact with the electrode mat long enough for them to discharge. This has the effect of decreasing the electrical image force which adheres the granules to the carpet surface. The granules may then become detached from the carpet before they can be recovered by the collectors 111-112, and fall back to the base of the electrodes. If the air flow is as wide as the distance separating the base of each electrode, the falling granules can be recirculated into the air stream. Otherwise the granules fall in the bottom of the chamber 100 and must be recovered and reintroduced into the chamber via the means 109.
- a flow rate of about 300 kg / hour and a carpet having a width of 1 m a speed of the order of 5 m / min may be sufficient.
- the method according to the invention may further comprise a step g) of cleaning the electrodes, subsequent to step f).
- the separating device according to the invention comprises a means for cleaning the electrodes, shown diagrammatically in FIGS. 1 and 2 by brushes 113. These make it possible to unstick the granules which would not have been removed by the doctor blades. 110. They especially allow to rid the treadmill dust P inevitably generated by the implementation of the process. Indeed, the shocks of the granules together, during triboelectric charging, cause some erosion of these granules which is materialized by dust. This accumulates on the treadmill and can decrease the adhesion of the granules by the electric image force.
- the brushes 113 make it possible to rid the carpets of this dust and to maintain the power of attraction and adhesion during the entire operating life of the device.
- the collectors 111 - 112 are in sealed contact with the corresponding conveyor belt 106 - 105 for collecting the dust and evacuating it from the chamber 100.
- the dust P can be evacuated by a dedicated collector 114.
- rotary electrodes combined with a doctor blade disposed opposite the fluidizing air stream relative to the electrodes can be used.
- Mobile evacuation and collection means may also be used with respect to a stationary electrode.
- the charge is made within the separation chamber, so that the granules are not likely to lose their charge before being subjected to the electric field.
- the fact that the granules are immediately discharged as soon as they adhere to an electrode also optimizes the yield, since the granules do not have time to lose their charge, and leaves room for other granules to adhere to the electrodes .
- the device comprises a granule introduction rate control means connected to a measurement means (not shown) of the mass of granules collected by the collectors 111 and 112.
- the introduction of the mixture of granules in step b) is carried out according to a flow rate, expressed as mass of granules introduced per unit of time, regulated to a value substantially equal to the mass of granules collected in step f) per unit of time.
- the flow control means is adapted to control the rate of introduction of the granules as a function of the mass measured by the measuring means.
- the air stream is preheated before entering the separation chamber.
- the electrostatic separation device according to the invention comprises a heating means 120 of the air stream, arranged upstream of the air inlet 102 of the separation chamber 100.
- the electrostatic separation device may also comprise an air chamber 130, arranged downstream of the air inlet 102 of the separation chamber 100, and comprising means for homogenizing the incoming air flow. in the separation chamber 100.
- this air chamber 130 is disposed upstream of the air diffuser 102a and is connected to a compressor 131.
- the means for homogenizing the air stream are, for example, glass balls 132. Their distribution in the air chamber 130 divides the stream of compressed air, so that the air stream is homogeneous along its entire width when it enters the chamber 100 and ensures a uniform horizontal pressure in the separation chamber 100.
- the introduction of the granules can be made by spraying from the bottom of the separation chamber, with the flow of air (and optionally a complementary air stream) so that the projected granules upwards levitate in the air stream in a turbulent regime and are electrically charged by contacts between them and / or with the walls of the separation chamber.
Landscapes
- Electrostatic Separation (AREA)
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13/259,874 US8541709B2 (en) | 2009-03-27 | 2010-03-23 | Method for electrostatically separating a granule mixture made of different materials, and device for implementing same |
KR1020117025345A KR101736362B1 (ko) | 2009-03-27 | 2010-03-23 | 이종 소재로 구성된 과립 혼합물을 정전기로 분리하는 방법 및 그 시행 장치 |
CA2756629A CA2756629C (fr) | 2009-03-27 | 2010-03-23 | Procede de separation electrostatique d'un melange de granules de materiaux differents et dispositif de mise en oeuvre |
JP2012501342A JP5661097B2 (ja) | 2009-03-27 | 2010-03-23 | 様々な材料でできている細粒混合物を静電分離する方法、およびこの方法を実施する装置 |
EP10726143.0A EP2411155B1 (fr) | 2009-03-27 | 2010-03-23 | Procédé de séparation électrostatique d'un mélange de granules de matériaux différents et dispositif de mise en oeuvre |
CN201080017973.6A CN102421530B (zh) | 2009-03-27 | 2010-03-23 | 静电分离由不同材料构成的颗粒混合物的方法以及实施该方法的装置 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR0901494A FR2943561B1 (fr) | 2009-03-27 | 2009-03-27 | Procede de separation electrostatique d'un melange de granules de materiaux differents et dispositif de mise en oeuvre |
FR0901494 | 2009-03-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2010109096A1 true WO2010109096A1 (fr) | 2010-09-30 |
Family
ID=41277499
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/FR2010/000245 WO2010109096A1 (fr) | 2009-03-27 | 2010-03-23 | Procédé de séparation électrostatique d'un mélange de granules de matériaux différents et dispositif de mise en oeuvre |
Country Status (9)
Country | Link |
---|---|
US (1) | US8541709B2 (fr) |
EP (1) | EP2411155B1 (fr) |
JP (1) | JP5661097B2 (fr) |
KR (1) | KR101736362B1 (fr) |
CN (1) | CN102421530B (fr) |
CA (1) | CA2756629C (fr) |
FR (1) | FR2943561B1 (fr) |
MY (1) | MY160936A (fr) |
WO (1) | WO2010109096A1 (fr) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU179023U1 (ru) * | 2017-12-25 | 2018-04-25 | Научно-производственная корпорация "Механобр-техника" (Акционерное общество) | Электростатический вибрационный сепаратор |
RU185261U1 (ru) * | 2018-09-13 | 2018-11-29 | Научно-производственная корпорация "Механобр-техника" (Акционерное общество) | Электростатический вибрационный сепаратор |
WO2024042205A1 (fr) | 2022-08-26 | 2024-02-29 | Skytech | Procédé de séparation d'un mélange de granules par effet triboélectrique |
Families Citing this family (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102010026445A1 (de) * | 2010-07-08 | 2012-01-12 | Evonik Degussa Gmbh | Flugaschetrennung mittels Koronaentladung |
CN103008316A (zh) * | 2012-12-11 | 2013-04-03 | 吴江兰瑞特纺织品有限公司 | 一种悬挂式纤维收集槽 |
JP6138970B2 (ja) * | 2013-04-15 | 2017-05-31 | ポスコPosco | 原料の選別装置及びその選別方法 |
CN106076626B (zh) * | 2016-06-07 | 2017-08-25 | 燕山大学 | 一种基于颗粒尺度的多级静电除尘设备 |
KR101850689B1 (ko) * | 2016-08-10 | 2018-06-11 | 주식회사크러텍 | 분진제거장치 |
CN108014922B (zh) * | 2017-11-08 | 2020-04-21 | 南方科技大学 | 一种摩擦电热电内搅拌除尘检测设备及其除尘检测方法 |
CN108057523B (zh) * | 2017-11-08 | 2020-04-17 | 南方科技大学 | 一种摩擦电热电除尘检测设备及其除尘检测方法 |
CN108097458B (zh) * | 2017-11-08 | 2020-04-17 | 南方科技大学 | 一种热电自驱动除尘检测设备及其除尘检测方法 |
CN108176510B (zh) * | 2017-11-08 | 2020-04-21 | 南方科技大学 | 一种摩擦电热电自驱动除尘检测设备及其除尘检测方法 |
FR3078638B1 (fr) | 2018-03-07 | 2020-04-10 | Universite De Poitiers | Procede et dispositif de separation electrostatique de materiaux granulaires |
WO2021048351A2 (fr) | 2019-09-11 | 2021-03-18 | Michiel Cramwinckel | Procédé pour transformer un déchet polymère en un produit gazeux |
CN111822151B (zh) * | 2020-05-21 | 2021-11-16 | 浙江大学 | 一种利用静电解析聚乙烯生长形貌的系统和方法 |
CN114011575B (zh) * | 2020-07-28 | 2023-07-21 | 郑州信息科技职业学院 | 一种发动机实验用进气过滤装置 |
KR102460590B1 (ko) * | 2020-11-24 | 2022-10-28 | 주식회사 국민기계 | 비산 철 분진 포집 장치 |
US20230175099A1 (en) * | 2021-11-10 | 2023-06-08 | Comstock Ip Holdings Llc | Li-ion battery recycling process and system for black mass fractionation and recovery of specific materials |
FR3129092B1 (fr) | 2021-11-15 | 2023-11-10 | Michelin & Cie | Installation destinée à séparer dans un champ électrique les composants d’un mélange de fibres et de granules à l’aide d’un tribochargeur pourvu d’une grille de confinement sélectif desdits composants |
WO2023083988A1 (fr) | 2021-11-15 | 2023-05-19 | Compagnie Generale Des Etablissements Michelin | Installation destinée à séparer dans un champ électrique les composants d'un mélange de fibres et de granules à l'aide d'un tribochargeur pourvu d'une grille de confinement sélectif desdits composants |
FR3132448B1 (fr) | 2022-02-09 | 2024-01-19 | Michelin & Cie | Installation de séparation des composants d’un mélange de fibres et granules par battage du mélange au moyen d’un champ électrique alternatif |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1574621A (fr) * | 1967-08-04 | 1969-07-11 | ||
DE2643002B1 (de) * | 1976-09-24 | 1977-11-10 | Kali & Salz Ag | Vorrichtung zur elektrostatischen aufladung und trennung von mineralstoffgemischen |
JPS5742355A (en) * | 1980-08-23 | 1982-03-09 | Senichi Masuda | Electrostatic separator |
US4627579A (en) * | 1983-08-05 | 1986-12-09 | Advanced Energy Dynamics, Inc. | Particle charging and collecting system |
EP0279200A2 (fr) * | 1987-02-17 | 1988-08-24 | Organ-Faser Technology Company N.V. | Procédé pour la séparation de parties en matériau électriquement non conducteur à partir d'ordure, en particulier de plastic et/ou papier et appareil à cet effet |
US5885330A (en) * | 1996-08-12 | 1999-03-23 | Lee; Jae Keun | Separation system and method of unburned carbon in flyash from a coal-fired power plant |
DE19912462A1 (de) * | 1998-08-19 | 2000-02-24 | Lehmann Maschf F B | Verfahren und Vorrichtung zur Trennung eines Bruchgutes |
Family Cites Families (25)
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 |
JPS5982955A (ja) * | 1982-10-26 | 1984-05-14 | 張 均仁 | 循環電極式静電気集塵装置 |
US4605485A (en) * | 1984-04-17 | 1986-08-12 | Exxon Research And Engineering Co. | Charge injection device |
DE3434190C1 (de) * | 1984-09-18 | 1985-10-24 | Kali Und Salz Ag, 3500 Kassel | Verfahren und Vorrichtung zur Steuerung der elektrostatischen Trennung von Kalirohsalzen in elektrostatischen Freifallscheidern |
EP0185966B1 (fr) * | 1984-12-21 | 1989-01-25 | BBC Brown Boveri AG | Procédé et dispositif de dépoussiérage d'un courant de gaz contenant des particules solides ou liquides au moyen d'un champ électrique |
JPS63287568A (ja) * | 1987-05-19 | 1988-11-24 | Teijin Ltd | 粉体粒子の分級方法及びその装置 |
DE4139472C1 (fr) * | 1991-11-29 | 1993-03-11 | Gerhard Dr. 8011 Kirchheim De Weber | |
JP3222045B2 (ja) * | 1995-09-26 | 2001-10-22 | 日立造船株式会社 | 放電・落下型静電選別装置 |
JPH1057835A (ja) * | 1996-08-14 | 1998-03-03 | San Techno Kk | 油性ヒューム捕集装置 |
DE19648373C1 (de) * | 1996-11-22 | 1998-01-08 | Kali & Salz Ag | Elektrostatische Trennvorrichtung zur Sortierung triboelektrisch aufgeladener Stoffgemische |
US6074458A (en) * | 1997-02-24 | 2000-06-13 | Separation Technologies, Inc. | Method and apparatus for separation of unburned carbon from flyash |
KR100235290B1 (ko) * | 1997-12-13 | 1999-12-15 | 명호근 | 기류 충돌 정전 분리형을 이용한 미분체의 분리방법 및 장치 |
JP3601319B2 (ja) * | 1998-10-14 | 2004-12-15 | 松下電器産業株式会社 | 静電選別装置及び選別方法 |
JP3606749B2 (ja) * | 1998-11-05 | 2005-01-05 | 日立造船株式会社 | プラスチック選別装置 |
JP2000140700A (ja) * | 1998-11-12 | 2000-05-23 | Konica Corp | 粉体分離装置および粉体分離方法 |
US6452126B1 (en) * | 1999-03-12 | 2002-09-17 | Mba Polymers, Inc. | Electrostatic separation enhanced by media addition |
US6651818B1 (en) * | 1999-10-28 | 2003-11-25 | Bcde Group Waste Management Ltd Oy | Ion particle classifier and classifying method |
US6329623B1 (en) * | 2000-06-23 | 2001-12-11 | Outokumpu Oyj | Electrostatic separation apparatus and method using box-shaped electrodes |
JP4830196B2 (ja) * | 2000-12-12 | 2011-12-07 | パナソニック株式会社 | プラスチック粉砕物の静電選別装置 |
JP3981014B2 (ja) * | 2001-03-27 | 2007-09-26 | 川崎重工業株式会社 | 粒子の静電分離方法 |
JP3984059B2 (ja) * | 2002-01-21 | 2007-09-26 | 川崎重工業株式会社 | 排ガス浄化装置 |
US6773489B2 (en) * | 2002-08-21 | 2004-08-10 | John P. Dunn | Grid type electrostatic separator/collector and method of using same |
JP2006322683A (ja) * | 2005-05-20 | 2006-11-30 | Mitsubishi Heavy Ind Ltd | 蒸気発生器 |
US7880108B2 (en) * | 2007-10-26 | 2011-02-01 | Becton, Dickinson And Company | Deflection plate |
JP5742355B2 (ja) * | 2011-03-24 | 2015-07-01 | セイコーエプソン株式会社 | 頭部装着型表示装置 |
-
2009
- 2009-03-27 FR FR0901494A patent/FR2943561B1/fr not_active Expired - Fee Related
-
2010
- 2010-03-23 CN CN201080017973.6A patent/CN102421530B/zh not_active Expired - Fee Related
- 2010-03-23 JP JP2012501342A patent/JP5661097B2/ja not_active Expired - Fee Related
- 2010-03-23 EP EP10726143.0A patent/EP2411155B1/fr active Active
- 2010-03-23 CA CA2756629A patent/CA2756629C/fr not_active Expired - Fee Related
- 2010-03-23 WO PCT/FR2010/000245 patent/WO2010109096A1/fr active Application Filing
- 2010-03-23 US US13/259,874 patent/US8541709B2/en not_active Expired - Fee Related
- 2010-03-23 KR KR1020117025345A patent/KR101736362B1/ko active IP Right Grant
- 2010-03-23 MY MYPI2011004604A patent/MY160936A/en unknown
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1574621A (fr) * | 1967-08-04 | 1969-07-11 | ||
DE2643002B1 (de) * | 1976-09-24 | 1977-11-10 | Kali & Salz Ag | Vorrichtung zur elektrostatischen aufladung und trennung von mineralstoffgemischen |
JPS5742355A (en) * | 1980-08-23 | 1982-03-09 | Senichi Masuda | Electrostatic separator |
US4627579A (en) * | 1983-08-05 | 1986-12-09 | Advanced Energy Dynamics, Inc. | Particle charging and collecting system |
EP0279200A2 (fr) * | 1987-02-17 | 1988-08-24 | Organ-Faser Technology Company N.V. | Procédé pour la séparation de parties en matériau électriquement non conducteur à partir d'ordure, en particulier de plastic et/ou papier et appareil à cet effet |
US5885330A (en) * | 1996-08-12 | 1999-03-23 | Lee; Jae Keun | Separation system and method of unburned carbon in flyash from a coal-fired power plant |
DE19912462A1 (de) * | 1998-08-19 | 2000-02-24 | Lehmann Maschf F B | Verfahren und Vorrichtung zur Trennung eines Bruchgutes |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU179023U1 (ru) * | 2017-12-25 | 2018-04-25 | Научно-производственная корпорация "Механобр-техника" (Акционерное общество) | Электростатический вибрационный сепаратор |
RU185261U1 (ru) * | 2018-09-13 | 2018-11-29 | Научно-производственная корпорация "Механобр-техника" (Акционерное общество) | Электростатический вибрационный сепаратор |
WO2024042205A1 (fr) | 2022-08-26 | 2024-02-29 | Skytech | Procédé de séparation d'un mélange de granules par effet triboélectrique |
FR3139016A1 (fr) | 2022-08-26 | 2024-03-01 | Skytech | Procédé de séparation d’un mélange de granules par effet triboélectrique |
Also Published As
Publication number | Publication date |
---|---|
CA2756629A1 (fr) | 2010-09-30 |
FR2943561A1 (fr) | 2010-10-01 |
FR2943561B1 (fr) | 2011-05-20 |
MY160936A (en) | 2017-03-31 |
CN102421530B (zh) | 2015-08-19 |
CN102421530A (zh) | 2012-04-18 |
EP2411155A1 (fr) | 2012-02-01 |
JP2012521866A (ja) | 2012-09-20 |
KR20120014130A (ko) | 2012-02-16 |
US20120085683A1 (en) | 2012-04-12 |
EP2411155B1 (fr) | 2019-06-26 |
CA2756629C (fr) | 2016-06-28 |
KR101736362B1 (ko) | 2017-05-16 |
JP5661097B2 (ja) | 2015-01-28 |
US8541709B2 (en) | 2013-09-24 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2411155B1 (fr) | Procédé de séparation électrostatique d'un mélange de granules de matériaux différents et dispositif de mise en oeuvre | |
CN112752621B (zh) | 对松散物料除尘的装置及方法 | |
US20130175371A1 (en) | Electric sorting by means of corona discharge | |
US4305797A (en) | Material separation by dielectrophoresis | |
EP3762148B1 (fr) | Procédé et dispositif de séparation électrostatique de matériaux granulaires | |
WO2020058847A2 (fr) | Procédé et installation de séparation aéraulique | |
WO2013153296A1 (fr) | Séparateur par courant de foucault | |
FR2951660A1 (fr) | Dispositif de traitement d'un granulat comprenant des composants en polymere lies a des composants metalliques et de composants en textile | |
WO2023083988A1 (fr) | Installation destinée à séparer dans un champ électrique les composants d'un mélange de fibres et de granules à l'aide d'un tribochargeur pourvu d'une grille de confinement sélectif desdits composants | |
FR3129095A1 (fr) | Procédé de séparation des composants d’un mélange de fibres et de granules par neutralisation électrostatique et tamisage, et installation correspondante | |
FR3129093A1 (fr) | Installation destinée à séparer dans un champ électrique les composants d’un mélange de fibres et de granules à l’aide d’un tribochargeur pourvu d’une grille de confinement sélectif desdits composants | |
EP3782734A1 (fr) | Dispositif de séparation électrostatique, procédé de séparation et utilisation associés | |
WO2024042205A1 (fr) | Procédé de séparation d'un mélange de granules par effet triboélectrique | |
FR2785551A1 (fr) | Dispositif de separation mecanique de sable a haute temperature present dans un courant de gaz | |
WO2022085665A1 (fr) | Procédé et appareil de séparation électrostatique | |
FR3101260A1 (fr) | Dispositif de charge électrostatique d’un mélange de granules, procédé et utilisation associés | |
KR102562603B1 (ko) | 에어 패들을 구비한 분진제거장치 | |
EP4051435B1 (fr) | Installation de traitement a tri densimetrique optimise et procede de traitement afferent | |
FR2635278A1 (fr) | Classificateur par gravite | |
JP2018140331A (ja) | 静電分離装置、及び静電分離方法 | |
RU71566U1 (ru) | Коронный электросепаратор | |
CN117505263A (zh) | 一种报废光伏组件拆解碎片的梯次分选设备及方法 | |
FR2931709A1 (fr) | Dispositif de purification d'un flux de gaz charge en particules solides. | |
FR2481640A1 (fr) | Appareil et procede d'epuration de granules plastiques utilises pour le moulage de lentilles optiques | |
JPS5926156A (ja) | 静電選別装置 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 201080017973.6 Country of ref document: CN |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 10726143 Country of ref document: EP Kind code of ref document: A1 |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2756629 Country of ref document: CA |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2012501342 Country of ref document: JP |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
ENP | Entry into the national phase |
Ref document number: 20117025345 Country of ref document: KR Kind code of ref document: A |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2010726143 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 13259874 Country of ref document: US |