Title of Invention

METHOD AND DEVICE FOR ISOLATING ALEURONE PARTICLES

Abstract

The invention relates to a method and device for separating a mixture (1), made of particles of a first particle type (2) and a second particle type (3), especially aleurone particles and shell particles made of comminuted bran, said particles being scarcely distinguishable in terms of size and density, into various types of particles (2, 3). Separation occurs according to particle-type specific tribo-electric charging of said particles in a first active area (13, 14; 27, 28) and subsequent separation of the differently charged moving particles in an electric field.

Full Text

The invention relates to a method and a device for separating the various sorts of particles in a mixture comprised of particles produced by comminuting the clays of cereal grains, in particular wheat, and are present as a mixture consisting of at least a first and second sort of particle, according to the preamble to claim 1 or 30. In addition, the invention relates to a product according to claim 51, which is also obtained via the method and device according to the invention. WO 85/04349 describes a method for obtaining aleurone cell particles from wheat clay, in this case, the clay particles are comminuted in a hammer mill in a first step, so that aleurone cell particles and shell particles are present as a mixture. This mixture is given an electrical charge through exposure to frictional electricity in a second step, wherein the aleurone cell particles and the shell particles receive different electrostatic charges. In a third step, the mixture with the differently charged particles is moved through an electrical field, so that the differently charged particles are varyingly deflected, wherein the shell particles and aleurone cell particles are caught in separate containers. The frictional electric charge (step 2) takes place in a stream of dry air, into which the mixture is introduced, and which moves in a hollow column. In this case, obviously turbulent air streams arise in the column ("elutriator"), wherein the particles in the mixture rub against both each other and the interior wall of the elutriator, thereby receiving the respective electrostatic charge. In this method of prior art, however, large quantities of air had to be moved. Nonetheless, no intensive frictional electric interaction takes place between the particles and the interior elutriator walls. Therefore, the object of the invention is to separate a mixture comprised of various sorts of particles, in particular aleurone and shell particles from comminuted clay, which hardly differ in terms of size and density, into its various sorts of particles more efficiently than in prior art. This object is achieved by means of the method according to claim 1, in which: a) The particles of the first particle sort and second particle sort in the mixture are moved along at least one surface of at least one solid material in a first impact area in such a way as that at least one portion of their particle surface is at least sectionally in contact with the solid material surface as they move along the at least one solid material surface, as a result of which the particles of the first particle sort and the particles of the second particle sort become electrically charged in such a way that the electrical charge of the particles of the first particle sort differs from the electrical charge of the particles of the second particle sort enough to enable an electrostatic separation of particles of the first particle sort from particles of the second particle sort; b) In a second impact area, the particles of the first particle sort and second particle sort with the sufficiently different electrical charges are subsequently moved into an electrical field between a first electrode area and a second electrode area, between which there is an electrical potential difference, at essentially the same velocity, as a result of which the particles of the first particle sort and second particle sort with the sufficiently different electrical charges move along sufficiently different paths as they travel through the electrical field; and c) The particles of the first particle sort and the particles of the second particle sort are caught at a first location and at a second location at the end of their journey through the electrical field, characterized in that the at least one surface of theleast one solid material is concave in the first impact area, and that the particles of the first sort and particles of the second sort in the mixture moving along the concave surface are pressed against the concave surface of the solid material as a result of their centrifugal force as they move inside the first impact area. The particles can be gather at this first and second location, and removed after enough have accumulated. As an alternative, they can also be continuously, e.g., pneumatically, conveyed further in step c) after separation in step b), and then be routed to a packaging system, for example. In particular, the particles of the first particle sort are aleurone particles, and the particles of the second particle sort are residual particles from which aleurone has been removed, in particular shell particles, of the comminuted clay. The object according to the invention is also achieved with the device according to claim 30, with. a) A first impact area with at least one surface of at least one solid material, along which the particles of the first particle sort and the second particle sort of the mixture can move in such a way that at least one portion of their particle surface is at least sectionally in contact with the solid material surface as they move along the at least one solid material surface; b) a second impact area subsequent to the first impact area, with a first electrode area and a second electrode area, between which an electrical voltage can be applied; and with a first accumulation area for particles of the first sort and an accumulation area for particles of the second sort separate from the first accumulation area, characterized in that the at least one surface of the at least one solid material is concave in the first impact area, so that the particles of the first sort and second sort that can move along the concave surface are pressed against the concave surface of the solid material as a result of their centrifugal force as they move inside the first impact area. In particular, the at least one surface of the at least one solid material is concave in the first impact area, so that the particles of the first sort and second sort that can move along the concave surface are pressed against the concave surface of the solid material as a result of their centrifugal force as they move inside the first impact area. The product according to the invention, In particular aleurone particles, which was obtained by separating the various particle sorts of the mixture through the use of steps a), b) and c) of the aforementioned method, has a high level of purity. It is preferably obtained through the repeated application of steps a), b) and c). Additional advantages, features and possible applications of the Invention will now be presented in the subclaims and the following description of two exemplary embodiments of the Invention based on the drawing, wherein: Fig. 1 shows a first exemplary embodiment of the Invention; and Fig. 2 shows a second exemplary embodiment of the invention. The first device according to the invention shown on Fig. 1 comprises a supply vessel 22 In which the mixture 1 to be separated, which contains at least a first particle sort 2 and a second particle sort 3, is routed to the first Impact area 13, 14, In which particles 2, 3 of mixture 1 are given an electrical charge varying by particle sort before the particles 2, 3 carrying different electric charges are supplied to the second treatment area 31, 32, 35, where they accumulate at different locations 33, 34 in a separation vessel 35, sorted according to type of particle based on their electric charge. Through the force of gravity, the mixture 1 goes out of the feed vessel 22, which tapers toward the bottom, into a conveyor device 18, 19 consisting of a conveyor screw 18 and into a conveyor channel 19. The conveyor screw 18, which is driven by a drive motor 23, conveys the mixture 1 through a product Inlet 15 into a housing 14, where a rotor element 13 is rotatably mounted. There is a gap area 21 between the rotor element 13, which is driven by a drive motor 24, and the housing 14, such that the mixture 1, which is supplied through the product inlet 15 and strikes the rotor element 13, is accelerated both radially and tangentlally through this gap area due to friction at the surface of the rotor element. The mixture 1 accelerated in this way passes through the gap area 21 and obliquely strikes the surface 11 of the inside wall of the housing, which has a concave curvature. Due to its own inertia (centrifugal force) and due to constantly resupplied mixture, the mixture 1 is pressed against the surface 11 having a concave curvature and is conveyed along this surface until it comes out of the housing 14 through the product outlet 16 and enters a separation vessel 35. The disk-shaped rotor element 13 has elevations 20, which are situated on its disk surface facing the product inlet 15. In addition to the above-mentioned friction on the surface of the rotor element 13 ("baffle disk"), these elevations 20 also contribute toward the acceleration of the mixture 1 and the ever-present air through the gap area 21, and on the other hand, they also exert an impact effect (baffle effect) on the particles 2, 3 of the mixture, so that any agglomerates of multiple particles which might be present are broken up. This impact separation (baffle separation) of agglomerates before or during the buildup of electric charge on the particles due to friction on the solid body surfaces is important, because such agglomerates may of course also consist of particles of different types, which would then reach the collecting site 33 or at the collecting site 34, depending on their total charge. Then, however, in any case one would have "foreign particles" at the respective collecting sites 33 and 34. Depending on their geometric shapes, these elevations 20 may have primarily an accelerating and/or pumping effect on the mixture and/or the air, or they may have primarily a dispersing effect on the particles of the mixture. A blocky, angular shape of these elevations 20 promotes a dispersing effect, while a paddle shape increases the acceleration or pumping effect. Elevations of different shapes may also be provided on the rotor element 13 to achieve a controlled effect. To prevent the mixture 1, which is supplied through the product inlet 15, from traveling even a very short distance through the gap area 21 between the product inlet 15 and the product outlet 16 and thereby escaping the necessarily intense action in the first treatment area 13, 14, the product inlet 15 is situated eccentrically with respect to the rotor element 13. In addition (and not for reasons of better illustration as in Fig. 1), the product inlet 15 is situated directly behind the product outlet 16 in the direction of rotation of the rotor element 13 peripherally, so that the mixture travels at least approximately 360° on a spiral pathway in the gap area 21 between the product inlet 15 and the product outlet 16. This prevents "short-circuiting" of the pathway of the mixture between the product inlet and the product outlet. During its path through the gap area 21, the particles 2, 3 of the mixture 1 come in intense contact with the inside surfaces 11, 12 of the housing 14 and with the surface of the rotor element 13, in particular its elevations 20 and the concave curvature of the inside surface 11 of housing 14. This leads to a specific electric charge buildup on the particles of the different types of particles 2, 3. Because of their high velocity, the dispersed particles coming out through the product outlet 16 go approximately horizontally into the separation vessel 35, whereby the cylindrical neck area 35a of the separation vessel serves as a calming zone for the particles carrying different electric charges as they come out of the housing 14. They then settle out in the interior of the separation vessel under the influence of gravity. In the interior of the separation vessel 35, there is a first electrode 31 and a second electrode 32 opposite it. The first electrode 31 is grounded by a line 38, which contains a voltage source 37, while the second electrode 32 is grounded directly via a line 39. The differently charged particles settling out in the electric field between the two electrodes 31 and 32 travel downward on different paths, depending on their electric charge. A partition 36, which projects from the bottom area 35b of the collecting vessel 35 into the electric field between the electrodes 31, 32 subdivides the lower interior space of the separation vessel 35 into a first collecting area 33 and a second collecting area 34 in which the particles of the first type and/or the particles of the second type are collected. In an advantageous modification of this first exemplary embodiment from Fig. 1, an air classification is also performed in the first treatment area 13, 14. To this end, air or another gas mixture is pumped through an air inlet (not shown) into the first treatment area 13,14 and is guided within the first treatment area 13, 14 so that the fines ("flour" from endosperm residues, optionally still adhering to the aleurone particles) are separated from the coarse fraction (pure aleurone particles and pure husk particles), the fines being removed with the air stream through an air outlet (not shown) and only the coarse fraction passing through the product outlet 16 into the second treatment area 31,32,35. The second device according to this invention as shown in Fig. 2 differs from that shown in Fig. 1 in its first treatment area. Otherwise all the elements are identical and carry the same reference notation as those in Fig. 1. Instead of the housing 14 with the rotor element 13 which is rotatably mounted on it and can be driven by the drive motor 24, the device in Fig. 2 has a curved channel with a first end 27a and a second end 27b. The mixture 1 coming from a feed vessel 22, in particular aleurone particles and husk particles of the bran, is supplied through a product inlet 15, and a moving fluid, in particular air, is supplied through a fluid inlet 29 to a fluidization area 17 at the end of which there is a dispersion angle 26, which is connected to the first end 27a of the curved channel 27 and through which the fluidization area 17 opens into the curved channel 27. The second end 27b of the curved channel 27 opens into a product separator 28 with a fluid outlet 30 and a product outlet 16, which opens into the separation vessel 35. The conveyor device 18, 19 transports the mixture 1 out of the feed vessel 22, through the product inlet 15 and into the fluidization area 17. A sufficient amount of fluid at a sufficient velocity is used to achieve airborne conveyance without any accumulation of particles in the interior of the curved channel 27. Due to the abrupt deflection when the particles impact on the dispersing angle 26, the above-mentioned dispersion/de-agglomeration of the particles of the mixture is accomplished. During their subsequent movement in the fluid stream and due to the friction between the particles moving along the inside surface of the curved channel 27, there is a particle type-specific buildup of electric charge on the particle types 2, 3 of mixture 1. The fluid is separated through the fluid outlet 30 in the downstream product separator 28, and the mixture of the differently charged particles according to type of particle then enters the separation vessel with its electric field. In principle, two cases of electric charging of the particles can be differentiated: The particles of the first type of particle are negatively (positively) charged and the particles of the second type of particle are negatively (positively) charged, but to a different extent. These particles thus differ only in the absolute value of their charge, but not in the polarity of the charge. The particles of the first type of particle are negatively (positively) charged and the particles of the second type of particle are positively (negatively) charged. The particles thus differ in polarity and possibly also in the absolute value of their charge. In the first case, the electrically charged particles of the first type and those of the second type repel one another, and there is practically no re-agglomeration of different particles. Separation takes place in the electric field due to different amounts of deflection in the same direction. In the second case, the electrically charged particles of the first type and those of the second type attract one another and re-agglomeration of different particles is possible. Separation takes place in the electric field due to different amounts of deflection in opposite directions. To prevent re-agglomeration of particles in any case before they are separated into the different types of particles in the electric field, the "particle densities" must be kept low and the "particle dwell times" must be kept short during the buildup of electric charge In the first treatment area accordingly. In the first exemplary embodiment in Fig. 1, this is accomplished because of the selected geometry due to the cross section of the gap area, which becomes wider in the radial direction, and due to a sufficiently high rotational speed of the rotor element 13. In the second exemplary embodiment in Fig. 2, this is accomplished by adjusting a sufficiently low product throughput/fluid throughput ratio in the fluidization area 17 and a sufficiently high fluid velocity. In all the exemplary emb odiments of the device according to this invention, the type of particle and the type of solid material on which the particles develop a triboelectric charge play a significant role whether the first case or the second case is obtained. Thus, for example, very good charge buildup and separation results would be achieved for an aleurone particle/husk particle mixture if the solid surfaces 11 and 12, which play a crucial role in the charge buildup, are made of stainless steel. List of Reference Notation 1 mixture of particles 2 first type of particle 3 second type of particle 11 first surface (concave) 12 additional surface 13, 14 first treatment area (first exemplary embodiment) 13 rotor element 14 housing 15 product inlet 16 product outlet 17 fluidization area 18, 19 conveyor device 18 conveyor screw 19 conveyor channel 20 elevation (baffle element, paddle element,.,.) 21 gap area 22 feed vessel 23 drive motor (for conveyor screw) 24 drive motor (for rotor element) 26 dispersing angle 27, 28 first treatment area (second exemplary embodiment) 27 curved channel 27a first end of 27 27b second end of 27 28 product separator 29 fluid inlet 30 fluid outlet 31,32, 35 second treatment area (first or second exemplary embodiment) 31 first electrode area 32 second electrode area 33 first location/collecting area 34 second location/collecting area 35 separation vessel 35a neck area 35b bottom area 36 partition 37 voltage source 38, 39 electric lines We Claim 1. A method for separating the various sorts of particles in a mixture comprised of particles produced by comminuting the clays of cereal grains, in particular wheat, and are present as a mixture (1) consisting of at least a first and second sort of particle, wherein a) the particles of the first particle sort (2) and the second particle sort (3) of the mixture are moved along at least one surface (11, 12) of at least one solid material in a first impact area (13, 14; 27, 28) in such a way as that at least one portion of their particle surface is at least sectionally in contact with the solid material surface (11, 12) as they move along the at least one solid material surface, as a result of which the particles of the first particle sort (2) and the particles of the second particle sort (3) become electrically charged in such a way that the electrical charge of the particles of the first particle sort differs from the electrical charge of the particles of the second particle sort enough to enable an electrostatic separation of particles of the first particle sort from particles of the second particle sort; b) In a second impact area (31, 32, 35), the particles of the first particle sort (2) and second particle sort (3) with the sufficiently different electrical charges are subsequently moved into an electrical field between a first electrode area (31) and a second electrode area (32), between which there is an electrical potential difference, at essentially the same velocity, as a result of which the particles of the first particle sort (2) and second particle sort (3) with the sufficiently different electrical charges move along sufficiently different paths as they travel through the electrical field; and c) The particles of the first particle sort (2) and the particles of the second particle sort (3) are caught at a first location (33) and at a second location (34) at the end of their journey through the electrical field, characterized in that the at least one surface (11) of the at least one solid material is concave in the first impact area (13, 14), and that the particles of the first sort (2) and particles of the second sort (3) in the mixture moving along the concave surface (11) are pressed against the concave surface of the solid material as a result of their centrifugal force as they move inside the first impact area. 2. The method according to claim 1, characterized in that the particles of the first particle sort (2) are aieurone particles, and the particles of the second particle sort (3) are residual particles from which the aieurone has been removed, in particular shell particles, of the comminuted clay (1). 3. The method according to one of the preceding claims, characterized in that the solid material is electrically conductive. 4. The method according to one of the preceding claims, characterized in that the surface of the solid material is sectionally electrically conductive and electrically nonconductive. 5. The method according to one of the preceding claims, characterized in that the solid material is electrically nonconductive. 6. The method according to claim 3 or 5, characterized in that the conductive solid material is grounded. 7. The method according to one of the preceding claims, characterized in that one of the electrode areas (31, 32) is grounded such that the first electrode 31 is grounded by a line 38, which contains a voltage source 37, while the second electrode 32 is grounded directly via a line 39. 8. The method according to claim 6 and/or 7, characterized in that the conductive solid material and one of the electrode areas (31, 32) are additionally interconnected in an electrically conductive manner to facilitate the movement of differently charged particles field between the two electrodes 31 and 32 downward on different paths, based on their electric charge. 9. The method according to one of the preceding claims, characterized in that the solid material is a metal or a metal alloy, in particular stainless special steel. 10. The method according to one of the preceding claims, characterized in that the particles of the first sort (2) and the particles of the second sort (3) of the mixture (1) are moved inside the first impact area (13, 14) in the presence of a nonconductive fluid. 11. The method according to one of the preceding claims, characterized in that the particles of the first sort (2) and the particles of the second sort (3) of the mixture (1) are moved inside the first impact area (13, 14) by means of a fluid stream such that at least one portion of their particle surface is at least sectionally in contact with the solid material surface as they move along the at least one solid material surface. 12. The method according to one of the preceding claims, characterized in that the particles of the first sort (2) and the particles of the second sort (3) of the mixture (1) are moved inside the first impact area (13, 14) against a fluid stream such that that the particles of the first sort and particles of the second sort in the mixture moving along the concave surface are pressed against the concave surface of the solid material as a result of their centrifugal force as they move inside the first impact area. 13. The method according to one of the preceding claims, characterized in that the fluid has nitrogen and/or carbon dioxide. 14. The method according to claim 13, characterized in that the fluid is air. 15. The method according to one of the preceding claims, characterized in that the relative velocity between the at least one surface (11, 12) and the particles (2, 3) moved along it measures about 5 m/s to 25 m/s. 16. The method according to claim 14 or 15, characterized in that the relative atmospheric moisture of the used air lies under 25 %. 17. The method according to one of the preceding claims, characterized in that the mixture (1) comprised of the particles (2, 3) has a humidity content of less than 10 %. 18. The method according to one of the preceding claims, characterized in that the particles of the mixture (1) are predominantly smaller than 500 µm, and preferably larger than 100 µm. 19. The method according to one of claims 10 to 18, characterized in that the first impact area is designed such that the mixture having particles of the first sort and particles of the second sort is moved with essentially no electrical charge through the product inlet, and carried by the fluid stream supplied through the fluid inlet and discharged through the fluid outlet in turbulent motions through the first impact area and along its concave surface, and finally routed through the product outlet with the particles in their respective electrically charged state into the second impact area. 20. The method according to one of claims 10 to 18, characterized in that the first impact area is designed such that the mixture having particles of the first sort and particles of the second sort is supplied by a conveying device in the supply area via the product inlet to the first impact area in such a way that the particles of the first sort and particles of the second sort each assume a first partial charge of their respective final electrical charge in the supply area, and wherein the mixture of partially charged particles are carried by the fluid stream supplied through the fluid inlet and discharged through the fluid outlet in turbulent motions through the cyclone area and along its concave surface, so that the particles of the first sort and particles of the second sort each assume a second partial charge of their final electrical charge, and are finally routed through the product outlet into the second impact area. 21. The method according to one of claims 10 to 18, characterized in that the first impact area (13, 14) has pivoted in a casing (14) a rotor element (13), which is shaped in such a way that, when turned, the particles (2, 3) of the mixture (1) contained in the first impact area (13, 14) are accelerated through the surface (12) of the rotating rotor element (13) with a radial and tangential component, and are relayed to the concave inner surface (11) of the casing (14) at a velocity with a radial and tangential component. 22. The method according to claim 21, characterized in that elevations (20) project into a gap area (21) between the rotor element (13) and casing (14) through which passes the moving particle current, and extend from the surface (12) of the rotor element and/or from the inner wall of the casing to disperse any agglomerates that might have formed between the particles of the mixture. 23. The method according to one of claims 10 to 18, characterized in that the first impact area has a curved channel (27) with a first end and a second end, in which a product inlet empties out in the first end, and a product separator (28) with a product outlet and fluid outlet is secured to the second end for separating the product and fluid, wherein the mixture having particles of the first sort and particles of the second sort is supplied through the product inlet, and carried by a fluid stream supplied through the fluid inlet and discharged through the fluid outlet through the first impact area with the curved channel and along its concave surface, and is finally routed through the product separator and its product outlet into the second impact area with the particles in their respective electrically charged state. 24. The method according to claim 23, characterized in that the curved channel (27) is a curved hose or bent tube. 25. The method according to claim 23 or 24, characterized in that the curved channel (27) is spiral or helical. 26. The method according to one of claims 10 to 25, characterized in that the mixture having the electrically charged particles is discharged from the first impact area (13, 14; 27, 28) into the second impact area (31, 32. 35) by means of gravitational forces and/or centrifugal forces and/or a fluid stream. 27. The method according to one of the preceding claims, characterized in that any agglomerates that might have been formed out of particles of the first sort and particles of the second sort are dispersed prior to entering into or within the first impact area. 28. The method according to claim 27, characterized in that potential agglomerates are dispersed prior to entering the first impact area or within the first impact area through impact. 29. The method according to claim 27 or 28, characterized in that the first impact area is formed via the series-parallel connection of various devices and consisting of an impact disperser and a cyclone separator. 30. A device for separating the various sorts of particles in a mixture comprised of particles produced by comminuting the clays of cereal grains, in particular wheat, and are present as a mixture (1) consisting of at least a first and second sort of particle, using the method according to one of claims 1 to 29, with a first impact area (13, 14; 27, 28) with at least one surface (11, 12) of at least one solid material, along which the particles of the first particle sort (2) and the second particle sort (3) of the mixture can move in such a way that at least one portion of their particle surface that moves along at least one solid material surface is at least sectlonally in contact with the solid material surface (11, 12); and a second impact area (31, 32, 35), with a first electrode area (31) and a second electrode area (32), between which an electrical voltage can be applied; and with a first accumulation area (33) for particles of the first sort (2) and an second separate (36) accumulation area (34) for particles of the second sort (3), characterized in that at least one surface (11) of at least one solid material is concave in the first impact area (13,14; 27, 28), such that the particles of the first sort (2) and second sort (3) that can move along the concave surface (11) inside the first impact area are pressed against the such surface as a result of their centrifugal force. 31. The device according to claim 30, characterized in that the first impact area is designed as a cyclone separator with a fluid inlet, an fluid outlet, a product inlet and a product outlet. 32. The device according to one of claims 30 or 31, characterized in that it has a supply area through which the mixture having particles of the first sort and particles of the second sort can be supplied to the first impact area (13, 14; 27, 28) by means of a conveying device (18, 19) in the supply area via the product inlet. 33. The device according to one of claims 30 to 31, characterized in that the first impact area (13, 14) has pivoted in a casing (14) a rotor element (13), which is shaped in such a way that, when turned, the particles (2, 3) of the mixture (1) contained in the first impact area (13, 14) can be accelerated through the surface (12) of the rotating rotor element (13) with a radial and tangential component, and relayed to the concave inner surface (11) of the casing (14) at a velocity with a radial and tangential component. 34. The device according to claim 33, characterized in that elevations (20) project into a gap area (21) between the rotor element (13) and casing (14) through which can pass the moving particle current, and extend from the surface (12) of the rotor element and/or from the inner wall of the casing, so that any agglomerates that might be contained in the mixture are dispersed before it is routed to the concave inner surface. 35. The device according to one of claims 30 to 34, characterized in that the first impact area (13, 14) is designed to function as a centrifugal device, containing a rotor element which is an impact plate (13) with numerous elevations (20). 36. The device according to claim 35, characterized in that a product inlet (15) is arranged at a location of the casing (14) that is eccentric relative to the impact plate (13), so that loading takes place eccentrically on the impact plate in the casing. 37. The device according to claim 33 to 36, characterized in that an air pump or a compressor is hooked up to the first impact area (13, 14) in order to pump a fluid in the first impact area (13, 14) in the direction counter to the centrifugally accelerated particle current. 38. The device according to claim 33 to 36, characterized in that an air pump or a compressor is hooked up to the first impact area (13, 14) in order to pump a fluid in the first impact area (13, 14) in the same direction as the centrifugally accelerated particle current. 39. The device according to one of claims 34 to 38, characterized in that the impact plate (13) bears angular elevations (20) in its radially outer edge area. 40. The device according to one of claims 34 to 38, characterized in that the impact plate (13) bears web-like elevations (20) from its centre to the edge area. 41. The device according to one of claims 34 to 40, characterized in that all elevations (20) are formed on the at least one impact plate (13). 42. The device according to one of claims 34 to 38, characterized in that the elevations (20) formed on the at least one impact plate (13) are designed as turbine blades. 43. The device according to claim 30, characterized in that the first impact area (27, 28) has a curved channel (27) with a first end (27a) and a second end (27b), in which a product inlet (15) and fluid inlet (29) is connected to the first end, and a product separator (28) with a product outlet (16) and fluid outlet (30) is secured to the second end for separating the product and fluid, wherein the mixture having particles of the first sort and particles of the second sort can be supplied through the product inlet (15), carried by a fluid stream supplied through the fluid inlet (29) and discharged through the fluid outlet (30) through the first impact area with the curved channel (27) and along its concave surface, and finally routed through the product separator (28) and its product outlet (16) into the second impact area (31, 32, 35) with the particles in their respective electrically charged state. 44. The device according to claim 43, characterized in that a dispersing angle (26) against which the particles of the mixture transported through the device collide during their reversal of movement is arranged upstream from the curved area of the curved channel (27), so that any agglomerates that might be contained in the mixture are dispersed before being transported further to the curved channel. 45. The device according to one of claims 32 to 44, characterized in that the supply area of the conveying device (18, 19) has a conveyor worm (18) with which the particles of the first sort and particles of the second sort can be supplied to the first impact area (13, 14; 27, 28), wherein the particles receive their respective electrostatic charge by rubbing against the surface of the conveyor worm while supplying the first partial charge. 46. The device according to claim 30, characterized in that the first impact area is a hammer mill or an impact crusher, 47. The device according to claim 30, characterized in that the first impact area has a non- clogging air separator or a turbo-mill. 48. The device according to one of claims 30 to 47, characterized in that, in the second impact area (31, 32, 35), the first electrode area consists of a first electrode (31), and the second electrode area consists of a second electrode (32). 49. The device according to one of claims 30 to 47, characterized in that the first electrode and second electrode in the second impact area (31, 32, 35) are arranged like a plate capacitor. 50. The device according to one of claims 30 to 47, characterized in that the first electrode and second electrode in the second impact area (31, 32, 35) are arranged like a cylinder capacitor.

Documents:

1001-chenp-2004-claims filed.pdf

1001-chenp-2004-claims granted.pdf

1001-chenp-2004-correspondnece-others.pdf

1001-chenp-2004-correspondnece-po.pdf

1001-chenp-2004-description(complete) filed.pdf

1001-chenp-2004-description(complete) granted.pdf

1001-chenp-2004-drawings.pdf

1001-chenp-2004-form 1.pdf

1001-chenp-2004-form 19.pdf

1001-chenp-2004-form 26.pdf

1001-chenp-2004-form 3.pdf

1001-chenp-2004-form 5.pdf

1001-chenp-2004-pct.pdf