Separation device for cleaning contaminated bulk material

Abstract

Separation device (1) for cleaning contaminated bulk material (2), preferably plastic bulk material, in particular recyclate (3), comprising: a cleaning chamber (4) with a preferably at least partially conically shaped inlet area (5); an inlet nozzle (14) leading into the inlet area (5); and an outlet opening (16) which can preferably be closed by a flap (17), wherein the separation device (1) is designed to be operated in a conveying sequence in which the contaminated bulk material (2) is conveyed through the inlet nozzle (14) into the inlet region (5) by suction, in an optional emptying sequence in which a fluid, in particular air, is sucked in through the inlet nozzle (14), and in an emptying sequence in which cleaned bulk material (2) is discharged through the outlet opening (16), wherein the conveying sequence and preferably the optional emptying sequence form a conveying phase, characterized in that the cleaning chamber (4) has a preferably at least partially conically shaped circulation region (6) and the inlet region (5) and the circulation region (6) are arranged and designed such that the contaminated bulk material (2) is conveyed from the inlet region into the circulation region (6) by suction during the conveying phase during operation of the separating device (1) and is continuously circulated in the circulation region (6) by suction until the emptying sequence and is thereby cleaned, wherein contaminants (24) which are detached from the contaminated bulk material (2) can be sucked out of the circulation region (6) by sucking in the contaminated bulk material (2) during the conveying phase via a suction opening (20).

Description

[0001] The invention relates to a separating device for cleaning contaminated bulk material, comprising: a cleaning chamber with an inlet area that is preferably at least partially conically shaped; an inlet nozzle leading into the inlet area; and an outlet opening that can preferably be closed by a flap, wherein the separation device is configured to be operated in a conveying sequence in which the contaminated bulk material is conveyed through the inlet nozzle into the inlet region by suction, in an optional emptying sequence in which a fluid, in particular air, is sucked in through the inlet nozzle, and in an emptying sequence in which cleaned bulk material is discharged through the outlet opening, wherein the conveying sequence and preferably the optional emptying sequence form a conveying phase.

[0002] Recycled plastic material is increasingly being used in the manufacture of plastic products, but this material can be contaminated with dust and fines. Contamination can arise, among other things, when the recycled plastic material is cut in cutting mills. Dust and fines can lead to quality problems during the manufacture of plastic products. For example, coking can occur when the plastic material is melted. Furthermore, fines in the plastic material exhibit different melting behavior than the actual plastic material, resulting in an irregular distribution in the plastic melt and, in some cases, streaks in the finished plastic product. Before the recycled plastic material can be further processed by plastic processing machines, it must therefore be cleaned to ensure compliance with quality specifications.

[0003] Material separators of the type mentioned above are known from the prior art. In these separators, an extraction module extracts dust and fine particles from a passing plastic material over a short distance of typically less than 300 mm. After the plastic material has passed through the extraction module, it lands in a container. Due to the relatively short distance along which contaminants from the passing plastic material are extracted, the plastic material is not completely cleaned and still contains high levels of dust and fine particles. To achieve a higher degree of cleaning, the process would have to be repeated several times, which can lead to increased effort or reduced material throughput, particularly in tightly timed manufacturing processes.

[0004] WO 03 / 037534 A1 discloses a method and device for cleaning or separating lighter material, such as dust, from heavier granules. The contaminated granules are introduced via an inlet nozzle and conveyed via a deflection pipe into an inlet area of ​​the cleaning chamber. The contaminated granules are conveyed upwards into a conically tapered hopper section. The first heavy components of the granules fall to the bottom. Lighter, still at least partially contaminated granules continue upwards into an upper chamber area, where a distribution plate device is located. There, the remaining granules to be cleaned are deflected several times and transported even further upwards. Successively heavier, slowed-down parts of the granules fall to the bottom, while lighter components, such as dust, are sucked upwards. The dust ultimately exits the separation device through an opening at the very top.The cleaned granulate collects in the lower area and is discharged through an outlet opening of the separator.

[0005] In light of these statements, the object of the present invention is to at least partially alleviate the disadvantages of the prior art. Preferably, the object of the present invention is to provide a separation device of the type mentioned above, which enables improved cleaning of bulk material. Preferably, the time required for cleaning the bulk material should not be prolonged.

[0006] This object is achieved by a separation device according to claim 1. A plant for producing a plastic product is defined in claim 14.

[0007] The invention is described below using a method for cleaning contaminated bulk material. The features, effects, and advantages described in connection with the method apply analogously to the separation device or can be transferred to the separation device in a corresponding manner.

[0008] A method for cleaning contaminated bulk material, which can be carried out with a separator, comprises the following steps: i) sucking in the contaminated bulk material via an inlet nozzle of the separation device and thereby conveying the contaminated bulk material into a preferably at least partially conically shaped inlet area of ​​the cleaning chamber during a conveying sequence; ii) sucking in a fluid, in particular air, through the inlet nozzle during an optional emptying sequence following the conveying sequence, in particular to empty the inlet nozzle and a suction line of possible residues of the contaminated bulk material, wherein the conveying sequence and preferably the optional emptying sequence form a conveying phase; and iii) Discharge of the cleaned bulk material through an outlet opening during a discharge sequence after completion of the conveying phase.

[0009] In such a method, the contaminated bulk material is conveyed by suction during the conveying phase from the inlet region into a preferably at least partially conically shaped circulation region of the cleaning chamber. In the circulation region, the contaminated bulk material is continuously circulated by suction until the emptying sequence and is thereby cleaned. Contaminants that detach from the contaminated bulk material are suctioned out of the circulation region by suctioning the contaminated bulk material during the conveying phase via a suction opening. Advantageously, the continuous circulation during the conveying sequence and the optional emptying suction sequence thoroughly cleans the bulk material in the circulation region without extending the overall duration of the cleaning cycle, consisting of the conveying sequence, optional emptying suction sequence, and emptying sequence.This allows the process and separation device to be integrated into an existing system without the need for complex modifications. The circulation is achieved by suctioning in the bulk material. The suction of the bulk material is preferably achieved by creating a vacuum or negative pressure. In one embodiment, the optional suction of the fluid can also be achieved by a vacuum or negative pressure. The circulation facilitates the separation of dust and fine particles from the bulk material to be cleaned, allowing them to be subsequently suctioned away. In contrast to the prior art, the bulk material is cleaned throughout the entire conveying phase and thus over a longer period of time.Bulk material conveyed into the separation device therefore does not simply remain there while further material flows in during the conveying sequence or while a fluid, in particular air, is sucked in during the optional emptying sequence, but is constantly circulated until the emptying sequence and is thus cleaned of dust and fine particles. The conveying sequence, the optional emptying sequence and the emptying sequence together form a cleaning cycle within which a specific quantity of bulk material is cleaned and discharged. The bulk material is preferably a plastic bulk material, in particular recycled plastic bulk material, also known as recyclate. The plastic bulk material can consist of petroleum-based polymers or biopolymers, for example. The bulk material can be in the form of granules, grains, shreds, pieces of film or powder, for example.The separation device has a cleaning chamber into which the bulk material is sucked and in which the bulk material is subsequently cleaned. The cleaning chamber is preferably designed to be substantially rotationally symmetrical. The cleaning chamber can have, at least in sections, a cylindrical almond-shaped outer wall. The inlet area and the circulation area are arranged within the cleaning chamber. The circulation area and the inlet area can be spatially separated from one another, for example by a wall. Multiple circulation areas and / or inlet areas can also be provided. If multiple circulation areas and / or inlet areas are provided, these can also be spatially separated from one another, for example by a wall. The cleaning chamber can be made at least partially of transparent material in order to allow a view into the inlet area and the circulation area.The circulation region is preferably arranged at least partially above the inlet region. The circulation region can, for example, have a volume of 1 l to 80 l. The inlet region can, for example, have a volume of 0.5 l to 20 l. In step i), the contaminated bulk material is sucked in via an inlet nozzle of the separation device during the conveying sequence and thereby conveyed into an inlet region of the cleaning chamber. The suction takes place by generating a negative pressure. The bulk material can, for example, be contaminated with finely divided, in particular fine-grained, or powdery particles. During the conveying phase, mainly bulk material, but also fluid, in particular air, is sucked in. The inlet region can be at least partially conical in shape.The contaminated bulk material can be stored in a reservoir outside the cleaning chamber and sucked in from there, for example via a suction line, in particular a pipe or a hose. A dosing device, for example a flap or a valve, can be configured to release only a specific quantity of accumulated contaminated bulk material during the conveying sequence for suction into the inlet area. The inlet nozzle can be arranged, for example, parallel or at right angles to a tangential circumferential direction of the cleaning chamber. In general, the inlet nozzle can be arranged at any angle to the outer wall of the cleaning chamber, as long as the supply of bulk material is permitted. In the inlet area, the sucked-in contaminated bulk material can be at least partially separated by swirling.The inlet area is preferably at least partially conical in shape in order to direct the flow of contaminated bulk material. Due to an at least partially conical shape, the bulk material can be guided along the inner wall of the inlet area and partially swirled and slowed down, as a result of which the first dust and fine particles can already be released. In order to clear the inlet nozzle and the suction line of any bulk material that may have remained, so that this does not fall back and lead to blockages in the suction line or the suction nozzle, it is optionally provided in step ii) that a fluid, in particular air, is sucked in during an optional emptying sequence following the conveying sequence. In the emptying sequence, no new bulk material is removed or sucked in from the reservoir of contaminated bulk material, but at most only residues in the suction line orin the intake port by suction of the fluid into the inlet area. Ambient air can in particular serve as the sucked-in fluid. During the conveying sequence and preferably the optional emptying suction sequence, which together form the conveying phase, according to the invention the contaminated bulk material is sucked in and thereby conveyed from the inlet area into a circulation area of ​​the cleaning chamber. If no emptying suction sequence is provided, the conveying phase is formed solely by the conveying sequence. An emptying suction sequence can be dispensed with, for example, in the case of short suction line lengths. The circulation area can be at least partially conical in shape. Bulk material can already reach the circulation area during the conveying sequence. The vast majority of the bulk material is sucked into the circulation area during the optional emptying suction sequence at the latest.By sucking in fluid during the conveying phase, essentially all of the bulk material in the inlet area is conveyed into the circulation area. Only small residues can remain in the inlet area. During the conveying phase, the bulk material is continuously circulated and thus cleaned within the circulation area by suction. Circulation is preferably achieved by an upwardly directed suction fluid flow, which draws the bulk material upwards, from where it is displaced by following bulk material and falls back down. The circulation loosens dust and fine particles, which can then be suctioned off. To ensure that no bulk material is sucked off with the dissolved impurities, a grid, preferably a particularly replaceable wire sieve, can be provided whose opening width is smaller than, for example, the smallest granulate size suitable for subsequent plasticizing.The opening width defines the boundary between bulk material and dust or fine particles. The opening width refers to the maximum diameter of a grid opening. The strength of the intake fluid flow can be selected such that the bulk material is not sucked onto the grid the entire time until the discharge sequence and no longer detaches. The intake fluid flow can be a substantially constant fluid flow, for example, a fluid flow with a strength between 50 m and 100 m. 3 / h and 400 m 3 / h, preferably between 100 m 3 / h and 300 m 3 / h, with an example of essentially 200 m 3 / h. The strength of the intake fluid flow can depend, among other things, on the type of bulk material and the length and cross-section of the intake line. While the bulk material is circulated, contaminants that detach from the contaminated bulk material are sucked away. The intake of the bulk material or the suction of the contaminants is preferably carried out by the same suction device, which can be connected in particular in the circulation area. The suction or suction creates a fluid flow from the intake nozzle and any connected suction line via the inlet area into the circulation area and from there to the suction device.In step iii), the conveying phase, consisting of the conveying sequence and preferably the optional emptying suction phase, is ended by completely deactivating or reducing the suction and extraction, and the emptying sequence is started, in which the cleaned bulk material is discharged through an outlet opening. The cleaned bulk material can, for example, be fed directly or indirectly via a further process step or further cleaning to a plastics processing machine, such as an injection molding machine or extrusion line. The outlet opening can be closable. After the emptying sequence has ended, the cleaning cycle can begin again by sucking in heaped bulk material from the reservoir in the conveying sequence. Preferably, steps i-iii) are carried out in the specified order. The emptying suction sequence can, for example, last between 0 s and 180 s.For example, the pumping sequence can last between 1 s and 120 s. The emptying sequence can last between 1 s and 30 s.

[0010] Directional and locational information in this disclosure refers to the intended use of the cleaning chamber. Preferably, the circulation area is arranged at least partially above the inlet area.

[0011] It is preferred if the suction opening is provided on the top side of the cleaning chamber, and a suction device is connected to the suction opening, which suctions in the bulk material and removes the contaminants during the conveying phase. The suction opening is preferably arranged at the top side of the circulation area, so that an upward fluid flow is created in the circulation area during the conveying sequence and the optional emptying sequence. The suction device can be formed, for example, by a compressor. Suctioned-off contaminants can be collected, for example, in a container or a bag.

[0012] In one embodiment, it can be provided that the outlet opening is arranged on an underside of the cleaning chamber and the cleaned bulk material falls downwards through the outlet opening due to gravity during the emptying sequence, preferably wherein the outlet opening can be closed by a flap during the conveying phase. The outlet opening can in particular be arranged on the underside of the inlet region. During the emptying sequence, the suction is deactivated or reduced to such an extent that the cleaned bulk material falls downwards through the outlet opening due to gravity. The optional flap can be opened for this purpose. It is preferred if the flap is closed during the conveying phase, in particular essentially hermetically closed.

[0013] It is advantageous if, after being sucked into the inlet area during the conveying sequence, the contaminated bulk material is decelerated by the inner wall of the inlet area, preferably with the bulk material moving essentially in the manner of a screw thread tapering downwards or upwards. Contact of the bulk material with the inner wall of the inlet area decelerates the bulk material through friction and shakes it, allowing initial contaminants to be released. A tapered shape of the inlet area allows the bulk material to be moved in the manner of a screw thread tapering downwards or upwards, allowing the bulk material to be transferred in a targeted manner to the circulation area.

[0014] In one embodiment, the circulation area has an inlet opening, particularly on the underside, which is preferably arranged below the inlet nozzle, so that the bulk material is first sucked downwards to the inlet opening in the inlet area during the conveying phase and then sucked upwards into the circulation area. The inlet opening can also be arranged laterally on the circulation area. However, if the inlet opening is arranged on the underside, this has the advantage that cleaned bulk material can simply fall downwards during the emptying sequence and can thus more easily escape from the circulation area.

[0015] It is particularly preferred if the contaminated bulk material is circulated in the circulation area by being sucked in from above, displaced radially outward by following contaminated bulk material, falling downward, and then being sucked in again from above. For this purpose, the suction device can be connected to an upper side of the circulation area.

[0016] To clean a large quantity of bulk material, it is advantageous if the conveying phase and the discharge sequence form a single cleaning cycle, and several cleaning cycles are performed consecutively. In each cleaning cycle, new, contaminated bulk material can be drawn in from a reservoir. The cleaning cycles can all have the same duration.

[0017] To clean contaminated bulk material, at least one additional separation device can be provided, which is connected in parallel to the separation device and also cleans contaminated bulk material according to steps i)-iii) as described above using the method. The additional separation device can be constructed in a similar way, in particular identically, to the separation device. The additional separation device can perform the same process as the separation device.

[0018] Also disclosed is a method for producing a plastic product comprising the following steps: (a) cleaning contaminated bulk material using a method for cleaning contaminated bulk material as described above; b) feeding the cleaned bulk material to a plastics processing machine, in particular an injection moulding machine or extrusion line; c) Production of a plastic product by the plastic processing machine.

[0019] After cleaning the contaminated bulk material, intermediate storage, a further process step, or further cleaning may be required. The plastic product could, for example, be a part for the interior of an automobile, a packaging container, a toy, or a window profile.

[0020] The object of the invention is achieved by a separation device of the type mentioned at the outset, in which it is provided that the cleaning chamber has a preferably at least partially conically shaped circulation region and the inlet region and the circulation region are arranged and designed such that the contaminated bulk material is conveyed from the inlet region into the circulation region by suction during the conveying phase during operation of the separation device and is continuously circulated in the circulation region by suction until the emptying sequence and is thereby cleaned, wherein contaminants which detach from the contaminated bulk material can be sucked out of the circulation region by sucking in the contaminated bulk material during the conveying phase via a suction opening.The separation device according to the invention is preferably designed to carry out the above-described method for cleaning contaminated bulk material. The advantages and features described in connection with the method for cleaning contaminated bulk material are therefore transferable to the separation device according to the invention. The inlet region and the circulation region can be spatially separated from one another, in particular by a wall. The separation device is preferably designed as a vacuum conveying separation device. The separation device preferably has a device for generating a vacuum or negative pressure or is, for example, connected to such a device. With the aid of the vacuum or negative pressure, the bulk material or optionally the fluid can be conveyed through the separation device.

[0021] In one embodiment, the suction opening is arranged on an upper side of the cleaning chamber, in particular on an upper side of the circulation area, and is designed as a connection for a suction device. The suction device can be connected to the suction opening via a hose or a pipe. Alternatively, the suction device can be connected directly to the suction opening.

[0022] It is advantageous if the outlet opening is arranged on a bottom side of the cleaning chamber and the cleaned bulk material falls downwards through the outlet opening due to gravity in the emptying sequence, preferably wherein the outlet opening can be closed by a flap in the conveying phase.

[0023] To prevent the bulk material from being sucked out, a grid can be provided in the circulation area, preferably on an upper side of the circulation area. The grid can, in particular, be arranged horizontally in the circulation area. Depending on the design of the separation device, other grid arrangements, such as an inclined or vertical arrangement, are also possible. The grid preferably extends substantially over the entire cross-sectional area of ​​the circulation area. The grid can be a wire sieve. The grid is preferably designed to be replaceable.

[0024] The grid can, for example, have an opening width of 0.2 mm to 5 mm, in particular 0.5 mm to 3 mm.

[0025] In one embodiment, it can be provided that the circulation area preferably has an inlet opening on the underside through which the contaminated bulk material enters the circulation area. The inlet opening is arranged in particular below the inlet nozzle, so that the bulk material can be sucked into the inlet area during the conveying phase, preferably downwards toward the inlet opening, and then upwards into the circulation area. By arranging the inlet opening on the underside, cleaned bulk material can advantageously be conveyed out of the circulation area due to gravity during the emptying sequence.

[0026] It is preferred if an inlet pipe is connected to the circulation area, with the inlet opening located at the end of the inlet pipe facing the underside of the cleaning chamber. The inlet pipe can, for example, have a length of 40 mm to 550 mm. The inlet pipe can, for example, have a diameter of 30 mm to 80 mm. The inlet pipe preferably has a round cross-section.

[0027] It has proven particularly advantageous if the cross-sectional area of ​​the inlet opening is between 50% and 130%, preferably between 60% and 120%, of the cross-sectional area of ​​the inlet nozzle. Alternatively, the cross-sectional area of ​​the inlet opening can be substantially equal to the cross-sectional area of ​​the inlet nozzle.

[0028] It is advantageous if the separating device is designed to circulate the contaminated bulk material in the circulation area by sucking the contaminated bulk material from above, displacing it radially outwards by following contaminated bulk material, falling downwards and then being sucked in again from above.

[0029] In one embodiment, it can be provided that the conveying phase and the emptying sequence form a cleaning cycle, and the separating device is designed to carry out several cleaning cycles in succession.

[0030] To facilitate the flow of bulk material into the circulation area, the inlet area and the circulation area can be arranged to at least partially overlap, viewed in the cross-section of the cleaning chamber and along a longitudinal axis of the cleaning chamber. In other words, there is a section along the longitudinal axis of the cleaning chamber in which both the inlet area and the circulation area are located.

[0031] To guide the material and fluid flow, it is advantageous if, viewed in the cross-section of the cleaning chamber, the inlet area and the circulation area each have a conical section, and if, in the inlet area, a channel for the contaminated bulk material is formed between the conical sections of the inlet area and the circulation area. The conical section of the circulation area promotes the circulation of the bulk material.

[0032] In one embodiment, the inlet nozzle is arranged at the level of the conically converging section of the circulation area, viewed in the cross-section of the cleaning chamber. This advantageously guides the flow of contaminated bulk material into the inlet area.

[0033] Also disclosed is a plant for producing a plastic product, which comprises: a suction device; a separation device as described above, connected to the suction device; a plastics processing machine, in particular an injection molding machine or extrusion line, which is connected to the separation device.

[0034] The contaminated bulk material can be transported to the separation device and from the separation device to the plastics processing machine, particularly via hoses or pipes. The plastics processing machine can produce, for example, parts for automotive interiors, packaging containers, toys, or window profiles.

[0035] The invention is described below using a specific embodiment, to which it is not intended, however, to be limited.

[0036] They show: Fig. 1 a separator in cross section; Fig. 2 the separator in a conveying phase in cross-section; and Fig. 3 the separator in a discharge sequence in cross section.

[0037] Fig. 1 shows a separating device 1 for cleaning contaminated bulk material 2 (see Fig. 2 and Fig. 3). The bulk material 2 can, for example, be a recycled plastic material, called recyclate 3. In particular, the bulk material is plastic granulate. The separation device 1 has a cleaning chamber 4, which is divided into an inlet area 5 and a circulation area 6. In the illustration shown, the circulation area 6 is arranged at least partially above the inlet area 5. However, viewed along the axis of symmetry 7, there is an overlap area 8 in which both the inlet area 5 and the circulation area 6 are arranged at the same height along the longitudinal axis 7. In the illustration shown, the axis of symmetry 7 also forms the longitudinal axis of the cleaning chamber 4. The inlet area 5 and the circulation area 6 are spatially separated from one another by a wall 9, except for an inlet opening 13, which will be described in more detail later. The wall 9 can be designed to be removable.Both the inlet region 5 and the circulation region 6 each have a conically tapered section 10a, 10b on their underside. The conically tapered section 10b can form the wall 9. Above the conically tapered sections 10a, 10b, the inlet region 5 and the circulation region 6 each have preferably straight wall sections 11a, 11b. The wall sections 11a, 11b are formed by the outer wall 11 of the cleaning chamber. The conically tapered section 10b of the circulation region 6 opens into an inlet pipe 12, on the underside of which an inlet opening 13 is provided. Bulk material 2 can pass from the inlet region 5 into the circulation region 6 and vice versa through the inlet opening 13 and the inlet pipe 12.

[0038] The cleaning chamber 4 further comprises an inlet nozzle 14, which, in the illustration shown, is arranged substantially perpendicular to the longitudinal axis 7 and opens into the inlet region 5. The inlet nozzle 14 can be connected to a reservoir (not shown) of contaminated bulk material 2 via a suction line 15, indicated by the dotted lines.

[0039] On the underside 50 of the cleaning chamber 4, i.e., also on the underside of the inlet area 5, an outlet opening 16 is provided, which can be closed with a flap 17. The flap 17 can be opened and closed by means of a drive 18, for example, a hydraulic or pneumatic actuator or an electric motor. In an alternative embodiment, the flap 17 is actuated by gravity. In the illustration shown, the cross-sectional area of ​​the outlet opening 16 is inclined to the longitudinal axis 7 of the cleaning chamber 4.

[0040] In the illustration shown, a suction opening 20 is arranged on the top side 19 of the cleaning chamber 4, via which the cleaning chamber 4 can be connected to a suction device (not shown). The suction opening 20 opens into a deflection chamber 52. The suction opening 20 is arranged centrally in the illustration shown, i.e., essentially centrally around the axis of symmetry 7. The suction opening 20 or, as in the example shown, an opening 53 of the deflection chamber 52 can also be designed as a connection for the suction device or for a hose or pipe to the suction device.

[0041] In the illustration shown, the cleaning chamber 4 has a lockable lid 21 in which the suction opening 20 is formed. The lid 21 can be folded back via a hinge 22, thus opening the cleaning chamber 4. It is preferred if the lid can be opened without tools.

[0042] A grid 23 is provided in the circulation area 6, which, in the illustration shown, is oriented horizontally, i.e., perpendicular to the longitudinal axis 7. Of course, the grid 23 can also be oriented obliquely to the longitudinal axis 7. The grid 23 is designed to retain bulk material 2 in the circulation area 6, while allowing dust and fine particles to pass through. The grid 23 can preferably be replaced without tools. In one example, the grid 23 has an opening width of 2 mm.

[0043] Fig. 2 and Fig. 3 show the separation device 1 during operation. The flow path of the bulk material 2 and the contaminant 24 is indicated by arrows 25, 26, 28, 29, 30, and 31.

[0044] In a conveying and emptying sequence, which together form a conveying phase, a specific quantity, typically in the range of 1 kg to 50 kg, of contaminated bulk material is sucked in through the suction opening 20 via the inlet nozzle 14. The emptying sequence is an optional sequence that is not mandatory but is implemented in the illustrated embodiment. If no emptying sequence is provided, the conveying phase is formed solely by the conveying sequence. Particularly with short lengths of the suction line 15, an emptying sequence can be omitted. Due to the suction negative pressure or the resulting volume flow, the contaminated bulk material 2 is first sucked into the inlet area 5 (arrow line 25). In the inlet area 5, the contaminated bulk material 2 is slowed down by contact with the sections 10a, 10b and 11a and sucked downwards towards the inlet opening 13 (arrow line 26).Depending on the volume flow rate, the contaminated bulk material 2 flows around the inlet pipe 12 one or more times, moving downwards. This movement, which can be described as a tapered screw thread, is facilitated by a channel 27 formed between the tapered sections 10a, 10b in the inlet area 5. Finally, the contaminated bulk material 2 enters the circulation area 6 via the inlet pipe 12 and is sucked upwards (arrow line 28).

[0045] During the conveying sequence, only a specific amount of bulk material 2 is sucked in. After all, or at least the majority, of the bulk material 2 has entered the cleaning chamber 4, a fluid, preferably air, is sucked in through the inlet nozzle 14 in a suction sequence following the conveying sequence. This has two effects: Firstly, residues of bulk material 2 in the suction line 15 and in the inlet nozzle 14 are sucked into the cleaning chamber 4. Secondly, the inflowing fluid forces the contaminated bulk material 2 into the circulation area 6, where it is circulated. The circulation also already takes place during the conveying sequence.

[0046] After the contaminated bulk material 2 has been sucked up through the inlet pipe 12, it is drawn centrally toward the suction opening 20. From there, it is displaced radially outward by following bulk material 2 (arrow line 29), falls laterally downwards, and from there, aided by the conically tapered section 10b of the circulation area 6, is sucked back up centrally toward the suction opening 20. The bulk material 2 is thus tipped over. The grid 23 prevents the suction of bulk material 2 but allows contaminants to pass through. This process is referred to as circulation. Through circulation, contaminants 24, such as dust and fine particles 24, are detached from the contaminated bulk material 2 and suctioned away through the grid 23 (arrow lines 30). The bulk material 2 is cleaned by circulation and suction.

[0047] After a certain period of time, the emptying sequence and thus the conveying phase are terminated by stopping or reducing the suction through the suction opening 20. The sequence following the conveying phase is referred to as the emptying sequence. In the emptying sequence, the bulk material 2 falls back down through the inlet pipe 12 (arrow lines 31) into the inlet area 5 due to gravity, as shown in Fig.3. By opening the flap 17, the cleaned bulk material 2 passes from the inlet area 5 through the outlet opening 16 to the outside. Additional suction can promote the conveyance of the cleaned bulk material 2 through the outlet opening 16. After passing through the outlet opening 16, the cleaned bulk material 2 can be conveyed further to another separation device (not shown) or directly or indirectly, for example via an intermediate storage facility, to a plastics processing machine (also not shown). Further conveyance can occur through pipes or hoses, into which the cleaned bulk material is preferably sucked.

[0048] Several separation devices 1 can also be arranged and operated in parallel in order to clean contaminated bulk material 2 using the process. QUOTES CONTAINED IN THE DESCRIPTION

[0000] This list of documents submitted by the applicant was generated automatically and is included solely for the convenience of the reader. This list is not part of the German patent or utility model application. The DPMA assumes no liability for any errors or omissions. Cited patent literature

[0000] WO 03 / 037534 A1

[0004]

Claims

[1] Separation device (1) for cleaning contaminated bulk material (2), preferably plastic bulk material, in particular recyclate (3), comprising: a cleaning chamber (4) with a preferably at least partially conically shaped inlet area (5); an inlet nozzle (14) leading into the inlet area (5); and an outlet opening (16) which can preferably be closed by a flap (17), wherein the separation device (1) is designed to be operated in a conveying sequence in which the contaminated bulk material (2) is conveyed through the inlet nozzle (14) into the inlet region (5) by suction, in an optional emptying sequence in which a fluid, in particular air, is sucked in through the inlet nozzle (14), and in an emptying sequence in which cleaned bulk material (2) is discharged through the outlet opening (16), wherein the conveying sequence and preferably the optional emptying sequence form a conveying phase, characterized by , that the cleaning chamber (4) has a preferably at least partially conically shaped circulation region (6) and the inlet region (5) and the circulation region (6) are arranged and designed such that the contaminated bulk material (2) is conveyed from the inlet region into the circulation region (6) by suction during the conveying phase during operation of the separating device (1) and is continuously circulated in the circulation region (6) by suction until the emptying sequence and is thereby cleaned, wherein contaminants (24) which are detached from the contaminated bulk material (2) can be sucked out of the circulation region (6) by sucking in the contaminated bulk material (2) during the conveying phase via a suction opening (20). [2] Separation device (1) according to claim 1, characterized bythat the suction opening (20) is arranged on an upper side (19) of the cleaning chamber (4), in particular on an upper side of the circulation area (6), and is designed as a connection for a suction device. [3] Separation device (1) according to claim 1 or 2, characterized by that the outlet opening (16) is arranged on a bottom side (50) of the cleaning chamber (4) and the cleaned bulk material (2) falls downwards through the outlet opening (16) due to gravity in the emptying sequence, preferably wherein the outlet opening (16) can be closed by a flap (17) in the conveying phase. [4] Separation device (1) according to one of claims 1 to 3, characterized by that a grid (23) is provided in the circulation area (6), preferably on an upper side of the circulation area (6). [5] Separation device (1) according to claim 4, characterized bythat the grid (23) has an opening width of 0.2 mm to 5 mm, in particular 0.5 mm to 3 mm. [6] Separation device (1) according to one of claims 1 to 5, characterized by that the circulation area preferably has an inlet opening on the underside through which the contaminated bulk material reaches the circulation area, wherein the inlet opening is arranged in particular below the inlet nozzle, so that the bulk material (2) in the conveying phase in the inlet area (5) can first be sucked preferably downwards to the inlet opening (13) and then into the circulation area (6), in particular upwards. [7] Separation device (1) according to claim 6, characterized by that an inlet pipe (12) is connected to the circulation area (6), at the end of which pipe facing the underside (50) of the cleaning chamber (4) the inlet opening (13) is arranged. [8] Separation device (1) according to claim 6 or 7, characterized bythat the cross-sectional area of ​​the inlet opening (13) is between 50% and 130%, preferably between 60% and 120%, of the cross-sectional area of ​​the inlet nozzle (14). [9] Separation device (1) according to one of claims 1 to 8, characterized by that the separating device (1) is designed to circulate the contaminated bulk material (2) in the circulation area (6) by the contaminated bulk material (2) being sucked in from above, being displaced radially outwards by following contaminated bulk material (2), falling downwards and then being sucked in again from above. [10] Separation device (1) according to one of claims 1 to 9, characterized by that the conveying phase and the emptying sequence form a cleaning cycle, the separating device is designed to carry out several cleaning cycles in succession. [11] Separation device (1) according to one of claims 1 to 10, characterized bythat in the cross-section of the cleaning chamber (4) and along an axis of symmetry (7), in particular the longitudinal axis, of the cleaning chamber (4), the inlet area (5) and the circulation area (6) at least partially overlap. [12] Separation device (1) according to one of claims 1 to 11, characterized by that, viewed in the cross-section of the cleaning chamber (4), the inlet region (5) and the circulation region (6) each have a conically converging section (10a, 10b) and in the inlet region (5) a channel (27) for the contaminated bulk material (27) is formed between the conically converging sections (10a, 10b) of the inlet region (5) and the circulation region (6). [13] Separation device (1) according to claim 12, characterized by that the inlet nozzle (14) is arranged at the level of the conically converging section (10b) of the circulation area (6) when viewed in the cross section of the cleaning chamber (14). [14] Plant for manufacturing a plastic product, comprising: a suction device; a separation device (1) according to one of claims 1 to 13, which is connected to the suction device; a plastics processing machine, in particular an injection molding machine, which is connected to the separation device (1).

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