HYDRAULIC DENSITY SEPARATION DEVICE
20240198355 ยท 2024-06-20
Assignee
Inventors
- G?nter Specht (Freital, DE)
- Sebastian Scheller (Rabenau, DE)
- J?rg Thomas (Dresden, DE)
- Sebastian Kemper (Witten, DE)
Cpc classification
B03B11/00
PERFORMING OPERATIONS; TRANSPORTING
International classification
Abstract
A hydraulic density separation device for separating a heavy material fraction with components of higher density from a light material fraction with components of lower density from a feed material includes a conveying device for conveying away the heavy material fraction, receiving chamber which can be filled with water for receiving the feed, a flow generator for generating a water flow in the receiving chamber and a water-fillable separation chamber for receiving the light material fraction. The conveying device has a shaft with a screw conveyor section for conveying the heavy material fraction out of the receiving chamber. The flow generator is designed and arranged such that a flow path of the water flow leads from the receiving chamber into the separation chamber. The conveying device has, in addition to the screw conveyor section, at least one washing section having a plurality of separate paddles arranged on the shaft.
Claims
1. A hydraulic density separation device for separating a heavy material fraction with components of higher density from a light material fraction with components of lower density from a feed material, comprising: a conveying device for conveying away the heavy material fraction; a receiving chamber which can be filled with water for receiving the feed material; a flow generator for generating a water flow in the receiving chamber; and a water-fillable separation chamber for receiving the light material fraction; wherein the conveying device has a shaft with at least one screw conveyor section for conveying the heavy material fraction out of the receiving chamber; wherein the flow generator is designed and arranged in such a way that a flow path of the water flow leads from the receiving chamber into the separation chamber; and wherein the conveying device has, in addition to the screw conveyor section, at least one washing section having a plurality of separate paddles arranged on the shaft.
2. The hydraulic density separation device according to claim 1, wherein a plurality of screw conveyor sections is provided, a washing section being arranged between two adjacent screw conveyor sections; and/or wherein a plurality of washing sections is provided, with the screw conveyor sections and the washing sections being arranged alternately with respect to one another.
3. The hydraulic density separation device according to claim 1, wherein the washing section comprises one of the following: between 2 and 52 paddles, between 4 and 36 paddles, and between 12 and 24 paddles.
4. The hydraulic density separation device according to claim 1, wherein the winding of the screw conveyor section extends over a range between 360? and 1440?.
5. The hydraulic density separation device according to claim 2, wherein adjacent washing sections have a different number of paddles and/or differently formed and/or arranged paddles and/or wherein adjacent screw conveyor sections have differently formed windings.
6. The hydraulic density separation device according to claim 1, wherein the paddles are arranged at an angle on the shaft in such a way that a material transport of the heavy material fraction in the conveying direction of the shaft also takes place in the region of the respective washing section, and/or wherein a plurality of paddles are arranged one behind the other in relation to a longitudinal direction of the shaft and/or wherein a plurality of paddles are arranged one behind the other in a circumferential direction of the shaft.
7. The hydraulic density separation device according to claim 1, wherein a radial paddle length is at least substantially equal to a web height of the winding of at least one adjacent screw conveyor section.
8. The hydraulic density separation device according to claim 1, wherein the shaft is arranged and mounted at an angle ? with respect to the base, the angle ? being one of the following: between 8? and 85?, between 10? and 70? and between 12? and 20?; and/or wherein the shaft is mounted with its one shaft end in the region of the receiving chamber and with its other shaft end in the region of a discharge opening of the heavy material fraction.
9. The hydraulic density separation device according to claim 1, wherein an outflow opening of the flow generator opens into the receiving chamber and/or wherein the separation chamber is designed as a suction chamber for the flow generator.
10. The hydraulic density separation device according to claim 9, wherein the receiving chamber has a curved deflection area for the water flow at least substantially opposite the outflow opening and/or below the shaft; and/or wherein a center axis of the outflow opening runs below a central longitudinal axis of the shaft.
11. The hydraulic density separation device according to claim 1, wherein a weir is arranged between the receiving chamber and the separation chamber.
12. The hydraulic density separation device according to claim 1, wherein a further conveying device for discharging the light-weight fraction is assigned to the separation chamber.
13. The hydraulic density separation device according to claim 12, wherein the conveying direction of the further conveying device extends at least substantially opposite to the conveying direction of the conveying device; and/or wherein the receiving chamber and/or the separation chamber are arranged and designed in such a way that the flow path of the light material fraction into the separation chamber is deflected by 90?+/?20?.
14. The hydraulic density separation device according to claim 1, wherein a suction device is provided which is designed to suck off and/or suck in dirty water from the receiving chamber and/or from the separation chamber; and/or wherein a feed device is provided for feeding fresh water into the receiving chamber and/or into the separation chamber.
15. The hydraulic density separation device according to claim 1, wherein a separating plate is arranged at least in regions between the receiving chamber and a conveyor housing in which the shaft is arranged.
16. The hydraulic density separation device according to claim 7, wherein the distance between the outermost upper edge of the winding and/or of the paddle and one of the adjacent housing walls of a conveyor housing in which the shaft is arranged is one of the following: at least 30 mm, between 40 mm to 900 mm, and between 100 to 200 mm.
17. The hydraulic density separation device according to claim 9, wherein a suction pipe, which is arranged at least in regions in the separation chamber for sucking in water located in the separation chamber, is associated with the flow generator.
18. The hydraulic density separation device according to claim 11, wherein the flow path for the light material fraction extends from the upper region of the receiving chamber via the weir into the separation chamber.
19. The hydraulic density separation device according to claim 12, wherein the further conveying device has a riddle and/or vibrating screen and/or wherein the conveying plane of the further conveying device runs at least in regions below the upper edge of the weir.
20. The hydraulic density separation device according to claim 14, wherein the inflow opening of the feed device is provided below and/or in the region of the shaft.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION
[0086]
[0087] It is understood that water has been introduced into the density separation device 1 for its operation. However, the water or the water level is not shown in more detail in the embodiments shown.
[0088] The density separation device 1 comprises a conveying device 5 for conveying away the heavy material fraction 2, as shown in
[0089] In this context, it is understood that during operation the receiving chamber 6 is at least partially filled with water, the water itself being used for the separation process. Thus, the components of the heavy material fraction 2, which have a significantly higher density than the water, sink to the bottom of the receiving chamber 6 and are conveyed away by the conveying device 5. The light material fraction 3, which has components with lower or the same density as water or even slightly higher density than water, rises due to the buoyancy. Thus, the components are hydraulically separated on the basis of their density.
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[0091] In addition, the density separation device 1 comprises a separation chamber 8 which can be filled with water to receive the light material fraction 3. The separation chamber 8 can also serve to supply water for the flow generator 7, in particular to implement a closed flow circuitbut it does not have to.
[0092]
[0093] The further section of the conveying device 5, which can also be arranged in the water, can be arranged in a conveyor housing 19, which is shown in more detail in
[0094] The flow generator 7 shown in
[0095] Furthermore,
[0096] In
[0097] Finally, the paddles 11 may be arranged around the circumference of the shaft 9 in the area of the washing section 12 and serve at least for washing and cleaning the heavy material fraction 2. In further embodiments, but not shown in more detail, the paddles 11 are arranged in the washing section 12 such that they are aligned to follow the helix of the adjacent screw conveyor section 10, as explained previously. In particular, the helix and/or the helix pitch of the winding 13 of all screw conveyor sections 10 is at least substantially the same.
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[0100] The washing section 12 can have differently designed paddles 11 or a different number of paddles 11 depending on the desired cleaning result. In particular, it is envisaged that a washing section 12 has between 4 and 24 paddles 11, as shown in more detail in
[0101] In
[0102] It is not shown in detail that adjacent washing sections 12 can have a different number of paddles 11. Also, the paddles 11 of adjacent washing sections 12 may have different designs.
[0103] As explained above,
[0104] It is not shown in more detail that the helix pitch of adjacent screw conveyor sections 10 can also be designed differently.
[0105] The paddles 11 are in particular arranged at an angle on the shaft 9 in such a way that a material transport of the heavy material fraction 2 in the conveying direction F of the shaft 9 also takes place in the area of the respective washing section 12.
[0106]
[0107] It can be seen schematically from
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[0109] Furthermore,
[0110]
[0111]
[0112] In
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[0114] As previously explained,
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[0117] Furthermore,
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[0119] In addition,
[0120] Furthermore,
[0121] Furthermore,
[0122] It is not shown in more detail that a suction device can be provided, which is designed to suck off and/or suck in dirty water from the receiving chamber 6 and/or the separation chamber 8, in particular wherein density measurement sensors are assigned to the suction device. It is also not shown in more detail that a feed device is provided for feeding fresh water into the receiving chamber 6, in particular wherein the inflow opening of the feed device is provided below and/or in the region of the shaft 9.
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[0124] The conveyor housing 19 can be designed to be watertight in the water-bearing area.
[0125] It is not shown in more detail that the flow velocity of the flow generator 7 is adjustable, in particular for varying the degree of separation of the density of the components of the light material fraction 3.
[0126] Also not shown in more detail is that an overflow device may be provided for the receiving chamber 6 and/or separation chamber 8, which may for example be an overflow chute. In addition, a control device can be provided which can interact either with the density measurement sensors and/or the level sensors in the receiving chamber 6. This control device can be used to control the operation of the density separation device 1 as required.
[0127] The method according to the invention uses the density separation device 1 shown in the figures, which is filled with water for operation, so that the receiving chamber 6 and, if required, also at least in some areas the separation chamber 8 are filled with water.
[0128] The feed material 4 can then be fed in, for example via conveyor belts or via an excavator shovel.
[0129] The operation of the flow generator 7 then generates a water flow in the receiving chamber 6, which leads from the receiving chamber 6 into the separation chamber 8 and in particular leads to the entrainment of the light material fraction 3, wherein the light material fraction 3 can thus be led from the receiving chamber 6 into the separation chamber 8. Due to the gravitational effect, the components of the heavy material fraction 2 sink into the lower area of the receiving chamber 6 and are conveyed away via the conveyor 5.
[0130] The components of the light material fraction 3 rise due to the buoyancy effect and are also carried along by the water flow. The density of the components of the light material fraction 3 can be lower than the density of the water used or only slightly higher than the density of the water used. Preferably, the light material fraction 3, together with water, is led over the weir 26 into the separation chamber 8.
[0131] In particular, a closed water circuit is provided so that the water in the separation chamber 8 can be made available again to the receiving chamber 6 via the flow generator 7. However, it can also be provided that fresh water is always supplied to the receiving chamber 6.
[0132] The light material fraction 3 can preferably be conveyed away via the further conveying device 27, in particular wherein this is designed as a shaking and/or vibrating screen.
[0133] The heavy material fraction 2 is both conveyed away by the conveying device 5 and cleaned and/or washed in the area of the washing sections 12. The residual fraction, which is separated from the heavy material fraction 2 in the area of the washing sections 12, can in particular dissolve in the water or remain in the water in the conveyor housing 19 and, for example, be discharged by draining the water from the conveyor housing 19 after switching off the density separation device 1.
[0134] The separated heavy material fraction 2 is at least substantially freed from the residual fraction by the cleaning in the washing sections 12 and has in particular a high degree of purity.
[0135] However, the separation process between the heavy material fraction 2 and the light material fraction 3 does not take place in the area of the conveyor housing 19, but in the receiving chamber 6. In the area of the conveyor housing 19 and thus also through the washing sections 12, only a cleaning of the heavy material fraction 2 takes place and no separation of the light material fraction 3. The light material fraction 3 is thus not affected by the residual fraction of the heavy material fraction 2 loosened up by the washing sections 12.
LIST OF REFERENCE SIGNS
[0136] 1 Density separation device [0137] 2 Heavy material fraction [0138] 3 Light material fraction [0139] 4 Feed material [0140] 5 Conveying device [0141] 6 Receiving chamber [0142] 7 Flow generator [0143] 8 Separation chamber [0144] 9 Shaft [0145] 10 Screw conveyor section [0146] 11 Paddle [0147] 12 Washing section [0148] 13 Windings [0149] 14 Paddle length [0150] 15 Web height [0151] 16 Distance [0152] 17 Top edge [0153] 18 Housing wall [0154] 19 Conveyor housing [0155] 20 Shaft end [0156] 21 Other shaft end [0157] 22 Discharge opening [0158] 23 Outflow opening [0159] 24 Suction pipe [0160] 25 Deflection area [0161] 26 Weir [0162] 27 Further conveyor [0163] 28 Conveying level of 27 [0164] 29 Upper edge of 26 [0165] 30 Separating means [0166] 31 Flow tube [0167] 32 Opening in 31 [0168] F Conveying direction of 5 [0169] L Longitudinal direction of 9 [0170] M Central longitudinal axis of 23 [0171] A Central longitudinal axis of 9 [0172] R Conveying direction from 22 [0173] ? Angle