EP3310566B1 - Screw press device - Google Patents
Screw press device Download PDFInfo
- Publication number
- EP3310566B1 EP3310566B1 EP16730809.7A EP16730809A EP3310566B1 EP 3310566 B1 EP3310566 B1 EP 3310566B1 EP 16730809 A EP16730809 A EP 16730809A EP 3310566 B1 EP3310566 B1 EP 3310566B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- screw
- press
- drive
- housing
- press screw
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000000463 material Substances 0.000 claims description 62
- 230000005540 biological transmission Effects 0.000 claims description 7
- 230000003247 decreasing effect Effects 0.000 claims description 4
- 239000011796 hollow space material Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 description 21
- 230000006835 compression Effects 0.000 description 9
- 238000007906 compression Methods 0.000 description 9
- 230000007423 decrease Effects 0.000 description 9
- 239000000706 filtrate Substances 0.000 description 6
- 238000003825 pressing Methods 0.000 description 6
- 238000011161 development Methods 0.000 description 4
- 230000018109 developmental process Effects 0.000 description 4
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- 239000003921 oil Substances 0.000 description 3
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- 239000002028 Biomass Substances 0.000 description 2
- 235000014676 Phragmites communis Nutrition 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000005238 degreasing Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000013467 fragmentation Methods 0.000 description 2
- 238000006062 fragmentation reaction Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 206010061218 Inflammation Diseases 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000006735 deficit Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000004054 inflammatory process Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
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- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/12—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing
- B30B9/16—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing operating with two or more screws or worms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B15/00—Details of, or accessories for, presses; Auxiliary measures in connection with pressing
- B30B15/26—Programme control arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/12—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing
- B30B9/16—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing operating with two or more screws or worms
- B30B9/166—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing operating with two or more screws or worms the screws being coaxially disposed in the same chamber
Definitions
- the invention relates to a screw press device with a first screw press which has a first screw housing, a first screw press rotatably mounted in the first screw housing, a first inlet and a first outlet, at least one second screw press which has a second screw housing, a second screw press which is rotatably mounted in the second screw housing Press screw having a second inlet coupled to the first outlet and a second outlet, and a drive device for driving the first and second press screws.
- a screw press device of this type serves to strongly compress pressable and porous material, also referred to as pressed material, that is introduced via the inlet, with the result that liquid present in the material, also referred to as filtrate, is pressed out.
- pressable and porous material also referred to as pressed material
- filtrate liquid present in the material
- a steadily increasing pressure is required on the affected material.
- this process takes place with the help of the press screw due to the pitch of the screw.
- the press screw is usually surrounded by a strainer, which is also known as a so-called strainer basket, the pressed liquid can only flow in one direction towards the colander, i.e. from the inside to the outside.
- the extruder screws have a relatively high screw pitch at the inlet to accommodate the material to be extruded.
- the pitch of the screw generally decreases towards the outlet.
- the volume in the screw thread gap or in the conveying threads which likewise extend in a spiral shape between the spiral-shaped screw webs or spirals, decreases and the compression pressure increases.
- the material or volume flow is determined by the speed and the screw pitch of the press screw and is also dependent on various influences.
- the working method of the screw press has the advantage that the material or pressing material is not overheated, so that thermally induced impairments of the material or pressing material cannot occur.
- the use of two press screws connected in series according to the type mentioned as a two-stage solution offers a better possibility of automation, leads to a more effective degreasing of the product and has a higher throughput while at the same time saving energy and reducing wear.
- a screw press device of the type mentioned is generally used in technology.
- a preferred application is the production of meat meal, where it is important not only to achieve a high degree of comminution, but also a high degree of drying.
- Another use is the processing of oil-containing plant biomass, in which case the desired starting product is formed at least primarily from the oil pressed out of the biomass.
- Such a device is, for example, from DE 196 01 128 A1 is known, which describes a screw press for extracting vegetable oil from oil-containing material, which has at least two identically shaped sub-screw conveyors in terms of the shape of the screw winding to increase the squeezing capacity, which are connected in series with the interposition of an intermediate throttle point on one axis.
- the two partial screw conveyors are thus seated together on a drive shaft which is set in rotation by a drive device.
- the DE 298 20 464 U1 discloses a screw press device for dry or liquid-containing material to be pressed with a single press screw which is rotatably mounted in a screw housing having an inlet and an outlet. Furthermore, pressure means are provided for generating a counter-pressure on the material to be pressed, which resiliently prestress a closure member against the outlet in such a way that it releases a certain outlet cross-section of the outlet depending on the pressure difference between the material to be pressed and the counter-pressure.
- the pressure means are designed in such a way that the counter-pressure on the material to be pressed can be adjusted.
- the DE 20 2007 008 072 U1 discloses a screw press made from individual screw elements of a screw press with a screw housing, an inlet and an outlet, the screw elements being hollow and firmly connected to one another and being driven by an internally arranged drive shaft. Furthermore, a compensator element is arranged on the outlet-side end of the press screw behind the last screw element and in front of fastening parts of the screw elements on the screw shaft and is designed to be resilient.
- the DE 299 01 683 U1 describes a screw press for biowaste with a motor-driven screw press, which is enclosed by a tube over a first part of its length and by a sieve over a second part of its length, with a liquid outlet and with a solids outlet, with the press screw being open in the core area tube fixed in the direction of rotation is inserted.
- U.S. 2015/076084 A1 discloses a screw press device according to the preamble of claim 1.
- liquid can be squeezed out.
- overflow overflow
- underflow underflow
- the liquid discharge is disrupted.
- overflow the surface of the material is compressed to such an extent that the escape of liquid is severely impeded or even stopped; the friction that occurs and the resulting heat can damage the quality of the material to be pressed or even its Inflammation and thereby also increased wear of components of the screw press device are caused.
- underflow the liquid drain also dries up because there is now insufficient compression pressure to squeeze out the liquid.
- the first and second press screws can be driven at different speeds, with a special control concept according to the invention, for which purpose a correspondingly suitable speed control device is to be provided.
- the special control concept according to the invention consists in, for the first case when the pressure in the material or material to be pressed within the first screw housing, essentially adjacent to the first outlet, exceeds a predetermined first threshold value set the second press screw to a speed that is above a first speed value, and for the second case, when the pressure in the material or pressing material within the first press screw housing falls below a predetermined second threshold value, essentially adjacent to the first outlet, the second press screw to a speed set, which is below a second speed value.
- the invention makes use of the finding that as the speed of the press screw increases, there is less compression of the material or material to be pressed and thus also a lower degree of fragmentation, and with a decreasing speed of the press screw there is greater compression of the material or material to be pressed and thus also a higher degree of fragmentation is achieved.
- this avoids the material or material to be pressed being subjected to compression that is too high for the conditions there, long before the second outlet forming the outlet of the entire screw press device, with the result of increased friction and thus heating and the resulting risk of damage to the quality of the pressing material as well as increased wear of components of the device and clogging of the entire device, and in the second case it is ensured that the material or pressing material does not remain too viscous, but rather has a desired sufficient compression in the course of its path through the screw press device is subjected.
- control concept according to the invention therefore ensures that at the second outlet, which also forms the outlet of the entire screw press device, the material or pressed material always exits with a desired compression that is as high as possible, with the result that as much liquid as possible is removed from the material or pressed material could be squeezed out. Accordingly, the solution according to the invention leads to a significant increase in the efficiency of the screw press device without the risk of an increase in wear.
- the first threshold should expediently be equal to the second threshold.
- the first speed value should expediently be equal to the second speed value, with the first speed value and the second speed value is equal to the value of the speed of the first press screw.
- control concept according to the invention consists in setting the speed of the second press screw to a value greater than the speed of the first press screw for the first case that the pressure in the material within the first press screw housing essentially adjacent to the first outlet exceeds a predetermined threshold value to be raised so that the second press screw runs faster than the first press screw, and in the second case that the pressure in the material within the first press screw housing falls below the predetermined threshold value essentially adjacent to the first outlet, to a value below the speed of the first press screw, so that the second press screw then runs slower than the first press screw.
- the screw press device is characterized in that the speed control device has a sensor that measures a physical variable that is required by the drive device for driving the first press screw, the speed control device using the physical variable measured by the sensor as a measured variable for the pressure of the material within the first auger housing adjacent to the first outlet and setting the second auger to a speed greater than the speed of the first auger in the event that the physical quantity measured by the sensor exceeds a predetermined first threshold, and in the event that the physical variable measured by the sensor falls below a predetermined second threshold value, is below the speed of the first press screw, the physical variable preferably being a power output or an electrical current.
- one squeezing screw is driven by a hollow shaft, through which a shaft driving the other squeezing screw extends.
- a hollow shaft through which a shaft driving the other squeezing screw extends.
- the two squeezing screws and the two shafts are arranged coaxially with one another and one squeezing screw sits concentrically on the hollow shaft and the other press screw concentrically on an exposed section of the shaft which is partially surrounded by the hollow shaft.
- the first squeezing screw is driven by the hollow shaft and the second squeezing screw is driven by the shaft, which is partially surrounded by the hollow shaft.
- the drive device is arranged at that point of the device at which the shaft and the hollow shaft surrounding the shaft are located, each with an end section, and/or adjacent to the first inlet.
- the drive device preferably has two drive motors, of which one drive motor is designed to drive one squeezing screw and the other drive motor is designed to drive the other squeezing screw.
- one drive motor is preferably designed to drive the internal shaft essentially directly, and the other drive motor is designed to essentially drive the hollow shaft.
- the drive device to have a drive motor and a gear, in particular a planetary gear, the transmission ratio of which can be changed, the drive motor being designed to drive one press screw essentially directly, and the gear being coupled to the drive motor and is designed to drive the other press screw essentially directly, and the speed control device is designed to control the transmission by changing its transmission ratio.
- the first squeezing screw housing and the second squeezing screw housing should expediently form a common housing.
- an expander or extruder is arranged between the first outlet and the second inlet, which expander or extruder has a housing, an extruder screw rotatably mounted in the housing, an inlet coupled to the first outlet and an outlet coupled to the second inlet.
- Such an extruder causes a slight relaxation of the material or pressed material compressed at the first outlet.
- the two press screws and the extruder screw are expediently arranged coaxially to one another.
- the barrel of the extruder connects the first press screw barrel to the second press screw barrel.
- the extruder screw is preferably coupled in a torque-proof manner to the first press screw.
- the screw pitch of the extruder screw is preferably constant over its length.
- the screw pitch of the extruder screw can preferably be smaller than the screw pitch of the extruder screw, which is advantageous for the desired relaxation effect.
- the associated squeezing screw housing forms a cavity that is essentially cylindrical over the entire length of the squeezing screw and the squeezing screw has a steadily monotonically or continuously increasing core diameter and a steadily monotonously or continuously decreasing screw pitch. It is therefore essential in this embodiment that the core diameter increases without any interruption in the working direction and the pitch of the press screw decreases in a corresponding manner without any discontinuity.
- This solution allows an even higher proportion of liquid to be pressed out of solid material components while at the same time reducing the energy required for the extraction process for the drive device, as a result of which the output of the respective screw press can be increased even further.
- the screw press device shown as a whole comprises a housing 2, within which a first screw press 4 and a second screw press 6 provided downstream of the first screw press 4 are arranged. Due to the use of two screw presses 4, 6 connected in series, the screw press device according to the exemplary embodiment described is a two-stage screw press device. Such a two-stage solution offers a good possibility for automation and leads to a more effective degreasing of the product to be pressed and to a better utilization of the throughput while at the same time saving energy and reducing wear.
- the first screw press 4 has a first screw press housing 8, a first press screw 10 rotatably mounted in the first press screw housing 8 with spiral helices or screw webs 10a and conveying passages also extending spirally in between, a first inlet 12 designed as an inlet shaft in the illustrated embodiment, and a first outlet 14 on.
- the first squeezing screw housing 8 is provided with openings 8a and is usually designed or referred to as a strainer basket.
- the second screw press 6 has a second screw press housing 16, a second press screw 18 rotatably mounted in the second press screw housing 16 with spiral helices or screw webs 18a and itself conveyor passages also extending in a spiral shape in between, a second inlet 20 and a second outlet 22 .
- the second squeezing screw housing 16 is also perforated or provided with openings 16a and is usually also designed or referred to as a strainer basket.
- the press screw housings 8, 16 designed as strainer baskets are usually composed of two half-shells or several shell-shaped sections; This is advantageous, on the one hand, in order to allow easy access to the press screw, for example for maintenance purposes, and, on the other hand, as a simple way of adjusting the permeability of the press screw housing, which is designed as a strainer basket, by replacing the press screw housing with a press screw housing with a different degree of perforation or a different number of To create openings and / or openings with a different diameter.
- an expander 24, also referred to as an extruder, is provided between the two screw presses 4, 6, which has an expander housing 26, an expander screw 28 rotatably mounted in the housing with spiral coils or screw webs 28a and also spirally extending in between Conveyor passages 28b, an inlet 30 coupled to the first outlet 14 and an outlet 32 coupled to the second inlet 20.
- the wall of the expander housing 26 has no perforations or openings, but is closed.
- pins 26a which are designed as threaded bolts in the illustrated embodiment, are inserted through the wall of the expander housing 26 and protrude far into the conveyor passages 28b, which are delimited by the spiral-shaped screw webs 28a and also extend spirally. Therefore, the extruder or expander used in the illustrated embodiment is also referred to as a pin extruder or expander. So that the spiral-shaped screw flights 28a do not collide with the pins 26a, the screw flights 28a are provided with interruptions at the appropriate points, which allow the pins 26a to pass through and in Figure 2b not marked, but clearly recognizable.
- pin extruder 24 By designing the pin extruder 24 with the pins 26a, which are arranged in pin levels, such as Figures 2a and b can be seen, and pass through the interruptions in the screw webs 28a, there is a particularly good conveying effect.
- the splitting of the extrudate stream at each interruption in the screw flights 28a into a part that passes through the interruptions in the screw flights 28a in a substantially axial direction and a part that enters the spiral-shaped conveyor passages 28b following in the flow direction creates a achieves a particularly good mixing effect.
- the first press screw housing 8 and the second press screw housing 16 and the intermediate expander housing 26 form a common housing and thus enclose a common continuous space in which the two press screws 10, 18 and the intermediate expander screw 28 are arranged.
- the two squeezing screw housings 8, 16 and the expander housing 26 each have a cylindrical shape, with the two squeezing screw housings 8, 16 having essentially the same outer diameter and also essentially the same inner diameter in the illustrated embodiment, while the outer diameter of the expander housing 26 is smaller, but its Inner diameter approximately the inner diameter of the press screw housing 8, 16 corresponds.
- the diameter of its cylindrical base body without taking into account the radial extent of the screw webs 28a, at the inlet 30 of the expander housing 26 is smaller than the inside diameter of the first press screw 10 at the first outlet 14 and larger than the inside diameter of the second Press screw 18 at the second inlet 20, wherein the inside diameter of the expander screw 28 remains constant over its entire length.
- the second squeezing screw 18 sits on an exposed portion of an inner shaft 34, which is otherwise surrounded by an outer hollow shaft 36, on which the first squeezing screw 10 and the expander screw 26 sit.
- the inner shaft 34 and the outer hollow shaft 36 are rotatably mounted coaxially to one another about a common axis of rotation R, but can of course be driven independently of one another. Since the first press worm 10 and the expander worm 26 are mounted on the hollow shaft 36 and are thus connected to it in a rotationally fixed manner, they are set in rotation by the latter together at the same speed.
- the inner shaft 34 ensures that, independently of the outer hollow shaft 36 and thus the first press screw 10 and the expander screw 26, the second press screw 18 is set in rotation, since it is mounted on the inner shaft 34 and is non-rotatably connected to it.
- two drive motors 38, 40 are provided.
- an electric motor is used as the drive motor.
- the two drive motors 38, 40 form a common structural unit, which is arranged adjacent to the first inlet 12 at the upstream end of the housing 2.
- the outer hollow shaft 36 is driven by the first drive motor 38 and the inner shaft 34 by the second drive motor 40.
- a gear which is coupled to the first drive motor 38 and is preferably designed as a planetary gear.
- the two shafts 34, 36 are one in Figure 3a indicated axis of rotation R rotatably mounted in bearings, which are not marked in detail in the drawings; in principle, the drive motors 38, 40 can also serve as one of these bearings.
- the assembly consisting of the two screw presses 4, 6 and the expander 24 is arranged inside the housing 2 on supports 42, which in turn are seated on a horizontal support element 44.
- a compartment 46 is formed within the housing 2 below the assembly mentioned above, in which a filtrate emptying screw 48 is rotatably mounted above the bottom 2a of the housing 2, the pitch of its spiral helices or screw webs being in the opposite direction towards the centre, where the housing 2 with a filtrate outlet 50 is provided.
- a second compartment 52 is formed in the downstream end of the housing 2, in the lower portion of which a paddle wheel 54 is rotatably mounted, which is also referred to as a so-called. Reed crusher.
- the screw press device described serves to strongly compress pressable and porous material, also referred to as pressed material, which is entered via the first inlet 12, with the result that liquid present in the material, also referred to as filtrate, is pressed out and the material in a dry , compressed state from the second outlet 22 is discharged.
- the first inlet 12 of the first screw press 4 also forms the inlet for the entire screw press device and the second outlet 22 of the second screw press 6 forms the outlet for the entire screw press device for dispensing the then compressed material or material to be pressed. In order to expel the liquid from the material, a steadily increasing pressure is required on the affected material.
- the two screw presses 4, 6 connected in series are provided in the illustrated embodiment, in which this process takes place with the aid of the continuously operating press screws 10, 18 due to the screw pitch.
- the squeezing screws 10, 18 are surrounded by the respective squeezing screw housing 8, 16, which is provided with openings or perforations or is designed as a strainer or sieve body, the liquid that is pressed out can only flow in one direction towards the squeezing screw housings 8, 16, i.e. from inside out, flow.
- the figures 1 and 3 reveal that the first press screw 8 at the first inlet 12 of the first screw press 4 and the second press screw 18 at the second inlet 20 of the second screw press 6 and thus at its upstream beginning each have a relatively high screw pitch.
- the downstream second screw press 6 carries out post-processing instead of.
- the expander 24 connected between the two screw presses 4, 6 causes the material exiting at the first outlet 14 to relax, as a result of which the material to be pressed is broken up and thus remains porous. Accordingly, the expander 24 acts as a kind of buffer.
- the cavity delimited by the inner wall of the first press screw housing 8 increases at the transition from the first outlet 14 to the inlet 30 of the expander 24, which already leads to a first relaxation of the material to be pressed when it enters the expander 24.
- the screw pitch of the expander screw 28, which is non-rotatably coupled to the first press screw 10 is constant over its length and is less than the screw pitch of the two press screws 10, 18.
- the two press screws 10, 18 are designed essentially the same in terms of their dimensions and their screw pitch. Furthermore, you can 3 see that in the illustrated embodiment, both press screws 10, 18 have a steadily monotonically or continuously increasing core diameter of their cylindrical body and a steadily monotonously or continuously decreasing screw pitch, while according to figure 1 the two squeezing screw housings 8, 16 define a cylindrical cavity extending over the entire length of the associated squeezing screw 10 or 18, respectively.
- the core diameter of the cylindrical base body of the press screws 10, 18 increases without any interruption in the working direction, which is defined from left to right in the figures, and the pitch of the press screws 10, 16 decreases in a corresponding manner without any discontinuity. whereby the width, defined in the axial direction, of the conveying passages, which also extend spirally between the spiral-shaped screw webs 10a and 18a, respectively, decreases accordingly.
- the material or volumetric flow is determined by the speed and the screw pitch of the press screws 10, 18 and is also dependent on other different influences. As long as the material has sufficient porosity or capillarity, liquid can be squeezed out. However, if the material flow experiences either an increase in speed (overflow) or a decrease in speed (underflow) due to unfavorable circumstances, the liquid discharge is disrupted. In the first case of overflow, the surface of the material is compressed to such an extent that the escape of liquid is severely impeded or even stopped; the friction that occurs and the resulting heat can damage the quality of the material to be pressed or even cause it to ignite, and this can result in increased wear of the components of the screw press device. In the second case of underflow, the liquid drain also dries up because there is now insufficient compression pressure to squeeze out the liquid.
- the two press screws 10, 18 can be driven selectively at different speeds by the drive motors 38, 40 and a speed control device 60 is also provided to which the drive motors 38, 40 are connected. If a gearbox is used instead of the second drive motor 40, this must be designed in such a way that its transmission ratio can be changed, namely by the speed control device 60. Furthermore, the speed control device 60 is designed in such a way that, via a sensor 62, it receives the data from the first drive motor 38 measures the power consumption required for driving the first press screw 10 or a correspondingly required electrical current. The measured variable obtained in this way is then used by the speed control device 60 to determine the pressure of the material within the first press screw housing 8 adjacent to the first outlet 14 evaluated accordingly.
- the control concept of the speed control device 60 now consists of controlling the drive motors 38, 40 or at least the second drive motor 40 in such a way that the speed of the second press screw 18 for the first case when the pressure in the material within the first press screw housing 8 adjacent to the first outlet 14 exceeds a predetermined threshold value, is increased to a value greater than the rotational speed of the first press screw 10, so that the second press screw 18 runs faster than the first press screw 10, and for the second case when the pressure in the material inside the first press screw housing 8 is substantially falls below the predetermined threshold value adjacent to the first outlet 14, is lowered to a value below the rotational speed of the first press screw 10, so that the second press screw 18 then runs more slowly than the first press screw 10.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Press Drives And Press Lines (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Description
Die Erfindung betrifft eine Schneckenpressvorrichtung mit einer ersten Schneckenpresse, die ein erstes Schneckengehäuse, eine im ersten Schneckengehäuse drehbar gelagerte erste Pressschnecke, einen ersten Einlass und einen ersten Auslass aufweist, mindestens einer zweiten Schneckenpresse, die ein zweites Schneckengehäuse, eine im zweiten Schneckengehäuse drehbar gelagerte zweite Pressschnecke, einen mit dem ersten Auslass gekoppelten zweiten Einlass und einen zweiten Auslass aufweist, und einer Antriebseinrichtung zum Antrieb der ersten und zweiten Pressschnecken.The invention relates to a screw press device with a first screw press which has a first screw housing, a first screw press rotatably mounted in the first screw housing, a first inlet and a first outlet, at least one second screw press which has a second screw housing, a second screw press which is rotatably mounted in the second screw housing Press screw having a second inlet coupled to the first outlet and a second outlet, and a drive device for driving the first and second press screws.
Eine Schneckenpressvorrichtung dieser Art dient dazu, über den Einlass eingegebenes pressfähiges und poröses Material, auch als Pressgut bezeichnet, stark zu komprimieren mit der Folge, dass im Material vorhandene Flüssigkeit, auch als Filtrat bezeichnet, herausgepresst wird. Um die Flüssigkeit aus dem Material auszutreiben, bedarf es eines stetig wachsenden Pressdruckes auf das betroffene Material. In einer kontinuierlich arbeitenden Schneckenpresse findet dieser Vorgang mithilfe der Pressschnecke aufgrund deren Schneckengangsteigung statt. Da die Pressschnecke gewöhnlich von einem Siebkörper, der auch als sog. Seiherkorb bezeichnet wird, umschlossen ist, kann die ausgepresste Flüssigkeit nur in einer Richtung zum Seiherkorb hin, also von innen nach außen, fließen. Gewöhnlich haben die Pressschnecken am Einlass eine relativ hohe Schneckengangsteigung, um das zu pressende Material aufzunehmen. Zum Auslass hin nimmt die Schneckengangsteigung in der Regel ab. Dadurch nimmt das Volumen in der Schneckenganglücke bzw. in den sich zwischen den spiralförmigen Schneckenstegen bzw. Wendeln ebenfalls spiralförmig erstreckenden Fördergängen ab und der Kompressionsdruck zu. Der Material- bzw. Volumenstrom wird durch die Drehzahl und die Schneckengangsteigung der Pressschnecke bestimmt und ist des Weiteren von unterschiedlichen Einflüssen abhängig. Die Arbeitsweise der Schneckenpresse hat den Vorteil, dass das Material bzw. Pressgut nicht überhitzt wird, sodass thermisch bedingte Beeinträchtigungen des Materials bzw. Pressgutes nicht auftreten können. Die Verwendung zweier hintereinander geschalteter Pressschecken gemäß der eingangs genannten Art als zweistufige Lösung bietet eine bessere Automatisierungsmöglichkeit, führt zu einer wirksameren Entfettung des Produktes und hat eine höhere Durchsatzleistung unter gleichzeitiger Energieeinsparung und Verschleißminderung.A screw press device of this type serves to strongly compress pressable and porous material, also referred to as pressed material, that is introduced via the inlet, with the result that liquid present in the material, also referred to as filtrate, is pressed out. In order to expel the liquid from the material, a steadily increasing pressure is required on the affected material. In a continuously working screw press, this process takes place with the help of the press screw due to the pitch of the screw. Since the press screw is usually surrounded by a strainer, which is also known as a so-called strainer basket, the pressed liquid can only flow in one direction towards the colander, i.e. from the inside to the outside. Usually, the extruder screws have a relatively high screw pitch at the inlet to accommodate the material to be extruded. The pitch of the screw generally decreases towards the outlet. As a result, the volume in the screw thread gap or in the conveying threads, which likewise extend in a spiral shape between the spiral-shaped screw webs or spirals, decreases and the compression pressure increases. The material or volume flow is determined by the speed and the screw pitch of the press screw and is also dependent on various influences. The working method of the screw press has the advantage that the material or pressing material is not overheated, so that thermally induced impairments of the material or pressing material cannot occur. The use of two press screws connected in series according to the type mentioned as a two-stage solution offers a better possibility of automation, leads to a more effective degreasing of the product and has a higher throughput while at the same time saving energy and reducing wear.
Eine Schneckenpressvorrichtung der eingangs genannten Art wird allgemein in der Technik eingesetzt. Ein bevorzugter Verwendungszweck ist die Erzeugung von Fleischmehl, wobei es darauf ankommt, nicht nur einen hohen Zerkleinerungsgrad, sondern auch einen hohen Trocknungsgrad zu erzielen. Eine weitere Verwendung ist die Verarbeitung von ölhaltiger pflanzlicher Biomasse, wobei in diesem Fall das gewünschte Ausgangsprodukt zumindest primär von dem aus der Biomasse herausgepressten Öl gebildet wird.A screw press device of the type mentioned is generally used in technology. A preferred application is the production of meat meal, where it is important not only to achieve a high degree of comminution, but also a high degree of drying. Another use is the processing of oil-containing plant biomass, in which case the desired starting product is formed at least primarily from the oil pressed out of the biomass.
Eine solche Vorrichtung ist beispielsweise aus der
Die
Die
Die
Solange das Material über ausreichende Porosität bzw. Kapillarität verfügt, kann Flüssigkeit ausgepresst werden. Wenn aber der Materialstrom durch ungünstige Umstände entweder eine Geschwindigkeitsüberhöhung (Überströmung) oder eine Geschwindigkeitsabnahme (Unterströmung) erfährt, wird die Flüssigkeitsabgabe gestört. Im ersten Fall der Überströmung findet eine so starke Verdichtung der Oberfläche des Materials statt, dass der Flüssigkeitsaustritt stark behindert oder sogar gestoppt wird; dabei kann durch auftretende Reibung und daraus resultierende Hitze eine Schädigung der Qualität des Pressgutes oder gar dessen Entzündung sowie dadurch auch ein erhöhter Verschleiß von Komponenten der Schneckenpressvorrichtung verursacht werden. Im zweiten Fall der Unterströmung versiegt der Flüssigkeitsablauf ebenfalls, weil nunmehr nicht genügend Kompressionsdruck vorhanden ist, um die Flüssigkeit auszupressen.As long as the material has sufficient porosity or capillarity, liquid can be squeezed out. However, if the material flow experiences either an increase in speed (overflow) or a decrease in speed (underflow) due to unfavorable circumstances, the liquid discharge is disrupted. In the first case of overflow, the surface of the material is compressed to such an extent that the escape of liquid is severely impeded or even stopped; the friction that occurs and the resulting heat can damage the quality of the material to be pressed or even its Inflammation and thereby also increased wear of components of the screw press device are caused. In the second case of underflow, the liquid drain also dries up because there is now insufficient compression pressure to squeeze out the liquid.
Es ist eine Aufgabe der vorliegenden Erfindung, die Effizienz einer Schneckenpressvorrichtung der eingangs genannten Art zu steigern.It is an object of the present invention to increase the efficiency of a screw press device of the type mentioned at the outset.
Diese und ggf. noch weitere Aufgaben werden gelöst mit einer Schneckenpressvorrichtung mit den Merkmalen des Anspruchs 1.These and possibly other tasks are solved with a screw press device with the features of claim 1.
Demnach lassen sich die ersten und zweiten Pressschnecken wahlweise mit unterschiedlichen Drehzahlen antreiben, und zwar mit einem erfindungsgemäßen besonderen Steuerungskonzept, wozu eine entsprechend geeignete Drehzahlsteuerungseinrichtung vorzusehen ist. Das erfindungsgemäße besondere Steuerungskonzept besteht darin, für den ersten Fall, wenn der Druck im Material bzw. Pressgut innerhalb des ersten Schneckengehäuses im Wesentlichen benachbart zum ersten Auslass einen vorbestimmten ersten Schwellwert überschreitet, die zweite Pressschnecke auf eine Drehzahl einzustellen, die über einem ersten Drehzahlwert liegt, und für den zweiten Fall, wenn der Druck im Material bzw. Pressgut innerhalb des ersten Pressschneckengehäuses im Wesentlichen benachbart zum ersten Auslass einen vorbestimmten zweiten Schwellwert unterschreitet, die zweite Pressschnecke auf eine Drehzahl einzustellen, die unterhalb eines zweiten Drehzahlwertes liegt. Dabei macht sich die Erfindung die Erkenntnis zunutze, dass mit zunehmender Drehzahl der Pressschnecke eine geringere Kompression des Materials bzw. Pressgutes und somit auch ein geringerer Zerteilungsgrad und mit abnehmender Drehzahl der Pressschnecke eine höhere Kompression des Materials bzw. des Pressgutes und somit auch ein höherer Zerteilungsgrad erzielt wird. Somit wird im ersten Fall vermieden, dass das Material bzw. Pressgut bereits weit vor dem den Auslass der gesamten Schneckenpressvorrichtung bildenden zweiten Auslass einer für die dortigen Verhältnisse zu hohen Kompression mit der Folge einer erhöhten Reibung und somit Erhitzung und der daraus resultierenden Gefahr einer Schädigung der Qualität des Pressgutes sowie eines erhöhten Verschleißes von Komponenten der Vorrichtung und einer Verstopfung der gesamten Vorrichtung ausgesetzt wird, und bleibt im zweiten Fall gewährleistet, dass das Material bzw. Pressgut nicht zu viskos bleibt, sondern im Laufe seines Weges durch die Schneckenpressvorrichtung einer gewünschten ausreichenden Kompression unterworfen wird. Das erfindungsgemäße Steuerungskonzept sorgt demnach dafür, dass am zweiten Auslass, der ja auch den Auslass der gesamten Schneckenpressvorrichtung bildet, das Material bzw. Pressgut stets mit einer gewünschten, möglichst hohen Kompression mit der Folge austritt, dass möglichst viel Flüssigkeit aus dem Material bzw. Pressgut herausgepresst werden konnte. Demnach führt die erfindungsgemäße Lösung zu einer deutlichen Effizienzsteigerung der Schneckenpressvorrichtung ohne die Gefahr einer Erhöhung des Verschleißes.Accordingly, the first and second press screws can be driven at different speeds, with a special control concept according to the invention, for which purpose a correspondingly suitable speed control device is to be provided. The special control concept according to the invention consists in, for the first case when the pressure in the material or material to be pressed within the first screw housing, essentially adjacent to the first outlet, exceeds a predetermined first threshold value set the second press screw to a speed that is above a first speed value, and for the second case, when the pressure in the material or pressing material within the first press screw housing falls below a predetermined second threshold value, essentially adjacent to the first outlet, the second press screw to a speed set, which is below a second speed value. The invention makes use of the finding that as the speed of the press screw increases, there is less compression of the material or material to be pressed and thus also a lower degree of fragmentation, and with a decreasing speed of the press screw there is greater compression of the material or material to be pressed and thus also a higher degree of fragmentation is achieved. In the first case, this avoids the material or material to be pressed being subjected to compression that is too high for the conditions there, long before the second outlet forming the outlet of the entire screw press device, with the result of increased friction and thus heating and the resulting risk of damage to the quality of the pressing material as well as increased wear of components of the device and clogging of the entire device, and in the second case it is ensured that the material or pressing material does not remain too viscous, but rather has a desired sufficient compression in the course of its path through the screw press device is subjected. The control concept according to the invention therefore ensures that at the second outlet, which also forms the outlet of the entire screw press device, the material or pressed material always exits with a desired compression that is as high as possible, with the result that as much liquid as possible is removed from the material or pressed material could be squeezed out. Accordingly, the solution according to the invention leads to a significant increase in the efficiency of the screw press device without the risk of an increase in wear.
Bevorzugte Ausführungen und Weiterbildungen der Erfindung sind in den abhängigen Ansprüchen angegeben.Preferred embodiments and developments of the invention are specified in the dependent claims.
So soll zweckmäßigerweise der erste Schwellwert gleich dem zweiten Schwellwert sein. Ebenfalls soll zweckmäßigerweise der erste Drehzahlwert gleich dem zweiten Drehzahlwert sein, wobei bevorzugt der erste Drehzahlwert und der zweite Drehzahlwert gleich dem Wert der Drehzahl der ersten Pressschnecke ist.The first threshold should expediently be equal to the second threshold. Likewise, the first speed value should expediently be equal to the second speed value, with the first speed value and the second speed value is equal to the value of the speed of the first press screw.
Somit besteht bei dieser Ausführungsform das erfindungsgemäße Steuerungskonzept darin, die Drehzahl der zweiten Pressschnecke für den ersten Fall, dass der Druck im Material innerhalb des ersten Pressschneckengehäuses im Wesentlichen benachbart zum ersten Auslass einen vorbestimmten Schwellwert überschreitet, auf einen Wert größer als die Drehzahl der ersten Pressschnecke anzuheben, sodass die zweite Pressschnecke schneller als die erste Pressschnecke läuft, und für den zweiten Fall, dass der Druck im Material innerhalb des ersten Pressschneckengehäuses im Wesentlichen benachbart zum ersten Auslass den vorbestimmten Schwellwert unterschreitet, auf einen Wert unterhalb der Drehzahl der ersten Pressschnecke abzusenken, sodass dann die zweite Pressschnecke langsamer als die erste Pressschnecke läuft.Thus, in this embodiment, the control concept according to the invention consists in setting the speed of the second press screw to a value greater than the speed of the first press screw for the first case that the pressure in the material within the first press screw housing essentially adjacent to the first outlet exceeds a predetermined threshold value to be raised so that the second press screw runs faster than the first press screw, and in the second case that the pressure in the material within the first press screw housing falls below the predetermined threshold value essentially adjacent to the first outlet, to a value below the speed of the first press screw, so that the second press screw then runs slower than the first press screw.
Die erfindungsgemässe Schneckenpressvorrichtung zeichnet sich dadurch aus, dass die Drehzahlsteuerungseinrichtung einen Sensor aufweist, der eine physikalische Größe misst, die von der Antriebseinrichtung für den Antrieb der ersten Pressschnecke benötigt wird, wobei die Drehzahlsteuerungseinrichtung die vom Sensor gemessene physikalische Größe als Messgröße für den Druck des Materials innerhalb des ersten Pressschneckengehäuses benachbart zum ersten Auslass verwendet und die zweite Pressschnecke auf eine Drehzahl einstellt, die für den Fall, dass die vom Sensor gemessene physikalische Größe einen vorbestimmten ersten Schwellwert überschreitet, über der Drehzahl der ersten Pressschnecke liegt, und für den Fall, dass die vom Sensor gemessene physikalische Größe einen vorbestimmten zweiten Schwellwert unterschreitet, unterhalb der Drehzahl der ersten Pressschnecke liegt, wobei es sich bevorzugt bei der physikalischen Größe um eine Leistung oder einen elektrischen Strom handelt.The screw press device according to the invention is characterized in that the speed control device has a sensor that measures a physical variable that is required by the drive device for driving the first press screw, the speed control device using the physical variable measured by the sensor as a measured variable for the pressure of the material within the first auger housing adjacent to the first outlet and setting the second auger to a speed greater than the speed of the first auger in the event that the physical quantity measured by the sensor exceeds a predetermined first threshold, and in the event that the physical variable measured by the sensor falls below a predetermined second threshold value, is below the speed of the first press screw, the physical variable preferably being a power output or an electrical current.
Vorzugsweise wird die eine Pressschnecke von einer Hohlwelle angetrieben, durch die sich eine die andere Pressschnecke antreibende Welle erstreckt. Eine solche Maßnahme erlaubt eine einseitige Anordnung der Antriebseinrichtung, welche ja zum rotatorischen Antrieb der Wellen vorgesehen ist, sodass diese Ausführung räumliche Vorteile bietet. Bei einer Weiterbildung dieser Ausführung sind die beiden Pressschnecken und die beiden Wellen koaxial zueinander angeordnet und sitzt die eine Pressschnecke konzentrisch auf der Hohlwelle und die andere Pressschnecke konzentrisch auf einem freiliegenden Abschnitt der von der Hohlwelle abschnittsweise umgebenen Welle. Bei einer weiteren vorteilhaften Weiterbildung dieser Ausführung wird die erste Pressschnecke von der Hohlwelle und die zweite Pressschnecke von der abschnittsweise von der Hohlwelle umgebenen Welle angetrieben. Bei einer weiteren bevorzugten Weiterbildung ist die Antriebseinrichtung an derjenigen Stelle der Vorrichtung, an der sich gemeinsam die Welle und die die Welle umgebende Hohlwelle jeweils mit einem Endabschnitt befindet, und/oder benachbart zum ersten Einlass angeordnet.Preferably, one squeezing screw is driven by a hollow shaft, through which a shaft driving the other squeezing screw extends. Such a measure allows a one-sided arrangement of the drive device, which is provided for the rotary drive of the shafts, so that this embodiment offers spatial advantages. In a further development of this embodiment, the two squeezing screws and the two shafts are arranged coaxially with one another and one squeezing screw sits concentrically on the hollow shaft and the other press screw concentrically on an exposed section of the shaft which is partially surrounded by the hollow shaft. In a further advantageous development of this embodiment, the first squeezing screw is driven by the hollow shaft and the second squeezing screw is driven by the shaft, which is partially surrounded by the hollow shaft. In a further preferred development, the drive device is arranged at that point of the device at which the shaft and the hollow shaft surrounding the shaft are located, each with an end section, and/or adjacent to the first inlet.
Bevorzugt weist die Antriebseinrichtung zwei Antriebsmotoren auf, von denen der eine Antriebsmotor ausgebildet ist, die eine Pressschnecke anzutreiben, und der andere Antriebsmotor ausgebildet ist, die andere Pressschnecke anzutreiben. Bei der zuvor angesprochenen Ausführung mit Hohlwelle und innenliegender Welle ist vorzugsweise der eine Antriebsmotor ausgebildet, die innenliegende Welle im Wesentlichen direkt anzutreiben, und der andere Antriebsmotor ausgebildet, die Hohlwelle im Wesentlichen anzutreiben.The drive device preferably has two drive motors, of which one drive motor is designed to drive one squeezing screw and the other drive motor is designed to drive the other squeezing screw. In the previously mentioned embodiment with a hollow shaft and an internal shaft, one drive motor is preferably designed to drive the internal shaft essentially directly, and the other drive motor is designed to essentially drive the hollow shaft.
Alternativ ist es aber auch beispielsweise denkbar, dass die Antriebseinrichtung einen Antriebsmotor und ein Getriebe, insbesondere ein Planetengetriebe, dessen Übersetzungsverhältnis veränderbar ist, aufweist, wobei der Antriebsmotor ausgebildet ist, die eine Pressschnecke im Wesentlichen direkt anzutreiben, und das Getriebe mit dem Antriebsmotor gekoppelt und ausgebildet ist, die andere Pressschnecke im Wesentlichen direkt anzutreiben, und die Drehzahlsteuerungseinrichtung zur Steuerung des Getriebes durch Änderung von dessen Übersetzungsverhältnis ausgebildet ist.Alternatively, it is also conceivable, for example, for the drive device to have a drive motor and a gear, in particular a planetary gear, the transmission ratio of which can be changed, the drive motor being designed to drive one press screw essentially directly, and the gear being coupled to the drive motor and is designed to drive the other press screw essentially directly, and the speed control device is designed to control the transmission by changing its transmission ratio.
Ebenfalls ist es von Vorteil, einen Antriebsmotor der Antriebseinrichtung so auszubilden, dass von ihr die innen liegende Welle im Wesentlichen direkt angetrieben wird, und das Getriebe so auszubilden, dass von ihr die Hohlwelle im Wesenlichen direkt angetrieben wird.It is also advantageous to design a drive motor of the drive device in such a way that it essentially drives the internal shaft directly, and to design the transmission in such a way that it essentially drives the hollow shaft directly.
Zweckmäßigerweise sollten das erste Pressschneckengehäuse und das zweite Pressschneckengehäuse ein gemeinsames Gehäuse bilden.The first squeezing screw housing and the second squeezing screw housing should expediently form a common housing.
Bei einer weiteren bevorzugten Ausführungsform ist zwischen dem ersten Auslass und dem zweiten Einlass ein Expander bzw. Extruder angeordnet, der ein Gehäuse, eine im Gehäuse drehbar gelagerte Extruderschnecke, einen mit dem ersten Auslass gekoppelten Einlass und einen mit dem zweiten Einlass gekoppelten Auslass aufweist. Ein solcher Extruder bewirkt eine leichte Entspannung des am ersten Auslass komprimierten Materials bzw. Pressgutes. Zweckmäßigerweise sind die beiden Pressschnecken und die Extruderschnecke koaxial zueinander angeordnet. Vorzugsweise verbindet das Gehäuse des Extruders das erste Pressschneckengehäuse mit dem zweiten Pressschneckengehäuse. Bevorzugt ist die Extruderschnecke mit der ersten Pressschnecke drehfest gekoppelt. Des Weiteren ist vorzugsweise die Schneckengangsteigung der Extruderschnecke über ihre Länge konstant. Schließlich kann bevorzugt die Schneckengangsteigung der Extruderschnecke kleiner als die Schneckengangsteigung der Pressschnecken sein, was für den gewünschten Entspannungseffekt von Vorteil ist.In a further preferred embodiment, an expander or extruder is arranged between the first outlet and the second inlet, which expander or extruder has a housing, an extruder screw rotatably mounted in the housing, an inlet coupled to the first outlet and an outlet coupled to the second inlet. Such an extruder causes a slight relaxation of the material or pressed material compressed at the first outlet. The two press screws and the extruder screw are expediently arranged coaxially to one another. Preferably, the barrel of the extruder connects the first press screw barrel to the second press screw barrel. The extruder screw is preferably coupled in a torque-proof manner to the first press screw. Furthermore, the screw pitch of the extruder screw is preferably constant over its length. Finally, the screw pitch of the extruder screw can preferably be smaller than the screw pitch of the extruder screw, which is advantageous for the desired relaxation effect.
Bei einer weiteren bevorzugten Ausführung bildet für mindestens eine der Schneckenpressen das zugehörige Pressschneckengehäuse einen im Wesentlichen über die gesamte Länge der Pressschnecke zylindrischen Hohlraum und weist die Pressschnecke einen stetig monoton bzw. kontinuierlich zunehmenden Kerndurchmesser und eine stetig monoton bzw. kontinuierlich abnehmende Schneckengangsteigung auf. Somit ist es bei dieser Ausführung wesentlich, dass in Arbeitsrichtung der Kerndurchmesser ohne jede Unterbrechung zunimmt und in entsprechender Weise ohne jede Diskontinuierlichkeit die Steigung der Pressschnecke abnimmt. Diese Lösung erlaubt das Auspressen eines noch höheren Anteils an Flüssigkeit aus festen Materialbestandteilen unter gleichzeitiger Herabsetzung der für den Extraktionsvorgang erforderlichen Energie für die Antriebseinrichtung, wodurch sich die Leistung der jeweiligen Schneckenpresse noch weiter erhöhen lässt.In a further preferred embodiment, for at least one of the screw presses, the associated squeezing screw housing forms a cavity that is essentially cylindrical over the entire length of the squeezing screw and the squeezing screw has a steadily monotonically or continuously increasing core diameter and a steadily monotonously or continuously decreasing screw pitch. It is therefore essential in this embodiment that the core diameter increases without any interruption in the working direction and the pitch of the press screw decreases in a corresponding manner without any discontinuity. This solution allows an even higher proportion of liquid to be pressed out of solid material components while at the same time reducing the energy required for the extraction process for the drive device, as a result of which the output of the respective screw press can be increased even further.
Nachfolgend wird ein bevorzugtes Ausführungsbeispiel der Erfindung anhand der beiliegenden Zeichnungen näher erläutert. Es zeigen:
- Fig. 1
- im Wesentlichen im Längsschnitt eine Schneckenpressvorrichtung gemäß einem bevorzugten Ausführungsbeispiel der Erfindung;
- Fig. 2
- eine ausschnittsweise vergrößerteEinzelheit, die in
Fig. 1 durch einen mit "A" gekennzeichneten Kreis markiert ist, im Längsschnitt ( ) und in perspektivischer Seitenansicht (Figur 2aFigur 2b ); und - Fig. 3
- eine Anordnung aus zwei Pressschnecken mit dazwischenliegender Extruderschnecke in perspektivischer seitlicher Ansicht (a) sowie im Längsschnitt (b).
- 1
- substantially in longitudinal section a screw press device according to a preferred embodiment of the invention;
- 2
- a partially enlarged detail, which is shown in
1 is marked by a circle marked "A", in longitudinal section (Figure 2a ) and in perspective side view (Figure 2b ); and - 3
- an arrangement of two press screws with an intermediate extruder screw in a perspective side view (a) and in longitudinal section (b).
Die in
Die erste Schneckenpresse 4 weist ein erstes Pressschneckengehäuse 8, eine im ersten Pressschneckengehäuse 8 drehbar gelagerte erste Pressschnecke 10 mit spiralförmigen Wendeln bzw. Schneckenstegen 10a und sich dazwischen ebenfalls spiralförmig erstreckenden Fördergängen, einen im dargestellten Ausführungsbeispiel als Einlassschacht ausgebildeten ersten Einlass 12 und einen ersten Auslass 14 auf. Das erste Pressschneckengehäuse 8 ist mit Öffnungen 8a versehen und ist gewöhnlich als Seiherkorb ausgestaltet bzw. wird als ein solcher bezeichnet.The first screw press 4 has a first
Die zweite Schneckenpresse 6 weist ein zweites Pressschneckengehäuse 16, eine im zweiten Pressschneckengehäuse 16 drehbar gelagerte zweite Pressschnecke 18 mit spiralförmigen Wendeln bzw. Schneckenstegen 18a und sich dazwischen ebenfalls spiralförmig erstreckenden Fördergängen, einen zweiten Einlass 20 und einen zweiten Auslass 22 auf. Wie das erste Pressschneckengehäuse 8 ist auch das zweite Pressschneckengehäuse 16 perforiert bzw. mit Öffnungen 16a versehen und ist gewöhnlich ebenfalls als Seiherkorb ausgestaltet bzw. wird als ein solcher bezeichnet. Gewöhnlich sind die als Seiherkorb ausgebildeten Pressschneckengehäuse 8, 16 aus zwei Halbschalen oder mehreren schalenförmigen Abschnitten zusammengesetzt; dies ist vorteilhaft, um zum einen einen einfachen Zugang zu der Pressschnecke beispielsweise für Wartungszwecke zu erlauben und andererseits eine einfache Möglichkeit zur Anpassung der Durchlässigkeit des ja als Seiherkorb ausgebildeten Pressschneckengehäuses durch Auswechslung des Pressschneckengehäuses gegen ein Pressschneckengehäuse mit einem anderen Perforationsgrad bzw. einer anderen Anzahl von Öffnungen und/oder Öffnungen mit einem anderen Durchmesser zu schaffen.The
Wie die
Wie
Wie insbesondere
Um die beiden Wellen 34, 36 in Rotation zu versetzen, sind zwei Antriebsmotoren 38, 40 vorgesehen. Im beschriebenen Ausführungsbeispiel werden als Antriebsmotoren, ein Elektromotoren verwendet. Wie
Wie
Die beschriebene Schneckenpressvorrichtung dient dazu, pressfähiges und poröses Material, auch als Pressgut bezeichnet, welches über den ersten Einlass 12 eingegeben wird, stark zu komprimieren mit der Folge, dass im Material vorhandene Flüssigkeit, auch als Filtrat bezeichnet, herausgepresst und das Material in einem trockenen, komprimierten Zustand aus dem zweiten Auslass 22 ausgegeben wird. Somit bildet der erste Einlass 12 der ersten Schneckenpresse 4 auch den Einlass für die gesamte Schneckenpressvorrichtung und der zweite Auslass 22 der zweiten Schneckenpresse 6 den Auslass für die gesamte Schneckenpressvorrichtung zur Abgabe des dann komprimierten Materials bzw. Pressgutes. Um die Flüssigkeit aus dem Material auszutreiben, bedarf es eines stetig wachsenden Pressdruckes auf das betroffene Material. Hierzu sind im dargestellten Ausführungsbeispiel die beiden hintereinandergeschalteten Schneckenpressen 4, 6 vorgesehen, in denen dieser Vorgang mithilfe der kontinuierlich arbeitenden Pressschnecken 10, 18 aufgrund deren Schneckengangsteigung stattfindet. Da die Pressschnecken 10, 18 von dem jeweiligen Pressschneckengehäuse 8, 16 umschlossen ist, das mit Öffnungen oder Perforationen versehen bzw. als Seiher- oder Siebkörper ausgebildet ist, kann die ausgepresste Flüssigkeit nur in eine Richtung zu den Pressschneckengehäusen 8, 16 hin, also von innen nach außen, fließen. Wie die
Während die erste Schneckenpresse 4 den primären Pressvorgang übernimmt, findet mit der nachgeschalteten zweiten Schneckenpresse 6 eine Nachbearbeitung statt. Der zwischen die beiden Schneckenpressen 4, 6 geschaltete Expander 24 bewirkt eine Entspannung des am ersten Auslass 14 austretenden Materials, wodurch das Pressgut aufgebrochen wird und somit porös bleibt. Demnach wirkt der Expander 24 als eine Art Puffer. Hierzu vergrößert sich der von der Innenwandung des ersten Pressschneckengehäuses 8 begrenzte Hohlraum beim Übergang vom ersten Auslass 14 zum Einlass 30 des Expanders 24, was bereits zu einer ersten Entspannung des Pressgutes bei Eintritt in den Expander 24 führt. Wie insbesondere
Wie
Die aus dem Material ausgetriebene und durch die Öffnungen 8a, 16a der Pressschneckengehäuse 8, 16 austretende Flüssigkeit gelangt durch das erste Kompartment 46 aufgrund Schwerkrafteinfluss nach unten und sammelt sich auf bzw. über dem Boden 2a, wo sie dann durch die Wirkung der Filtratentleerungsschnecke 48 zum Filtratauslass 50 getrieben wird. Das final komprimierte Material tritt dagegen aus dem zweiten Auslass 22 der zweiten Schneckenpresse 6 aus und gelangt dabei in das zweite Kompartment 52, wo es aufgrund von Schwerkrafteinfluss nach unten fällt und mithilfe des Schaufelrades 54 durch einen in den Zeichnungen nicht dargestellten Auslass gefördert wird, der auch als sog. Schilferaustritt bezeichnet wird.The expelled from the material and through the
Der Material- bzw. Volumenstrom wird durch die Drehzahl und die Schneckengangsteigung der Pressschnecken 10, 18 bestimmt und ist auch noch von weiteren unterschiedlichen Einflüssen abhängig. Solange das Material über ausreichende Porosität bzw. Kapillarität verfügt, kann Flüssigkeit ausgepresst werden. Wenn aber der Materialstrom durch ungünstige Umstände entweder eine Geschwindigkeitsüberhöhung (Überströmung) oder eine Geschwindigkeitsabnahme (Unterströmung) erfährt, wird die Flüssigkeitsabgabe gestört. Im ersten Fall der Überströmung findet eine so starke Verdichtung der Oberfläche des Materials statt, dass der Flüssigkeitsaustritt stark behindert oder sogar gestoppt wird; dabei kann durch auftretende Reibung und daraus resultierende Hitze eine Schädigung der Qualität des Pressgutes oder gar dessen Entzündung sowie dadurch ein erhöhter Verschleiß von Komponenten der Schneckenpressvorrichtung verursacht werden. Im zweiten Fall der Unterströmung versiegt der Flüssigkeitsablauf ebenfalls, weil nunmehr nicht genügend Kompressionsdruck vorhanden ist, um die Flüssigkeit auszupressen.The material or volumetric flow is determined by the speed and the screw pitch of the press screws 10, 18 and is also dependent on other different influences. As long as the material has sufficient porosity or capillarity, liquid can be squeezed out. However, if the material flow experiences either an increase in speed (overflow) or a decrease in speed (underflow) due to unfavorable circumstances, the liquid discharge is disrupted. In the first case of overflow, the surface of the material is compressed to such an extent that the escape of liquid is severely impeded or even stopped; the friction that occurs and the resulting heat can damage the quality of the material to be pressed or even cause it to ignite, and this can result in increased wear of the components of the screw press device. In the second case of underflow, the liquid drain also dries up because there is now insufficient compression pressure to squeeze out the liquid.
Um diese nachteiligen Effekte zu vermeiden, lassen sich durch die Antriebsmotoren 38, 40 die beiden Pressschnecken 10, 18 wahlweise mit unterschiedlichen Drehzahlen antreiben und ist des Weiteren eine Drehzahlsteuerungseinrichtung 60 vorgesehen, an die die Antriebsmotoren 38, 40 angeschlossen sind. Sofern an anstelle des zweiten Antriebsmotors 40 ein Getriebe verwendet wird, ist dieses so auszubilden, dass sich dessen Übersetzungsverhältnis verändern lässt, und zwar durch die Drehzahlsteuerungseinrichtung 60. Des Weiteren ist die Drehzahlsteuerungseinrichtung 60 so ausgebildet, dass sie über einen Sensor 62 die vom ersten Antriebsmotor 38 für den Antrieb der ersten Pressschnecke 10 benötigte Leistungsaufnahme oder einen entsprechend benötigten elektrischen Strom misst. Die so gewonnene Messgröße wird dann von der Drehzahlsteuerungseinrichtung 60 zur Ermittlung des Druckes des Materials innerhalb des ersten Pressschneckengehäuses 8 benachbart zum ersten Auslass 14 entsprechend ausgewertet. Das Steuerungskonzept der Drehzahlsteuerungseinrichtung 60 besteht nun darin, die Antriebsmotoren 38, 40 oder zumindest den zweiten Antriebsmotor 40 so anzusteuern, dass die Drehzahl der zweiten Pressschnecke 18 für den ersten Fall, wenn der Druck im Material innerhalb des ersten Pressschneckengehäuses 8 benachbart zum ersten Auslass 14 einen vorbestimmten Schwellwert überschreitet, auf einen Wert größer als die Drehzahl der ersten Pressschnecke 10 angehoben wird, sodass die zweite Pressschnecke 18 schneller als die erste Pressschnecke 10 läuft, und für den zweiten Fall, wenn der Druck im Material innerhalb des ersten Pressschneckengehäuses 8 im Wesentlichen benachbart zum ersten Auslass 14 den vorbestimmten Schwellwert unterschreitet, auf einen Wert unterhalb der Drehzahl der ersten Pressschnecke 10 abgesenkt wird, sodass dann die zweite Pressschnecke 18 langsamer als die erste Pressschnecke 10 läuft.In order to avoid these disadvantageous effects, the two press screws 10, 18 can be driven selectively at different speeds by the
Claims (16)
- Screw press device havinga first screw press (4), which has a first press screw housing (8), a first press screw (10) that is rotatably mounted in the first press screw housing (8), a first inlet (12) and a first outlet (14), at least one second screw press (6), which has a second press screw housing (16), a second press screw (18) that is rotatably mounted in the second press screw housing (16), a second inlet (20) that is coupled to the first outlet (12) and a second outlet (22),and a drive device (38, 40) for the rotational drive of the first and second press screws (10, 18), which is designed to drive the first and second press screws (10, 18), optionally at different rotational speeds, characterised in that the screw press device has a rotational speed control device (60),which has a sensor (62),which measures a physical quantity that is required by the drive device (38, 40) for driving the first press screw (10),wherein the physical quantity is a power or an electrical current, andthe rotational speed control device (60) uses the physical quantity measured by the sensor (62) as a measure of the pressure of the material inside the first press screw housing (8) adjacent to the first outlet (14) and sets the second press screw (18) to a rotational speed at which, in the case that the physical quantity measured by the sensor (62) exceeds a predetermined threshold value above the rotational speed of the first press screw (10), and in the case that the physical quantity measured by the sensor (62) falls below the predetermined threshold value below the rotational speed of the first press screw (10), the second press screw (18) then runs slower than the first press screw (10).
- Device according to claim 1, wherein the one press screw (10) is driven by a hollow shaft (36), through which a shaft (34) driving the other press screw (18) extends.
- Device according to claim 2, wherein the two press screws (10, 18) and the two shafts (34, 36) are arranged coaxially with each other and one press screw (10) sits concentrically on the hollow shaft (36) and the other press screw (18) sits concentrically on an exposed section of the shaft (34) partially surrounded by the hollow shaft (36).
- Device according to claim 2 or 3, wherein the first press screw (10) is driven by the hollow shaft (36) and the second press screw (18) is driven by the shaft (34) that is partially surrounded by the hollow shaft (36).
- Device according to at least one of claims 2 to 4, wherein the drive device (38, 40) is arranged at that position of the device at which the end sections of both the shaft (34) and the hollow shaft (36) surrounding the shaft (34) are respectively located, and/or is arranged adjacent to the first inlet.
- Device according to at least one of the preceding claims, wherein the drive device has two drive motors (38), (40), of which one drive motor (38) is designed to drive one press screw (10), and the other drive motor (40) is designed to drive the other press screw (18).
- Device according to at least one of claims 2 to 5 as well as according to claim 6, wherein one drive motor (38) is designed to drive the internal shaft (34) essentially directly, and the other drive motor (40) is designed to drive the hollow shaft (36) essentially directly.
- Device according to at least one of claims 1 to 5, wherein the drive device has a drive motor and a gear, in particular a planetary gear, the transmission ratio of which is adjustable, wherein the drive motor is designed to drive one press screw (10) essentially directly, and the gear is coupled with the drive motor and is designed to drive the other press screw (18) essentially directly, and the rotational speed control device is designed to control the gear by changing its transmission ratio,
- Device according to claim 8 as well as at least one of claims 2 to 5, wherein the drive motor is designed to drive the internal shaft (34) essentially directly, and the gear is designed to drive the hollow shaft essentially directly.
- Device according to at least one of the preceding claims, wherein the first press screw housing (10) and the second press screw housing (18) form a common housing.
- Device according to at least one of the preceding claims, wherein an extruder (24) is arranged between the first outlet (14) and the second inlet (20), which extruder (24) has an extruder housing (26), an extruder screw (28) rotatably mounted in the extruder housing (26), an inlet (30) coupled to the first outlet (14), and an outlet (32) coupled to the second inlet (20).
- Device according to claim 11, wherein the two press screws (10, 18) and the extruder screw (28) are arranged coaxially to each other.
- Device according to claim 11 or 12, wherein the extruder housing (26) connects the first press screw housing (8) with the second press screw housing (16).
- Device according to at least one of claims 11 to 13, wherein the extruder screw (28) is coupled non-rotatably with the first press screw (10).
- Device according to at least one of claims 11 to 14, wherein the screw pitch of the extruder screw (28) is constant across its length and/or is smaller than the screw pitch of the press screws (10, 18).
- Device according to at least one of the preceding claims, wherein the press screw housing (8, 16) forms a hollow space that is essentially cylindrical across the whole length of the press screw (10, 18) for at least one of the screw presses (4, 6) and the press screw (10, 18) has a consistently monotonically or continuously increasing core diameter and a consistently monotonically or continuously decreasing screw pitch.
Applications Claiming Priority (2)
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DE202015004496 | 2015-06-19 | ||
PCT/EP2016/063852 WO2016202911A1 (en) | 2015-06-19 | 2016-06-16 | Screw press device |
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EP3310566A1 EP3310566A1 (en) | 2018-04-25 |
EP3310566C0 EP3310566C0 (en) | 2023-06-07 |
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CN108297471B (en) * | 2018-01-23 | 2024-02-20 | 北京工商大学 | Automatic clearance presses spiral oil press of arranging |
CN110936647A (en) * | 2018-09-21 | 2020-03-31 | Cbc株式会社 | Solid-liquid separation device |
CN109291488A (en) * | 2018-10-12 | 2019-02-01 | 北京晟智科技发展有限公司 | A kind of self-adjustable waste pressurizing unit |
CN112373113B (en) * | 2020-09-30 | 2022-09-13 | 合升翔液压技术(武汉)有限公司 | Energy-saving hydraulic press control system |
CN114311828B (en) * | 2022-01-11 | 2024-02-27 | 吉林嘉美食品有限公司 | Su seed oil extraction device |
CN118721837B (en) * | 2024-09-04 | 2024-11-01 | 吉林医药学院 | Squeezing device and hazelnut oil extraction method |
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JPS5832599A (en) * | 1981-08-21 | 1983-02-25 | Ebara Infilco Co Ltd | Screw press type hydroextractor |
JPS61132299A (en) * | 1984-11-30 | 1986-06-19 | Kurita Mach Mfg Co Ltd | Screw press |
JPS61245999A (en) * | 1985-04-23 | 1986-11-01 | Kurita Mach Mfg Co Ltd | Control device for screw press |
DE19601128C2 (en) | 1996-01-13 | 1999-07-22 | Ibg Monforts Gmbh & Co | Screw press |
DE29820464U1 (en) | 1998-11-16 | 1999-01-28 | Pro-Technik-Konstruktionen GmbH, 86159 Augsburg | Screw press |
DE29901683U1 (en) | 1999-02-01 | 1999-05-27 | Heissenberger & Pretzler Ges. M.B.H., Frohnleiten | Screw press |
CA2541737C (en) * | 2003-10-15 | 2011-03-08 | Nordic Water Products Ab | Apparatus and method for treating sludge |
DE202007008072U1 (en) | 2007-06-08 | 2008-10-23 | Hasenbein, Günter, Dipl.-Ing. | Snail of a screw press |
US9358484B2 (en) * | 2012-03-19 | 2016-06-07 | Purfil Aps | Rotating separator |
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2016
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EP3310566B8 (en) | 2023-08-16 |
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