The invention relates to a stuffing screw for an extruder system and to an extruder system having such a stuffing screw.
Extruders serve for producing strands from formable materials, wherein, within the extruder, the materials are mixed, often plasticated and driven out of a nozzle under high pressure in order for the material strands to be generated.
Extruders can be differentiated basically into two types, which differ in terms of the process principles. Processing extruders serve predominantly for shaping purposes (usually single shaft extruders), whereas compounding extruders serve for the chemical and/or physical modification (reacting, mixing, degassing, etc.) of substances (double-shaft extruders with shafts closely intermeshing and running in the same direction, Buss kneaders, etc.).
Stuffing screws (also providing a holding-down function) are used as secondary subassemblies on an extruder. The stuffing screws are basically conveying screws. These are used predominantly for two purposes. On the one hand, said stuffing screws serve to meter a product or additives into the extruder. On the other hand, stuffing screws also prevent product discharge from the extruder at extruder-housing openings which serve, for example, for ventilating or degassing purposes.
In the case of degassing in an extruder, the vapors and gases separated oft (the so-called vapor flow) have to be extracted from the product space. It is often the case here that very high gas speeds prevail. Moreover, product particles are produced in the case of degassing in the extruder as a result of the expansion and of foaming of the materials. This effect occurs particularly in the case of the degassing of highly viscoelastic materials, in particular elastomers. The resulting product particles can have a wide range of sizes, which can regularly extend from <0.1 mm up to a number of millimeters. As a result of the high gas speeds, the product particles can be discharged from the extruder with the vapor flow. Using a stuffing screw in the degassing opening, then, on the one hand prevents blockage of the degassing opening. On the other hand, the stuffing screw serves to separate off entrained product particles from the vapor flow. This is intended to protect downstream subassemblies, e.g. separators, extraction systems, vacuum systems or condensate systems, against deposits of product. Otherwise, a pronounced discharge of product particles into the downstream subassemblies would result in, for example, separators having to be frequently cleaned, vacuum pumps being damaged or condensate systems becoming blocked and thus suffering a loss in efficiency.
In tests for degassing rubber, it has been found that a large quantity of product particles is discharged despite the stuffing screws. Closer observations have shown that, as a result of the high gas speeds in the threads of the stuffing screw, the product particles, rather than adhering to the profile flanks or to the housing of the stuffing screw, are thrown back from the wads. In the case of viscoelastic materials, e.g. rubber, being handled, this effect is intensified by the high level of elasticity of the particles. The adhesion forces are then not large enough to overcome the rebound effect.
Proceeding from this prior art, the object of the invention was to improve the function of a stuffing screw, in particular in the case of degassing in an extruder. In particular, a discharge of product particles via the stuffing screw should be reduced.
This object is achieved by the subjects of the independent patent claims. Advantageous embodiments form the subject matter of the respective dependent patent claims and can be gathered from the following description of the invention.
The invention was based on the idea of reducing a discharge of product particles via the stuffing screw in that in the first instance said product particles are separated off from the vapor flow and then the separated-off product particles are agglomerated. The intention is then for the agglomerated product particles to be guided back into the extruder or discharged from the extruder system in a reliable manner, i.e. not via the venting system which adjoins the stuffing screw.
This basic idea of the invention is implemented according to the invention in that a stuffing screw which is intended for an extruder and comprises at least one housing and at least one conveying screw, which is mounted in a rotatable manner within the housing, wherein a conveying space is formed between an inner side of the housing and the conveying screw, has at least one portion of the inner side of the housing provided with one or (preferably) more depressions.
“Depressions” according to the invention are considered to be those which have a dosed base, as a result of which they are distinguished from openings such as are also present as functional openings in conventional stuffing screws.
It is possible for the depressions to be of any desired cross-sectional shape and to be provided in organized or non-organized form in the inner side of the housing
The depressions ensure that low-gas-speed stagnation zones are produced on the inner side of the housing. The speed of the product particles entrained by the gas decreases in these stagnation zones, and this makes it possible for particles to be is deposited in the groove. The depressions also have the advantage that the product particles can agglomerate therein. The agglomerates are then no longer entrained by the gas flow and can either be conveyed back into the extruder or discharged in a reliable manner.
It is particularly preferable for the depression(s) to be designed in the form of a (at least one groove).
“Groove” is understood, according to the invention, to be a depression which is located on the inner side of the housing and of which the length is preferably greater, and in particular a number of times greater, than its width.
Provision may be made for the depressions or the groove to be provided over (essentially) the entire length of the inner side of the housing. It may also be advantageous, however, for the depressions or the groove to be provided just in one or more portions of the inner side of the housing. Interrupting a groove can ensure further disruption of the gas flow, said disruption helping to separate off entrained product particles. It is possible for the depressions or the plurality of grooves in the various portions to be of the same shape (groove progression, groove width, groove cross section) or else to be designed differently. In the case of a continuous groove, provision may likewise be made for the groove shape to be of constant or variable design.
In a preferred embodiment of the stuffing screw according to the invention, provision may be made for the groove to run (essentially) parallel to the longitudinal axis of the stuffing screw. This is a straightforward and therefore relatively cost-effective possible realization. A parallel progression of the groove, however, can also be distinguished by agglomerates which are formed in the grooves being removed to particularly good effect.
Provision may particularly preferably be made, however, for the groove to run helically.
Provision can then preferably be made for the direction of pitch (right-hand pitch, left-hand pitch) of the groove to be counter to the direction of pitch of a (at least one) helically running thread of the conveying screw. It is particularly preferably possible is here to provide an angle ranging from 70° to 110° between the groove and the thread (as seen in relation to the longitudinal direction of the conveying screw). This can have the advantage that a main direction of flow of the gas flow in the thread is (more or less) perpendicular to the groove, and this helps to separate off the product particles. Furthermore, the task of conveying the agglomerates out of the grooves can be improved as a result.
An alternative embodiment can provide for the direction of pitch of the thread and of the groove to be identical. This means that the groove and the thread run more or less parallel. In particular in a combination with a triangular cross section of the groove, this arrangement can have the advantage that agglomerates can be conveyed out of the grooves to particularly good effect as a result of which the risk of “caking” or of the groove gradually “blocking up” is reduced.
Of course, it is also possible to combine the two alternatives, in order then to provide at least two helically running grooves which have opposite directions of pitch and therefore cross over. This makes it possible to achieve a combination of the advantages of the two groove progressions.
Provision may &so be made for the pitch of the groove to be non-uniform, i.e. for it not to be constant. In the case of at least two helical grooves, it is also possible for the individual grooves to have different pitches and different numbers of windings.
The configuration of a stuffing screw according to the invention improves, in particular, the task of separating off product particles from the gas flow when use is made of the stuffing screw for degassing an extruder of an extruder system, and therefore provision is preferably made for the stuffing screw or the housing thereof to have at least one degassing outlet, to which can be connected a degassing system with the components which are known from the prior art. However, the configuration of the stuffing screw according to the invention also has an advantage in terms of conveying material, and therefore said stuffing screw is also advantageously suitable for use for metering material into the extruder.
An extruder system according to the invention comprises at least one extruder and at least one stuffing screw as have been described above. The extruder comprises at least one extruder housing and an (at least one) extruder screw, which is mounted in a rotatable manner in the extruder housing. The stuffing screw adjoins the extruder preferably in a transverse direction and particularly preferably in a perpendicular direction, as seen in relation to the longitudinal axis of the extruder.
The extruder may be any known type of extruder, in particular in the form of single-shaft extruders, double-shaft extruders (with shafts rotating in the same direction or opposite directions and meshing or not meshing), multi-shaft extruders (e.g. ring extruders), planetary roller extruders and co-kneaders with an axially oscillating shaft. The extruder may likewise be in the form of any desired design of kneader (even a large-volume one) with one or more shafts. It is preferred, however, for the extruder to be configured in the form of a single-shaft extruder or a double-shaft extruder with shafts rotating in the same direction.
The stuffing screw according to the invention is also suitable, in particular, for degassing highly viscoelastic material, in particular an elastomer (e.g. rubber), conveyed in an extruder.
The invention will be explained in more detail hereinbelow with reference to exemplary embodiments illustrated in the drawings, in which:
An extruder system according to the invention has an extruder 1 and at least one stuffing screw 2 connected thereto. The extruder 1 comprises an extruder screw 3, which is mounted in an extruder housing 4 so as to be driven in rotation by a drive (not illustrated). The stuffing screw 2 comprises a conveying screw 5, which is mounted in a housing 7 so as to be driven in rotation by a drive 6. It is possible for the extruder 1 to have, for example, a single extruder screw 3 and for the stuffing screw 2 to have a single conveying screw 5, as is illustrated by way of example in
The stuffing screw 2 of an extruder system according to the invention may be provided as a feeding mechanism, via which a product and/or one or more additives are/is fed to the product already located in the extruder 1.
The stuffing screw 2 may also be provided for the purpose of degassing the extruder 1 (cf.
In the annular product space formed between the extruder screw(s) 3 and the extruder housing 4, the product is transported in the direction denoted by the arrow 12, and possibly mixed, plasticated and compressed in the process, by the rotation of the extruder screw(s) 3, designed with helically running threads 11. The inner volume of the extruder housing 4 and the inner volume of the housing 7 of the stuffing screw 2 are connected to one another, and therefore a product which is fed via the stuffing screw 2 can be introduced into the extruder 1 and gas which has formed in the extruder 1 can be discharged via the stuffing screw 2.
The stuffing screw 2 can be connected to the extruder 1 in any desired orientation.
Should a plurality of stuffing screws 2 be combined on an extruder 1, then they can be provided at different axial positions as seen in relation to the longitudinal axis of the extruder 1. It is also possible for a plurality of stuffing screws 2 to be arranged is with different radical orientations at one axial position of the extruder 1 (cf,
In the case of the embodiment of
In contrast to this, the embodiment of
1 Extruder
2 Stuffing screw
3 Extruder screw
4 Extruder housing
5 Conveying screw
6 Drive
7 Housing
8 inlet
9 Outlet
10 Extraction system
11 Thread
12 Transporting direction
13 Groove
14 Thread
15 Longitudinal axis
Number | Date | Country | Kind |
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15154095.2 | Feb 2015 | EP | regional |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2016/051220 | 1/21/2016 | WO | 00 |