DE102006063021B3 - Planetary roller extruder - Google Patents

Abstract

Extruder with at least one planetary roller part for degassing volatile materials, consisting of several interconnected modules (1, 2, 3), preferably with modules whose housings are provided at the ends with flanges (12, 13) and at the flanges ( 12, 13) are connected to each other, wherein the extruder pressure measuring points and / or temperature measuring points, wherein the housing are provided with a tempering, wherein the planetary roller part of a rotating central spindle (6), several to the central spindle (6) encircling Planet spindles (8) and a housing with internal toothing or a housing with an internally toothed bushing (14,15), wherein the planetary spindles (8) with the central spindle (6) and with the internal toothing of the housing or the internally toothed socket (14,15) comb the housing, wherein the planetary spindles (8) in the axial direction by a stop ring (20) are held in at least one intermediate ring (21, 22) lower is partially held, which in turn is at least partially disposed in the melt outlet side flange of the planetary roller extruder part housing and the flange of the corresponding module, wherein the intermediate ring (21, 22) surrounding the central spindle (6) leaving a passage gap for the melt, characterized in that the intermediate ring is additionally provided with a temperature control, wherein for temperature control in the extruder longitudinal direction and / or transversely thereto channels are guided through the intermediate ring, wherein the channels are guided past existing openings for the pressure measurement and / or the temperature measurement.

Description

The invention relates to a planetary roller extruder.

Extruders are used in particular for plastics processing. The plastic is usually used in the form of granules and plasticized by the extruder and discharged into a nozzle that brings the plasticized plastic in a desired shape.

Beyond plasticizing, the task of the extruder is to homogenize the melt. In most cases, additives and surcharges must be processed. This can also be done in the extruder. In this case, the extruder has the task of evenly distributing additives and additives.

Extruders are also used in the food industry and in chemistry.

Extruders come in different designs. Single-screw extruders, twin-screw extruders and planetary roller extruders are known.

Planetary roller extruders have an extremely large plasticizing effect in relation to the other extruders mentioned. This opens up the possibility of processing raw materials that are not or only insufficiently usable in the other extruders. However, planetary roller extruders can also be used to significantly increase production capacity.

Planetary roller extruders have a rotating central spindle, thus combing and rotating planetary spindles, which mesh with an internal toothing in the surrounding housing at the same time. The surrounding housing has a double jacket in contemporary training. The inner jacket is formed by a bushing. Between the inner and outer sheath, the important cooling of the planetary roller extruder is provided.

The bush is provided with the internal toothing. With her, the rotating planetary spindles mesh.

The planetary spindles require no guidance in the circumferential direction. The toothing ensures that the distance between the planetary spindles in the circumferential direction remains the same. It can be spoken of an own leadership.

In the axial direction, it requires an external guide, because the planetary spindles develop a more or less large pressure in the longitudinal direction. This pressure is the reaction pressure from the conveying action of the planetary spindles. The pressure is absorbed by a stop ring on which the planetary spindles glide.

In the following, we will always speak only of starter rings, although in an extruder with several planetary roller modules for the stop rings of the different modules, different designations, e.g. Thrust ring and start-up intermediate ring, are common.

All extruders have in common that in the melt or in the feed / treated gaseous components can occur. These may be ingredients that were undesirable from the start. Such ingredients may e.g. Be water. Some thermoplastics or fillers absorb water. Either these thermoplastics or fillers must be pre-dried, or the resulting steam in the extruder must be removed, degassed.

Gaseous constituents which are desirable at the beginning and undesirable in the further processing operation may be solvents, reaction accelerators or reaction inhibitors or inert gases. Insofar as no complete chemical conversion of these gases takes place, residues remain with monomers, oligomer decomposition products and decomposition products.

• Verbesserung der Produktqualität, Vermeidung gesundheitlicher Schädigung
• Verringerung der Kosten
• Verhindern eines chemischen Abbaus
• Durchführung weiterer Verfahrensschritte

Volatile constituents in the melt often amount to more than 3 to 4% by weight and, in extruded polymers, may usually not exceed 0.2% by weight. There are several reasons that force you to degas. This includes:

• Improvement of product quality, prevention of damage to health
• Reduction of costs
• Preventing chemical degradation
• Carrying out further process steps

For degassing different devices are offered. In most cases, the degassing is carried out on the extruder. First, a degassing zone is defined on the extruder. The following zones are known in the extruder:

Feed zone, compression zone, first plasticization and homogenization zone and decompression zone, second plasticization and homogenization or dispersion zone, cooling zone, discharge zone. The description of the different zones explains their function. Thus, the feed is drawn into the feed zone in the extruder and compressed in the compression zone. In the plasticizing zone, plasticization of the material takes place, in the homogenizing zone, homogenization of the material in the dispersion zone, distribution of additives and / or other substances, such as fillers in the material, cooling in the cooling zone, etc. The zone classification above applies to single-screw extruders or twin-screw extruder. In the planetary roller extruders usually the plasticizing and homogenizing zone is summarized.

For degassing various solutions are offered. All solutions are based on the fact that the dissolved in the melt volatiles are released by pressure reduction. The pressure drop may be at ambient pressure or at an overlying pressure. Inevitably, the gas then dissolves from the melt. The gas bubbles can then be removed.

As a gas outlet is already provided in the region of the pressure drop opening on the jacket / housing of the extruder, which is optionally connected to a suction line.

In cascade extruder systems or tandem extruder systems, the degassing usually takes place between the primary part and the secondary part.

During operation, the degassing zone is a relatively sensitive zone. Here it is important to achieve the best possible separation of gas and melt or of gas and feedstock. The DE19518255A1 Proposes to apply the degassing zone in the region of the junction between two planetary roller extruder modules. The modules primarily fulfill other tasks according to the older proposal. Each module forms a planetary roller extruder unit with central spindle, revolving planetary spindles and a housing. The housings of the modules are provided with a flange at the ends, so that the modules can be connected to each other at the flanges. The thrust rings are positioned in the area of the flanges.

The modules are selected so that there is a connection point with a starting ring at the desired degassing point.

The document nevertheless recommends a degassing between the modules on the sliding ring of the planetary spindles.

The degassing is based on the knowledge that the volatile components are released by pressure reduction. Also the DE19518255A1 makes use of that. In this case, there is a reduction of the melt pressure after passing through the gap zwiscshen stop ring and central spindle and degassing. The gap is designed for the respectively desired pressure gradient.

The invention has also taken on the task of facilitating the interpretation of the respective correct pressure gradient when the thrust ring is at least partially held with at least one intermediate ring, which in turn at least partially disposed in the melt outlet side flange of the planetary roller extruder part housing and the flange of the corresponding module is, wherein the intermediate ring surrounds the central spindle and release of a passage gap for the melt.

According to the invention, this is with the features of the claim 1 reached.

At the same time, baffle plates are provided in the area of the thrust rings, so that the melt / feedstock / material to be treated passes, after passing through the baffle plate, from a zone of higher pressure into one Zone of lower pressure. The zone of lower pressure lies in the conveying direction of the extruder behind the baffle plate.

Such a technique is not found in the DE 37 39 135 A1 or in the DE 43 10 966 A1 , The DE 37 39 135 A1 does not show a tempered contact ring. From this document, only a planetary roller extruder for the preparation of PVC or the like is taken. The melt is discharged from a delivery end of the extruder. At the end of the extruder there is a stop ring. The thrust ring has fixed blades for dividing the melt stream, but no tempering.

These DE 4310966A1 describes a degassing extruder with a single screw. The degassing extruder should have a throttle device with an annular gap which can be varied in the flow cross section between the inlet cylinder and the outlet cylinder. The throttle device is formed by a worm collar, which acts against a shoulder in the housing.

The degassing cylinder is to serve to compress a slurry-shaped mixture of plastics and aggregates and to degas this case.

How the degassing takes place in detail is not explained.

Typically, degassing takes place differently at the single-screw extruder, namely by changing the screw flight or the screw geometry. With this change, the pressure is lowered. It can be produced on the single-screw extruder virtually at any desired point, a pressure drop and a degassing be made. This requires no separate degassing extruder.

It is also popular to perform a degassing on tandem systems between primary extruder and secondary extruder.

Unusual is also a throttle device on the extruder.

The lower pressure is achieved by a zone of low pressure effect. This can e.g. be achieved by interruptions of the teeth of the planetary spindles. An area without pressure effect can be achieved in that the planetary spindles in the zone have no teeth or that a volume expansion arises from the fact that the planetary spindles start at some distance from the baffle plate. The distance depends on the diameter. Diameter is the pitch circle diameter of the internal teeth of the housing in a planetary roller extruder. The distance can be up to 200 mm and in extreme cases more. It is advantageous if not all planetary spindles have the distance and at least one of the planetary spindles has a small distance, e.g. at most 10mm.

This serves to keep the degassing opening in the thrust ring free. An undesirable material build-up in front of the degassing opening is prevented.

Although is also from the DE 2521774A1 an extruder with baffle plates known. However, this does not give any gap adjustment.

According to an older proposal, the planetary spindles are alternately short / long. There is also another alternate or non-uniform change of "short" and "long" into consideration, e.g. "Short-short-long" or "short-shorter-even shorter".

For degassing, the pressure gradient in front of and behind the thrust ring is essential. Preferably, the pressure gradient is adjusted by changing the passage gap on the thrust ring. The change takes place according to the invention viscosity-dependent. This optionally includes the reference to reference quantities. That is, it can be done on the basis of existing gap widths to certain melt viscosities, an adjustment of the gap widths to other melt viscosities by calculation or estimation. In this case, reaching the optimum gap width with the first setting is generally not mandatory or is usually a correction adjustment possible. As a result, the correct gap width can be adjusted with little effort on the way.

Preferably, the passage gap is conical. The gap adjustment can be achieved by adjusting the central spindle in the axial direction. The axial adjustment of the central spindle can be done hydraulically or mechanically. Both adjustments can be stepless, so that the pressure gradient also is infinitely variable. In practice, the optimum central spindle positions are quickly found for each material and operating condition of the extruder.

Optionally, a stepwise adjustment is provided.

For the degassing may be sufficient if only openings are present through which the released gas can escape.

By applying an induced draft, the degassing performance is significantly increased.

The degassing is preferably carried out through the stop ring, preferably also by applying a negative pressure to the melt pressure at the stop ring. The negative pressure is referred to below as vacuum and is adapted to the respective melt viscosity, the gas and the desired treatment of the melt. Optionally, a vacuum dome is used to generate the negative pressure application. The vacuum dome has a considerable volume. A vacuum is applied to the vacuum dome. The large volume of the dome contributes to the operational safety of the degassing and to the selectivity of the degassing.

The negative pressure in the vacuum dome is preferably generated by means of a pump. The suction pump can also be connected directly to the degassing line.

The degassing acts beyond the immediate space behind the stop ring also into the material captured by the spindles and forced in the conveying direction until the compression of the material prevents further degassing. It is particularly beneficial for the degassing, if the number of planetary spindles is less than normal. The number of planetary spindles depends on the diameter. With diameter of the pitch circle diameter of the internal teeth on the housing of the planetary roller extruder is designated. The following shows the normal planetary spindle numbers depending on the diameter and the spindle length: diameter Planet number of spindles length 70 to 100 mm 6 to 8 up to 700 mm 120 to 170 mm 8 to 10 up to 1000 mm 180 mm 9 to 11 up to 1000 mm 200 mm 10 to 12 up to 1000 mm 250 mm 13 to 15 up to 1000 mm 300 mm 17 to 19 up to 1000 mm 400 mm 23 to 25 up to 1200 mm

According to the older proposal, preferably at least 3 planetary spindles are used less for degassing than for normal spindle numbers.

This results in a relatively large distance between the planetary spindles, in which the material can degas for a relatively long time.

The smaller the number of planetary spindles, the larger the distance becomes.

At least the planet spindle number is 3 to ensure central centering of the central spindle.

With respect to this material, as long as degassing is still taking place, there is a form of backward degassing because the gas is withdrawn backward with respect to the conveying action of the extruder.

Optionally, a multi-stage degassing occurs.

Particularly favorable conditions arise when a vertical extruder is used. In the vertical extruder is formed by the gravity of the melt / feed / treated good behind the stop ring a very beneficial degassing cavity by ensuring at the same time by appropriate extruder throughput that the inflowing melt / feed / treated good the cavity fills. The gas is in the vertical arrangement of the least resistance to leakage from the melt and out of the extruder.

The extruder with degassing and in particular with temperature control can also be used for a thin-film evaporation. The resulting vapor is withdrawn as described above.

At the same time, the melt is forcibly rolled out very thinly, so that an extreme surface is created, which is very conducive to evaporation. The thin-film evaporation of conventional type is known as a falling-film evaporator or as a centrifugal evaporator.

In the falling-film evaporator liquids are brought into a falling motion. The disadvantage is the speed of the fall movement. To ensure a sufficient treatment time, either extremely long fall paths must be generated or the liquid must be recycled again and again. The method also fails with melts of slightly higher viscosity than with a liquid.

In the centrifugal evaporator, the liquid is distributed in a centrifuge on the inner shell. With the centrifuge, the problem of residence time can be solved. The centrifuge fails even with higher viscosity melts.

• a)zum Konzentrieren vom Flüssigprodukten und Schmelzen
• b)zum Konzentrieren von viskosen bzw. strukturviskosen Medien
• c)zum Abdestillieren

The extruder with the degassing according to the invention can be used

• a) for concentrating liquid products and melting
• b) for concentrating viscous or pseudoplastic media
• c) for distilling off

Optionally, the extruder with the degassing according to the invention is also used to first mix a reaction phase in the melt and then to deduct resulting gases. The reaction phase can be solid, liquid or gaseous. The extruder ensures optimal mixing.

It is also known to give the stop ring the task of material supply and / or to use the run-up ring as a measuring point for pressure or temperature.

The entry possibility for material can have special meaning in different cases. For the production of plastic foam, it has meanwhile become common to inject blowing agent after the plasticization of the plastic in the extruder, to mix with the melt and to keep under a foaming of the melt preventing pressure until the melt exits the extruder. This is usually associated with a pressure reduction so that the gas trapped in the melt expands and causes foaming with appropriate cell formation in the melt.

The entry option for material can also be used for the addition of plasticizers. Plasticizers are used for various plastics in order to ensure a desired flexibility of the plastic.

Some time ago, it has been recognized by the applicant that structural advantages are given when the degassing and / or the material entry takes place on a module-constructed extruder between the modules. Optionally, there should also be a temperature measurement and / or pressure measurement. When using a planetary roller module, the stop ring should be used. The details are in the DE 19720916A1 described. Furthermore, there is proposed a thrust ring, which is provided with various holes that can be used as desired for one or more of the tasks described above. The unused holes are closed by blind plugs.

The construction has proved so successful that in the meantime it is imitated by others.

Nevertheless, the invention has set itself the task to improve this design even further. The invention is based on the recognition that the thrust rings have only a small size in the axial extruder direction, namely 3 to 4 cm, and their temperature determined by the temperature in the adjacent extruder modules and optionally by a temperature control of the inside scrolls or central spindle becomes.

• -dass je nach Beschaffenheit des verwendeten Kunststoffes nur ein sehr enges Temperaturfenster zur Verfügung steht und
• -dass der Temperaturverlauf der Schmelze zwischen den verschiedenen Mess-Stellen nur eingeschränkt kontrollierbar ist.

According to the invention, however, an additional direct tempering of an intermediate ring holding the thrust ring has an effect on the process. This is especially true in the case of degassing. It has been shown that even small changes in temperature greatly affect the quality of the melt. This is especially the case in border areas. That explains that

• -that depending on the nature of the plastic used, only a very narrow temperature window is available and
• -that the temperature profile of the melt between the different measuring points is only limited controllable.

The intermediate rings are preferably used as centering rings, as in the DE 9421955U1 described.

Preferably, a separate Temperierungskreis is provided for the additional cooling on the intermediate ring holding the thrust ring. As a result, the temperature in the region of the contact rings can be changed independently of the other temperature profile in the extruder. This also allows temperature control after trials. That is, in experiments, the behavior of the melt is determined by measuring the temperature control in the various Temperierungskreisen and optionally with temperature measurement at the run-up ring and at other locations for certain melts, and then optionally with a temperature measuring point or few temperature measuring points to control the temperature ,

Similar effect can be achieved with the pressure measurement on the thrust ring.

With the combination of all functions in a run-up ring or intermediate ring, the inventor ventures on an extremely difficult construction. An optimal temperature control results when one or more circumferential channels are provided for the tempering in the intermediate ring. For the tempering and axially extending channels can be provided, which are preferably distributed uniformly around the circumference, but can also be distributed unevenly.

The tempering can also be provided in sections on the circumference of the intermediate ring.

As a tempering agent water is common on extruders, even at the planetary roller extruders. In addition, oil is known as tempering. With the oil higher temperatures can be driven during tempering.

The tempering can have both the cooling and a heating to the content. As a rule, cooling is required. However, depending on the temperature level of the melt, the heating of the intermediate ring is so strong that the use of oil instead of water is advantageous.

With circulating channels for the temperature control, the task of passing by the passage openings for the measuring probes. According to the invention, the passage is possible by changing the cross section. Instead of a favorable flat cross-section extending in the longitudinal direction of the extruder, a channel cross-section is preferably selected in the area of the passage, which extends in the extruder longitudinal direction over a small amount enabling the passage, while the channel cross-section extends in the direction transverse thereto over a correspondingly greater extent the channel cross-section has the same area in the area of the pass-by passage as before in the direction of flow of the temperature-control means. That is, after passing the channel cross section for the tempering is brought back into the same shape as before the passage.

The combination of the temperature control with a degassing is optionally characterized in that on the outside of the stop ring degassing pockets are incorporated, which lead via holes to vent openings on an end face of the stop ring or intermediate ring, preferably to the rear surface of the stop ring. The front face is the surface on which the orbiting planets glide.

Preferably, the thrust ring is seated in an intermediate ring and at the contact surface between the two rings, a channel is provided which connects the various pockets. The channel can be incorporated as a groove in the one and / or the other annular surface. Preferably, in the annular surface opens a suction line for applying a negative pressure for the degassing.

In the drawing, an embodiment of the invention is shown.

1 shows an extruder in modular design with a trained as a single screw filling part 1 and two planetary roller parts 2 and 3 ,

The filling part has an opening 4 for the feed, in the exemplary embodiment, a mixture of plastic granules and aggregates.

The planetary roller parts 2 and 3 own housing 10 and 1 1 with internal bushings 14 and 15 , a common central spindle 6 and rotating planetary spindles 8th ,

The central spindle 6 is positively connected to the screw of the filling part, so that the drive of the screw of the filling part at the same time rotates the central spindle.

The planetary spindles 8th have a toothing like the central spindle. The teeth are the teeth of the bushes 14 and 15 customized. The planetary spindles mesh at the same time with the central spindle and with the bushing. As a result, each rotation of the central spindle causes a rotation of the planetary spindles 8th around the central spindle.

The sockets 14 and 15 at the same time form channels for temperature control of the housing 10 and 11 , The channels are externally turned into the sockets and are closed by the housing sitting on it. The housings are shrunk onto the sockets. In the embodiment, water is pumped as coolant through the channels during operation. The coolant dissipates the accumulating heat.

Heat is generated when the plastic granules in the filling part are compressed and plasticized and under appropriate pressure in the planetary roller part 2 is promoted and homogenized. The resulting heat results from the applied deformation performance. By dissipating the heat, the temperature of the melt is reduced so that the plastic is not damaged. Setting the temperature also has other benefits.

The housings have at their opposite ends 12 and 13 one flange each. Both flanges are braced against each other by screws. They are doing by intermediate ring 21 and 22 and a stop ring 20 spaced.

The planetary spindles 8th are held solely due to the engagement of their teeth in the teeth of the central spindle and the toothing of the bush between the bush and the central spindle. The gearing is a helical gearing and causes during operation an axial thrust on the planetary spindles, so that the planetary spindles 8th be prevented in the axial direction from wandering. This is done with the help of the starting ring 20 , The stop ring 20 is from the intermediate rings 21 and 22 enclosed outside, which also have a Zentrierfunktion together with the stop ring. They set up the planetary roller parts 2 and 3 out to each other. The planetary spindles 8th slide with their faces on the thrust ring 20 , The sliding side is the front side in the melt flow direction 30 , the opposite side is the back 31 ,

In the starting ring 20 is from the back 31 her a groove incorporated and then closed again, so that a channel 25 arises. The channel 25 runs a short distance from the inside of the thrust ring 20 to about a 270 degree circumferential angle having a rectangular, flat cross section extending with its flat side in the axial extruder direction. At the ends 34 and 35 the channel goes into another channel 32 above. The channel 32 also has a rectangular, flat cross-section. However, the flat side is transverse to the longitudinal direction of the extruder, so that the channel 32 easy on holes 40 and 41 can be passed over, which are intended for a pressure measurement or temperature measurement. The holes 40 and 41 penetrate the stop ring 20 in the radial direction completely.

Also the channel 32 is created from the back in the way of a groove, which is then closed again, leaving the channel.

The grooves are milled in the embodiment.

To close the grooves rings or segments of rings are used, which are welded or soldered into the grooves. The segments or rings form lids.

The channels 25 and 32 serve an additional temperature control. For this they are flowed through in the operation of water. The water is via a connection 28 fed and discharged from a drain. To prevent a short-circuit flow is in the channel 25 between connection and drain a wall 27 intended.

The thrust ring has in the embodiment at the back nor vent openings 50 , Furthermore, there are pockets at the periphery of the degassing ring 51 , The bags 51 are milled and drilled holes with the vents 50 connected.

On the starting ring sits a dome 55 holding the degassing bags 51 overlaps and opens into a suction line. The cathedral 55 is so narrow in the longitudinal direction of the extruder that it is between the intermediate rings 21 and 22 and between the spaced flanges 12 and 13 Takes place.

At the front of the stop ring 20 are still recesses 26 for wearing surfaces 60 incorporated. The wear surfaces are in the embodiment of hard metal.

The measuring holes are closed with blind plugs when they are not needed. In the operating case, the plastic is compressed and plasticized and in the planetary roller part 2 homogenized with the aggregates. The resulting melt then enters the planetary roller part serving as the cooling part 3 , There, the melt is brought to a desired outlet temperature and discharged at the end of the extruder through a nozzle.

Claims (9)

Extruder with at least one planetary roller part for degassing volatile materials, consisting of several interconnected modules (1, 2, 3), preferably with modules whose housings are provided at the ends with flanges (12, 13) and at the flanges ( 12, 13) are connected to each other, wherein the extruder pressure measuring points and / or temperature measuring points, wherein the housing are provided with a tempering, wherein the planetary roller part of a rotating central spindle (6), several to the central spindle (6) encircling Planet spindles (8) and a housing with internal toothing or a housing with an internally toothed bushing (14,15), wherein the planetary spindles (8) with the central spindle (6) and with the internal toothing of the housing or the internally toothed socket (14,15) the housing, wherein the planetary spindles (8) are held in the axial direction by a stop ring (20) in at least one intermediate ring (21, 22) for is partially held, which in turn is at least partially disposed in the melt outlet side flange of the planetary roller extruder part housing and the flange of the corresponding module, wherein the intermediate ring (21, 22) surrounding the central spindle (6) leaving a passage gap for the melt, characterized in that the intermediate ring is additionally provided with a temperature control, wherein for temperature control in the extruder longitudinal direction and / or transversely thereto channels are guided through the intermediate ring, wherein the channels are guided past existing openings for the pressure measurement and / or the temperature measurement. After extruder Claim 1 , characterized in that the channels in front of and behind the openings for the pressure measurement and temperature measurement extend flat in the extruder longitudinal direction and extend in the area of the passage with a smaller degree in the extruder longitudinal direction and transverse to a larger extent. After extruder Claim 2 , characterized in that the channels have the same cross-sectional area before and after the passage and in the passage of the passage. Extruder after one of the Claims 1 to 3 , characterized in that the channels are formed by grooves on the back of the intermediate ring, which are closed by lids. Extruder after one of the Claims 1 to 4 , characterized in that the intermediate ring (21, 22) is provided on the outside with degassing, which lead through holes to degassing at the back of the intermediate ring. Extruder after one of the Claims 1 to 5 , characterized in that the provided at the housing ends of the modules flanges are spaced from each other and a supply line for Ternperierungsmittel and / or a degassing line and / or measuring lines between the flanges are performed. Extruder after one of the Claims 1 to 6 , characterized in that for the degassing pockets are provided on the periphery of the intermediate ring and are connected via bores with degassing at the back of the intermediate ring and that the pockets are comprised by a dome, which is arranged between the flanges of the housing ends. Extruder after one of the Claims 1 to 7 , characterized in that the intermediate ring is provided on the front side with an inserted wear insert. After extruder Claim 8 , characterized in that the wear insert is a hard metal.

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