• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to a device (1a..1g) for processing thermoplastic material, which comprises a storage container (2) / a transport line (11) for piece-shaped plastic particles, and a transport screw (3) connected thereto. Furthermore, the device (1a..1g) has an extruder (4) adjoining the transport screw (3), as well as a tempering device (7) arranged in the course of the transport screw (3). In addition, a temperature sensor (8, 8a, 8b) is arranged in the course of the transport screw (3) / of the extruder (4), and / or means (10) for detecting a load of a drive (6) of the extruder (4) are provided , Finally, the device (1a..1g) comprises means for influencing the tempering device (7) and a control / regulation unit (9) connected to the at least one temperature sensor (8, 8a, 8b) and the influencing means of the tempering device (7). Furthermore, an operating method for the device (1a..1g) is specified, in which the piece-shaped plastic particles in the course of the transport screw (3) by a tempering device (7) are tempered.
    公开号:AT517972A1
    申请号:T51001/2015
    申请日:2015-11-24
    公开日:2017-06-15
    发明作者:Dipl Ing Brzezowsky Klaus；Ing Klemens Gruber Dipl；Ing Pichler Thomas
    申请人:Next Generation Recyclingmaschinen Gmbh；
    IPC主号:
    专利说明:

    The invention relates to a device for processing of thermoplastic material, which comprises a reservoir for receiving piece-shaped plastic particles or a transport line for transporting piece-shaped plastic particles, connected to the reservoir / the transport line to a transfer port screw conveyor and an adjoining the screw extruder. In addition, the invention relates to a method for operating the above device
    An apparatus and a method of the above type are basically known from the prior art. For example, EP 0 934 144 B1 discloses an apparatus for processing thermoplastic material. The device comprises a machine housing with a feed hopper and a driven slide which presses the plastic material located on a base plate and to be processed into a conditioner drum or into a conveyor tube. Knives are mounted helically on the conditioner drum. The knives and the subsequent screw feed the shredded plastic material to a screw of an extruder into which the plastic material is dispensed.
    The disadvantage is especially the difficult to predict and controllable temperature at the entrance to the extruder. Among other things, this depends on the processed material (in particular its heat capacity), the throughput and also the shape and size of the plastic particles. Friction, shearing and compression can lead to significant heating already in the transport screw, so that the plastic particles can stick together or stick to the extruder inlet and clog it up. In principle, it is also unimaginable that the plastic particles at the entrance to the extruder are comparatively cold, for example when plastic is supplied at a very low temperature for further processing. Since the extruder has only limited means for influencing the temperature, the achievement of a target temperature at the nozzle of the extruder according to the prior art may not be guaranteed in every case.
    An object of the invention is therefore to provide an improved apparatus and an improved method for processing thermoplastic material. In particular, a desired temperature in the extruder and / or at the inlet of the extruder and at the nozzle with higher security should be achieved.
    The object of the invention is achieved with a device of the type mentioned above, which has a tempering device arranged in the course of the transport screw and a) at least one temperature sensor, which is arranged in the course of the screw conveyor and / or in the course of the extruder, means for influencing the tempering and a controller connected to the at least one temperature sensor and the influencing means of the tempering device and / or b) means for detecting a load of a drive of the extruder, means for influencing the tempering device and a controller connected to the detection means and the influencing means.
    The object of the invention is further achieved by a method for the operation of the above device, in which the piece-shaped plastic particles are tempered in the course of the screw conveyor by a tempering device.
    The proposed measures, a target temperature in the extruder and / or at the entrance of the extruder and at the nozzle with higher security can be achieved. The tempering device can be formed, for example, by a heating device, a cooling device or a combined heating and cooling device.
    It is conceivable that the plastic particles supplied to the extruder are cooled by means of the tempering device, for example when material has been delivered at very high temperature and / or has low heat capacity and / or has a lower melting temperature and / or excessively due to friction, shearing and compression in the transport tube was heated. As a result, clogging or sticking of the extruder inlet or caking of the plastic particles on the same is avoided or at least reduced.
    However, material supplied to the extruder can also be heated with the aid of the tempering device, for example if this was delivered at a very low temperature and / or exhibits high heat capacity and / or has a high melting temperature and / or does not occur in the transport tube due to friction, shearing and compression expected way was heated.
    In general, the heating of the plastic particles in the interior of the extruder takes place by internal friction, wherein the drive power of the extruder is almost completely converted into heat. In other words, the mechanically discharged engine power is almost entirely converted into thermal power, and the extruder drive motor effectively acts as a heater. The longer the extruder, the more heat can be introduced into the plastic. Due to the enormous shear forces, it can also lead to a negative impact on the material quality in extreme cases.
    A comparatively high feed temperature of the extruder is now advantageous in that the material is gently melted in the extruder, since it is already preheated into the extruder. As a result, the drive power for the extruder can be reduced and its overall length can be reduced. The energy consumption of the extruder per unit weight of the extruded material is thus also reduced and / or the material throughput is increased. In addition, material wear in the extruder can be reduced.
    In the final result, it is therefore not always useful to cool the plastic particles in the screw conveyor excessively, so as to avoid sticking of the extruder at the beginning or caking of the plastic particles on the same. Rather, it can be provided that the temperature of the plastic particles at the extruder inlet is just so high that none of the mentioned negative phenomena (excessive) occurs. This maintenance can be largely avoided at the disclosed devices, or maintenance intervals are extended, on the one hand because of the remaining free extruder input, on the other hand, because of the gentle operation of the extruder.
    In case a), the supply and / or removal of heat is adjusted or regulated directly as a function of a temperature of the plastic particles. In the case b), however, the supply and / or removal of heat is adjusted or regulated as a function of a load on the extruder and thus indirectly via the temperature of the plastic particles. In the process, the fact that the drive of the extruder is loaded in a characteristic manner at the setpoint temperature reached in the extruder is taken advantage of. If the load is above this characteristic value, this is an indication that the plastic particles are too cold and are not melted properly. If the load is below this characteristic value, this is an indication that the plastic particles are too hot and excessively thin. Accordingly, in an advantageous process in case a) the removal of heat is enhanced as the temperature in the extruder and / or at the inlet of the extruder increases and vice versa. In an analogous manner, the removal of heat is advantageously enhanced when the load in the extruder and / or at the inlet of the extruder decreases and vice versa.
    Advantageous embodiments and developments of the invention will become apparent from the dependent claims and from the description in conjunction with the figures.
    It is advantageous if a cooling capacity of the cooling device or of the combined heating and cooling device is greater than a power supplied by friction to the piece-shaped plastic particles in the transport screw. This makes it possible to cool the plastic particles before they enter the extruder and clogging or sticking of the extruder opening or a Anba bridges the plastic particles to avoid the same or at least reduce. In a further preferred variant, the cooling capacity of the cooling device or the combined heating and cooling device is greater than a drive power of the screw conveyor. The latter is generally easier to determine than a frictional power supplied to the plastic piece particles in the screw conveyor, thereby also simplifying the dimensioning of the cooling device or the combined heating and cooling device. Any resulting slight oversizing may serve as security. It is favorable if the at least one temperature sensor in case a) is arranged downstream of the tempering device in the transport direction of the conveyed plastic particles. In this way, the tempering can be controlled. In principle, however, it is also possible that the at least one temperature sensor is arranged in the transport direction before the tempering device. Such temperature sensors can also be included in the control of the tempering. Of course, it is also possible to control the tempering only. In particular, the case is possible that all temperature sensors are arranged in the transport direction before tempering.
    It is particularly advantageous if the at least one temperature sensor in case a) is arranged in the region of the transition between the transport screw and the extruder. In this way, a predeterminable (desired) temperature of the plastic particles supplied to the extruder can be maintained particularly well. Preferably, this type of control or this control loop is combined with a further control loop, which controls the heating in the extruder. The control loop of the screw conveyor and the control loop of the extruder can work independently of each other, or the two control loops may be superordinate yet another loop.
    It is also conceivable that the temperature sensor is arranged in case a) in the course of the extruder, in particular in the region of the outlet or the nozzle. As a result, the proper melting of the plastic particles can be well controlled. For example, the tempering device and a heater in the extruder are provided as actuators. In particular, the temperature control can be prioritized, that is, a heater of the extruder is switched on only when heating by the tempering is not sufficient.
    In a particularly advantageous embodiment, the heat supply in case b) is increased when the load of the extruder increases and vice versa. Accordingly, it is advantageous if the control is set up to increase the supply of heat by the tempering device, if a load of the extruder increases and vice versa. As a result, the extruder in turn warmer material is supplied, if the heating power for proper melting of the plastic particles is not sufficient and cooler material, if the plastic particles are melted in the extruder in an excessive manner.
    In general, the control / regulation of the temperature control can be based solely on a temperature measurement in or on the extruder, solely on a measurement of the load of the drive of the extruder or on a temperature measurement and a measurement of the load of the extruder drive. It is advantageous if a speed of a drive of the extruder, a current absorbed by this drive or the torsion of a shaft in the drive is measured to determine the load of the extruder. For this purpose, a sensor for measuring a rotational speed of the drive of the extruder (eg a digital incremental encoder) may be provided, a sensor for measuring a current absorbed by the drive (eg a voltmeter on a current measuring resistor) or, for example, a sensor for measuring the torsion of a Shaft in the drive (eg a measuring bridge with strain gauges). In general, the drive can also have a transmission. The above-mentioned speed and the above-mentioned torsion can therefore also be removed on a component in the transmission. In general, the extruder is loaded more heavily when the speed of the drive decreases, the current absorbed by the drive increases or the torsion of a shaft in the drive increases.
    It is furthermore particularly advantageous, if the type / type of processed plastic is detected by a sensor and / or detected by an input means, an association between the type / type of plastic and a desired temperature in the extruder and / or at the entrance of the extruder from a Memory is read and the target temperature, which corresponds to the recognized / entered type / type of plastic, is loaded into a control / regulation for controlling / regulating the tempering.
    Accordingly, it is also advantageous if the presented device comprises a sensor for detecting the type / type of processed plastic and / or an input means for inputting the type / type of processed plastic, a memory with an association between the type / type of the stored therein Plastic and a target temperature in the extruder and / or at the entrance of the extruder and
    Means for loading the target temperature, which corresponds to the detected / entered type / type of plastic, in the control / regulation.
    As a result, a wide variety of materials can be processed in an advantageous manner. This is particularly advantageous in the context of devices that are used for the recycling of plastic, since there are particularly many different plastics incurred. Often it is not known which plastic or which plastic mixtures are to be processed. By using the above-mentioned sensor or said input device, however, the type / type of processed plastic can be detected and the device can be adjusted to it, so that clogging of the extruder inlet or caking of plastic particles on the same is just avoided. This maintenance can be largely avoided at the disclosed devices, or maintenance intervals are extended, on the one hand because of the remaining free extruder input, on the other hand, because of the gentle operation of the extruder. In addition, the required drive power for the extruder or the overall length of the extruder is relatively low and the material quality obtained high.
    In a further particularly advantageous variant of the presented method, an association between the type / type of plastic and a desired temperature profile along at least part of the transport path of the plastic particles containing the desired temperature in the extruder and / or at the inlet of the extruder is read from the memory and the target temperature profile or parts thereof in other control circuit / control circuits in the transport path of the plastic particles, which are provided for controlling / regulating a temperature of the plastic particles loaded. Accordingly, a particularly advantageous embodiment of the disclosed device is characterized in that in the memory an association between the type / type of plastic and a target temperature profile along at least part of the transport path of the plastic particles, containing the target temperature in the extruder and / or at the entrance of the Extruder, is stored and further control circuits / control circuits are provided in the course of transport of the plastic particles, with which the temperature of the plastic particles can be influenced and in which said target temperature profile or parts thereof are loadable.
    In particular, in this context, it is also advantageous if the device has a plurality of arranged in the course of transport of the plastic particles temperature sensors. In this variant, not only a single desired temperature is specified selectively, but a desired temperature profile along at least part of the transport path of the plastic particles, which leads through the screw conveyor and the extruder. This allows the device to be better adjusted to the type / type of processed plastic.
    In particular, the temperature of the plastic particles depending on the type / type in its entire transport process or up to a position in the extruder be steadily increasing or steadily increasing, but be substantially constant in the course of the screw conveyor or steadily increasing, but in the course of the screw conveyor be sinking. The first case is particularly suitable for plastics, which are supplied by friction in the screw conveyor relatively little energy, or plastics which have a relatively high melting point. Examples are polyamide (PA) and polyethylene terephthalate (PET). The other two cases relate to plastics, which are supplied by friction in the screw conveyor relatively much energy, or plastics which have a relatively low melting point. Examples are polyolefins and ethylene vinyl acetate (EVA).
    In a further advantageous embodiment variant, the shredder means arranged thereon on the conveying screw, which are formed in particular by teeth and / or by continuous cutting edges and / or by knives. In this way, the conveyed into the screw conveyor material can be further crushed before it reaches the extruder. Thus, the extruder can be supplied with material of optimum size, which ensures proper mixing and proper melting of the material and can prevent clogging of the extruder. The screw conveyor can thus also be considered (partially) as a conditioner drum / shredder or contain this function.
    The screw conveyor may be continuously filled with cutters and / or teeth and / or knives, or may have them only in a (continuous) section (ie in a comminuting section) adjacent to an initial section and / or end section in which no cutters are made , Teeth or knives are arranged. Continuous cutting edges, teeth and blades can each be used alone or in any combination on the transport screw. "Through-cutting" extend substantially over the entire length of the screw conveyor or over the entire length of a crushing area. In particular, the continuous cutting can be spiral or axial. A plurality of continuous cutting edges can be distributed over the circumference of the conveying screw, or the conveying screw has only one continuous cutting edge. During the rotation of the transport screw, the continuous cutting edges are moved substantially transversely to their longitudinal extension, respectively the rotation of the transporting screw causes a movement with such a transverse component. The separation of the plastic particles is therefore mainly by shearing. "Teeth" can be interpreted as interrupted cutting or cutting with gaps. Also, their cutting can be spiral or axial and also their cutting are moved during the rotation of the screw conveyor transversely to the longitudinal extent. The separation of the plastic particles is therefore mainly by shearing and tearing. "Knives" do not have a pronounced axial extent, and their cutting edges extend substantially radially outwardly. When the transport screw is rotated, the cutters are again moved transversely to their longitudinal extension, but the plane of the "knife back" is essentially normal to the axis of rotation of the transport screw. The separation of the plastic particles is done mainly by cutting.
    In general, an exact subdivision of the separation process is hardly possible, especially if the cutting edges are not exactly aligned axially or not exactly radially. In general, the plastic particles are therefore comminuted by shearing and tearing and cutting. Finally, it is favorable if, in the region of the screw conveyor with its continuous cutting edges / knives / teeth (in particular in the comminuting area), cooperating, fixed counterblades / counterblades / counter teeth are arranged. As a result, the cutting performance of the screw conveyor is improved. In particular, when providing knives and counter knives, the separation of the plastic particles is no longer necessarily mainly by cutting but possibly also by shearing.
    It should be noted at this point that the variants disclosed to the device for processing thermoplastic material and the advantages resulting therefrom also apply mutatis mutandis to the embodiments of the operating method according to the invention and vice versa.
    For a better understanding of the invention, this will be explained in more detail with reference to the following figures.
    In each case, in a highly simplified, schematic representation:
    1 shows a first exemplary and schematically illustrated apparatus for processing thermoplastic material with a tempering device and a control via a temperature sensor in the region of entry into the extruder;
    2 shows a second exemplary device with a control over the load of the drive of the extruder.
    3 shows a further exemplary device with an extended control;
    Fig. 4 as in Figure 1, only with teeth and knives on the screw conveyor and a temperature sensor on the extruder die.
    Fig. 5 as shown in Figure 1, only with continuous cutting on the screw conveyor.
    6 shows a device with a sensor for detection and input means for inputting the type / type of processed plastic;
    7 shows a device with several influencing points in the course of the transport path of the plastic particles and
    8 shows temperature profiles for four different types / types of plastic particles along their transport path through the device.
    By way of introduction, it should be noted that in the embodiments described differently, identical parts have the same reference numerals or the same component designation.
    Drawings are provided, wherein the disclosures contained in the entire description can be transferred mutatis mutandis to the same parts with the same reference numerals or identical component names. Also, the location information chosen in the description, such as top, bottom, side, etc. related to the immediately described and illustrated figure and to transmit mutatis mutandis to the new situation in a change in position.
    1 shows a device 1a for processing thermoplastic material, which comprises a storage container 2 for receiving piece-shaped plastic particles, and a feed screw 3 connected to the storage container 2 at a transfer opening B and an extruder 4 adjoining the transport screw 3. The transport screw 3 is driven by a first drive motor 5 and the extruder 4 by a second drive motor 6. The screw conveyor 3 and the extruder 4 cross each other in the example shown. It should be noted, however, that FIG. 1 is a purely schematic illustration and that the feed screw 3 and the extruder 4 may also be arranged differently from one another, in particular coaxially. It is also conceivable that the screw conveyor 3 and the extruder 4 are driven by a single motor.
    In addition to the components already mentioned, the device 1a has a tempering device 7 arranged in the course of the transport screw 3. As a result, the transport screw 3 or the piece-shaped plastic particles conveyed with it can be tempered during delivery. Depending on the design of the tempering device 7, the plastic particles can be added or removed via the tempering device 7 heat, whereby they are heated or cooled accordingly.
    The tempering device 7 may be formed by a heating device, a cooling device or a combined heating and cooling device. Furthermore, the temperature device 7 may be operated with electric current or a heat transfer medium. In the case of operation with power, the tempering device 7 may be formed in particular as a heating coil. If the tempering device 7 is operated with a heat transfer medium, it can, for example, have a coiled tubing through which the heat transfer medium flows, which can be gaseous or liquid and which can heat or cool the tempering device 7.
    In FIG. 1, the tempering device 7 is shown as a heating and / or cooling sleeve arranged around the transport screw 3. This is advantageous, but not mandatory. It is also conceivable that the tempering device 7 is alternatively or additionally integrated in the shaft of the screw conveyor 3. In this way, the heat transfer between the plastic particles and the tempering 7 can be done very well.
    In FIG. 1, the tempering device 7 is also shown slightly in front of the inlet of the extruder 4. It is also conceivable, however, that the tempering device 7 directly adjoins the extruder 4 or even projects into the area of the extruder 4.
    In general, the supply and / or removal of heat is adjustable. For example, for this purpose, the current which flows through a heating coil of the tempering device 7, be adjustable. If the operation is provided with a heat transfer medium, the inflow to the tempering device 7 can be adjustable by means of a valve. It is also conceivable that the heat transfer medium can be passed in an adjustable manner via a bypass. Additionally or alternatively, it may also be provided that the temperature of the heat carrier can be adjusted via a heat exchanger, not shown, of a heating or cooling circuit.
    In addition, in the example shown in FIG. 1, the supply and / or removal of heat can be adjusted or regulated as a function of a measured temperature. For this purpose, the device 1a has a temperature sensor 8 for detecting a temperature in the region of the inlet of the extruder 4, as well as a control unit 9 connected to the temperature sensor 8 and the tempering device 7. The control 9 is set up to supply heat by the tempering device 7 increase as the temperature at the entrance of the extruder 4 decreases and vice versa. That is, the tempering device 7 is heated when a temperature at the inlet of the extruder 4 decreases and cooled when a temperature rises there.
    By the above-mentioned variant of the device 1 a, a representative for the case designated by "a" is realized. This means that at least one temperature sensor 8 is arranged in the course of the transport screw 3 and / or in the course of the extruder 4, and means for influencing the tempering device 7 as well as a control 9 connected to the at least one temperature sensor 8 and the influencing means of the tempering device 7 are provided.
    In the example shown, the temperature sensor 8 is arranged concretely in the transport direction of the conveyed plastic particles after the tempering device 7. In this way, a predeterminable (desired) temperature of the plastic particles fed to the extruder 4 can be regulated and thus adhered to particularly well.
    In principle, however, it is also possible that the temperature sensor 8 is arranged in the transport direction in front of the tempering device 7. In this case, for example, a controller for the tempering device 7 may be provided, which controls the power output of the tempering device 7 on the basis of the temperature of the supplied plastic particles. It is also conceivable that 7 temperature sensors 8 are arranged in front of the temperature device 7 and after the temperature device.
    The proposed measures a target temperature in the extruder 4 and / or at the entrance of the extruder 4 can be achieved with high security. By means of the tempering 7, the extruder 4 supplied material can be heated, for example, if this was delivered with very low temperature and / or high heat capacity and / or has a high melting temperature and / or by friction, shearing and compression in the transport pipe not in the expected Way was heated. It is also conceivable, however, in particular that the plastic particles fed to the extruder 4 are cooled with the aid of the tempering device 7, for example if material has been delivered at very high temperature and / or has low heat capacity and / or has a lower melting temperature and / or by friction, Shearing and compression in the transport tube was overheated.
    FIG. 2 now shows a device 1b, which is very similar to the device 1a shown in FIG. In contrast, the controller 9 is not connected to the temperature sensor 8, but with means 10 for detecting a load of the drive 6 of the extruder 4. Accordingly, the supply and / or removal of heat in the example shown in FIG Depending on a load of the extruder 4 set or regulated. In particular, the heat input is increased as the load of the extruder 4 increases and vice versa. That is, the tempering device 7 is heated as the load of the extruder 4 increases and cooled as the load of the extruder 4 decreases.
    By the named variant of the device 1 b, a representative for the case denoted by "b" is realized. This means that means 10 for detecting a load on a drive 6 of the extruder 4, means for influencing the tempering device 7 as well as a control 9 connected to the detection means 10 and the influencing means are provided.
    To determine the load of the extruder 4, the detection means 10 as a sensor for measuring a rotational speed of the drive 6 of the extruder 4 (eg as a digital incremental encoder), as a sensor for measuring a current absorbed by this drive 6 (eg as a voltmeter to a current measuring resistor) or be designed as a sensor for measuring the torsion of a shaft in the drive 6 (eg as a measuring bridge with strain gauges). If the speed of the drive 6 decreases, the current absorbed by the drive 6 increases or the torsion of a shaft in the drive 6 increases, this is a sign of a greater load on the extruder 4.
    It should be noted at this point that the drive 6 is not necessarily an engine alone, but rather that the drive 6 can also have a transmission. The above-mentioned speed and the above-mentioned torsion can therefore also be removed on a component in the transmission.
    Fig. 3 now shows another example of a device 1c which is very similar to the devices 1a and 1b shown in Figs. In the device 1c, the controller 9 is connected both to a temperature sensor 8 of the extruder 4 and to means 10 for detecting a load on the drive 6 of the extruder 4. The regulation of the tempering device 7 can thus be made particularly differentiated.
    In the device 1 c, in particular, the drive motor 5 of the screw conveyor 3 is connected to the controller 9 and is integrated into the control / regulation of the device 1 c. For example, the speed of the screw conveyor 3 can be lowered when the load of the extruder 4 increases and vice versa, in particular in synchronism with an increase in the temperature.
    In contrast to FIG. 1, the temperature sensor 8 is arranged in the region of the outlet of the extruder 4. Thereby, the controller 9 can regulate the temperature at the outlet of the extruder 4, whereby the proper melting of the plastic particles can be well controlled. Of course, the temperature sensor 8 could also be arranged at the inlet of the extruder 4, as shown in FIG.
    It can also be seen in particular from FIG. 3 that the device 1c does not necessarily have a container 2, but that the transport screw 3, as shown, can be connected to a transport tube 11. About the transport tube 11 plastic particles are transported not only to the screw conveyor 3, but also to other (not shown) units. In particular, the transport direction is from top to bottom. Due to the movement of the plastic particles and the projection projecting into the transport tube 11, some of the material transported in the transport tube 11 can be diverted and conveyed into the transport screw 3.
    In the examples shown so far, the screw conveyor 3 is oriented in the horizontal direction and the transfer opening B in the vertical direction. This is advantageous, but not mandatory. It is also conceivable, of course, that the transport screw 3 and / or the cross section of the transfer opening B are aligned obliquely.
    In general, it is also advantageous if the screw conveyor 3 has radially arranged blades, blades or teeth. In this way, the conveyed into the screw conveyor 3 material can be further crushed before it reaches the extruder 4. The transport screw 3 can thus also be (partially) considered as Auf-ready drum / shredder or include this function.
    FIG. 4 shows by means of a device 1 d, which essentially corresponds to the device 1 a shown in FIG. 1, as such a transport screw 3 can be formed. Specifically, the screw conveyor 3 of the device 1d teeth 12 and counter teeth 13 and knife 14 and counter knife 15, wherein the teeth 12 and counter teeth 13 are arranged in the front region of the screw conveyor 3 and the knife 14 and counter knife 15 in the end of the screw conveyor 3. In this way, the material conveyed into the transport screw 3 is further comminuted before it reaches the extruder 4. Thus, the extruder 4 material can be supplied of optimum size, whereby a proper mixing and proper melting of the material ensures and clogging of the extruder 4 can be prevented.
    In contrast to FIG. 1, in addition to a temperature sensor 8a arranged in the region of the inlet of the extruder 4, a further temperature sensor 8b is provided, which is arranged in the region of the nozzle of the extruder 4 (see also FIG. 3). As a result, the control 9 can be based both on the temperature of the plastic particles at the inlet of the extruder 4 and on the temperature at the outlet of the extruder 4. The process of processing the plastic particles can thus be controlled particularly well. In particular, a heater (not shown) of the extruder 4 may be connected to the control 9. As a result, a first control loop can be formed, which includes the first temperature sensor 8a and the tempering device 7, as well as a second control loop, which comprises the second temperature sensor 8b and the extruder heater. The two control loops can work independently of each other, or it can be a parent of this another control loop.
    Finally, Fig. 5 shows an example of a device 1e which is very similar to the device 1d shown in Fig. 4. In this variant, the screw conveyor 3, however, no teeth 12 and no knives 14, but continuous cutting 16. These cutting 16 cooperate with fixed blades 17, whereby the supplied material is also crushed.
    The fixed blades 17 may be formed, for example, as axially aligned cutting (see also the front view B) or else also run in a spiral (see the front view C). It is particularly advantageous if the pitch of the fixed helical cutting edges 17 is different from that of the cutting edges 16 of the transporting screw 3, since then load peaks in the drive torque are avoided. The spiral-shaped sheaths 17 can be wound in the same sense as the cutting edges 16 of the screw conveyor 3 or also in opposite directions. Finally, it would also be conceivable that the fixed blades 17 are normal to the axis of the screw conveyor 3.
    In general, it is advantageous if the stationary blades 17 are arranged only in the upper and in the lateral region of the transport screw 3, since this avoids that material accumulates in the lower region of the screw conveyor 3, which is not transported away. In addition, the tube, in which the screw conveyor 3 runs, funnel-shaped together, whereby the collection of plastic particles in the screw conveyor 3 is favored. Of course, said eccentric configuration and / or said funnel-shaped structure is also suitable for the teeth 12 and blades 14 shown in FIG. 4. Conversely, for the cutting edges 17 of FIG. 5, too, a coaxial and / or cylindrical screw conveyor 3 Arrangement possible. Finally, it is also conceivable that the transport screw 3 has cutting edges 12, blades 14 and teeth 16 or any combination thereof.
    6 shows a further variant of a device 1f, which has a sensor 18 for detecting the type / type of processed plastic, a memory 19 with an association between the type / type of plastic stored therein and a desired temperature in the extruder 4 and / or at the entrance of the
    Extruder 4 and means for loading the target temperature, which corresponds to the recognized type / type of plastic in the control / regulation 9. In the example shown, the memory 19 and the control / regulation 9 part of a process computer 20. Of course, the memory 19 and the control / regulation 9 also form independent units.
    In this variant, the temperature at the temperature sensor 8 is thus not only regulated, but it is also determined which setpoint of the control should be used. In principle, various sensors 18 can be used to detect the type / type of plastic. For example, this can work on the principle of spectral analysis. Under certain circumstances, an ongoing determination of the type / type of plastic due to the necessary measurement time is not or only partially possible. It is therefore also conceivable that the measurement is carried out at the beginning of a batch and the result of the following processing is used.
    The proposed measures a variety of materials can be processed in an advantageous manner. This is particularly advantageous in connection with devices 1f that are used for the recycling of plastic, since there are particularly many different plastics. Often it is not known which plastic or which plastic mixtures are to be processed. However, by using the above-mentioned sensor 18, the type / type of processed plastic can be detected and the device 1f can be set thereon.
    As an alternative or in addition to the sensor 18, input means 21 for inputting the type / type of processed plastic may also be provided, as shown in FIG. 6. In this way, the type / type can be entered by a machine operator, for example by selecting one or more plastics from a table offered. For example, the input can be based on the results of a laboratory analysis or supplier information.
    In addition to the above statements, it is noted that in the memory 19 also an association between the type / type of plastic and a desired temperature profile along at least part of the transport path of the plastic particles, containing the target temperature in the extruder 4 and / or at the entrance of the extruder. 4 , can be stored. In addition, further control circuits / control loops can be provided in the course of transport of the plastic particles, with which the temperature of the plastic particles can be influenced and in which said desired temperature profile or parts thereof can be loaded.
    In this variant, not only a single target temperature is selectively specified, but a target temperature profile along at least part of the transport path of the plastic particles, which at least by the screw conveyor 3 and the extruder 4 leads. As a result, the device 1f can be better adjusted to the type / type of processed plastic.
    7 shows an example in which the controller 9 influences several points of a device 1g, as shown in simplified fashion with dashed arrows. For this purpose, it is also possible to provide a plurality of temperature sensors 8, 8a, 8b (not explicitly shown in FIG. 7) arranged in the transport path of the plastic particles. In FIG. 7, a comminution shaft 22, which can be driven independently by the transport screw 3, is furthermore provided with knives arranged thereon. For the drive thereof, the device 1g therefore also comprises a further motor 23. With the aid of this comminuting or cutting shaft 22, the size of the plastic particles fed to the extruder can be set by the transport screw 3 independently of the material flow. If the rotational speed of the comminuting or cutting shaft 22 is increased with respect to the rotational speed of the conveying screw 3, the plastic particles are comminuted more strongly and vice versa.
    In particular, the temperature of the plastic particles depending on the type / type in its entire transport progress up to a position in the extruder 4 may be steadily increasing or steadily increasing, but be substantially constant in the course of the screw conveyor or steadily rising, but sinking in the course of the screw conveyor, as shown by way of example in FIG. 8, FIG. 8 shows a plurality of temperature profiles through the device 1g. Specifically, the temperatures T are shown at several points A..F distributed over the path s. Point A indicates the entrance of the storage container 2, point B the entrance to the shredding or knife shaft 22, point C the entrance to the screw conveyor 3,
    Point D the entrance to the extruder 4, point E a point in the extruder 4 and point F the output or the nozzle of the extruder. 4
    Specifically, temperature profiles for four different materials M1 ..M4 are shown. For the materials M1 and M2, the temperature T in the entire transport process up to the position E is steadily increasing. These gradients are particularly suitable for plastics, which is supplied by friction in the screw conveyor 3 relatively little energy, or plastics which have a relatively high melting point. For example, polyethylene terephthalate (PET) may be provided for the material M1 and polyamide (PA) for the material M2. For the materials M3 and M4, the temperature T in the entire transport process is continuously rising up to the position E, but sinking in the course of the transport screw 3. These courses are particularly suitable for plastics, which are supplied by friction in the screw conveyor 3 relatively much energy, or plastics which have a relatively low melting point. For example, for the material M3 polyolefin and material M4 ethylene vinyl acetate (EVA) may be provided.
    The materials M3 and M4 are thus cooled in the course of the transport screw 3 by the tempering device 7 in order to avoid clogging or sticking of the extruder opening D or caking of the plastic particles on the same or at least reduce it. It is advantageous in this context, in particular, when a cooling capacity of the temperature control device 7 is greater than a piece of plastic particles in the feed screw 3 supplied by friction performance. In a further preferred variant, the cooling capacity of the tempering device 7 is greater than a drive power of
    Transport screw 4. The latter is usually easier to determine than the piece-shaped plastic particles in the screw conveyor 4 supplied by friction performance, whereby the dimensioning of the temperature control device 7 is simplified. Any resulting slight oversizing may serve as security.
    In the present example, reference was made to a transport path to the E position. From this position E, the temperature T up to the nozzle F no longer increases. It is also conceivable that the temperature T also increases from the position E to the nozzle F. In this case, the above considerations apply to the entire transport path of the plastic particles through the device 1g.
    The embodiments show possible embodiments of a device 1a..1g for processing of thermoplastic material and method for their operation, it being noted at this point that various combinations of the individual embodiments are possible with each other.
    In particular, it is pointed out that the control principles presented are not necessarily bound to the mechanical properties of the design of the device 1a..1g chosen for explanation. That is, the examples are interchangeable in terms of their control properties and in terms of their mechanical structure. For example, the control principle presented in FIG. 1 can also be used with a transport screw 3 according to FIG. 4 or 5 or in connection with a transport tube 11. The control principle shown in Fig. 3 can also be applied in devices 1a, 1b, 1d, 1e, 1f, 1g and so on.
    In particular, it is stated that a device 1 a.1 g may in reality also comprise more or fewer constituents than illustrated.
    For the sake of order, it should finally be pointed out that in order to better understand the structure of the device 1a..1g, these or their components have been shown partially unevenly and / or enlarged and / or reduced in size.
    The task underlying the independent inventive solutions can be taken from the description.
    1a. 1g device for processing thermoplastic material 2 storage container 3 transport screw 4 extruder 5 first drive (for transport screw) 6 second drive (for extruder) 7 temperature control 8, 8a, 8b temperature sensor 9 control 10 detection means for the load of the extruder 11 transport tube 12 teeth (on transport screw) 13 Counter teeth 14 Knife (on transport screw) 15 Counter knife 16 continuous cutting edges (on transport screw) 17 Counter cutting 18 Sensor for detecting the type / type of plastic 19 Table / memory with classification Type / type Plastic vs. plastic. Target temperature 20 Process computer 21 Input means for entering the type / type of plastic 22 Disintegration shaft / knife shaft 23 Motor for comminution shaft / knife shaft A Input reservoir B Transfer opening / input to comminution shaft / knife shaft C Entrance to transport screw D Input to extruder E Position inside extruder F Outlet / nozzle Extruder M1..M4 Material s Path T Temperature
    权利要求:
    Claims (24)
    [1]
    claims
    1. Device (1a..1g) for processing of thermoplastic material, comprising a reservoir (2) for receiving piece-shaped plastic particles or a transport line (11) for transporting piece-shaped plastic particles, one with the reservoir (2) / the transport line (11 ) conveying screw (3) connected to a transfer opening (B) and an extruder (4) adjoining the transport screw (3), characterized by a tempering device (7) arranged in the course of the transport screw (3) and a) at least one temperature sensor (8, 8a, 8b), which is arranged in the course of the transport screw (3) and / or in the course of the extruder (4), means for influencing the tempering device (7) and one with the at least one temperature sensor (8, 8a, 8b) and Influencing means of the tempering device (7) connected control / (9) and / or b) means (10) for detecting a load of a drive (6) of the extruder (4), Means for influencing the tempering device (7) and a control (9) connected to the detection means (10) and the influencing means.
    [2]
    2. Device (1a..1g) according to claim 1, that the tempering device (7) by a heating device, a cooling device or a combined heating and cooling device is formed.
    [3]
    3. Device (1a..1g) according to claim 2, characterized in that a cooling capacity of the cooling device or the combined heating and cooling device is greater than a piece of plastic particles in the feed screw (3) supplied by friction performance.
    [4]
    4. Device (1a..1g) according to one of claims 1 to 3, characterized in that the at least one temperature sensor (8, 8a, 8b) in the case a) in the transport direction after the tempering device (7) is arranged.
    [5]
    5. Device (1a..1g) according to one of claims 1 to 4, characterized in that the at least one temperature sensor (8, 8a, 8b) in case a) in the region of the transition between the screw conveyor (3) and the extruder ( 4) is arranged.
    [6]
    6. Device (1a..1g) according to one of claims 1 to 5, characterized in that the control (9) in the case a) is adapted to increase the heat supply by the tempering device (7) when a temperature (T ) in the extruder (4) / at the inlet of the extruder (4) decreases and vice versa.
    [7]
    7. Device (1a..1g) one of claims 1 to 3, characterized in that the control (9) in case b) is adapted to increase the heat supply by the tempering device (7) when a load of the extruder ( 4) rises and vice versa.
    [8]
    8. Device (1a..1g) according to one of claims 1 to 7, characterized by a sensor (18) for detecting the type / type of processed plastic and / or an input means (21) for inputting the type / type of processed plastic a memory (19) with an association therein stored between the type / type of plastic and a set temperature in the extruder (4) / at the entrance of the extruder (4) and means for loading the set temperature, which of the recognized / input type / type of Plastic corresponds to the control / regulation (9).
    [9]
    9. Device (1a..1g) according to one of claims 1 to 8, characterized by a plurality of arranged in the transport path of the plastic particles temperature sensors (8, 8a, 8b).
    [10]
    10. Device (1a..1g) according to any one of claims 8 or 9, characterized in that in the memory (19) an association between the type / type of plastic and a desired temperature profile along at least part of the transport path of the plastic particles containing the desired temperature in the extruder (4) / at the inlet of the extruder (4) is stored, and further control circuits / control circuits are provided in the transport path of the plastic particles, with which the temperature (T) of the plastic particles can be influenced and in which said target temperature profile or Parts of it are loadable.
    [11]
    11. Device (1a..1g) according to one of claims 1 to 10, characterized in that the transport screw (3) thereon arranged crushing means (12, 14, 16).
    [12]
    12. Device (1a..1g) according to claim 11, characterized in that the shredding means by teeth (12) and / or knives (14) and / or continuous cutting edges (16) are formed.
    [13]
    13. Device (1a..1g) according to claim 12, characterized in that in the region of the screw conveyor (3) with their teeth (12) / knives (14) / continuous cutting (16) cooperating, fixed counter teeth (13) / counter knife (15) / counter cutting (17) are arranged.
    [14]
    14. A method for processing thermoplastic by means of a device (1a..1g), which comprises a reservoir (2) for receiving piece-shaped plastic particles or a transport line (11) for transporting piece-shaped plastic particles, one with the reservoir (2) / Transport line (11) at a transfer opening (B) connected screw conveyor (3) and to the screw conveyor (3) subsequent extruder (4), characterized in that the piece-shaped plastic particles in the course of the screw conveyor (3) tempered by a tempering device (7) become.
    [15]
    15. The method according to claim 14, characterized in that the plastic particles are tempered by supply or removal of heat via the tempering device (7).
    [16]
    16. The method according to claim 15, characterized in that the supply and / or removal of heat as a function of a temperature (T) in the extruder (4) / at the input of the extruder (4) is set or regulated.
    [17]
    17. The method according to claim 16, characterized in that the dissipation of heat is enhanced when the temperature (T) in the extruder (4) / at the inlet of the extruder (4) increases and vice versa.
    [18]
    18. The method according to any one of claims 15 to 17, characterized in that the supply and / or removal of heat in dependence on a load of the extruder (4) is set or regulated.
    [19]
    19. The method according to claim 18, characterized in that the dissipation of heat is increased when the load on the extruder (4) decreases and vice versa.
    [20]
    20. The method according to claim 18 or 19, characterized in that for determining the load of the extruder (4) a speed of a drive (6) of the extruder (4), one of this drive (6) recorded current or the torsion of a shaft in the drive (6) is measured.
    [21]
    21. The method according to any one of claims 14 to 20, characterized in that the piece-shaped plastic particles in the course of the screw conveyor (3) by the tempering device (7) are cooled.
    [22]
    22. The method according to any one of claims 14 to 21, characterized in that the type / type of processed plastic is detected by a sensor (18) and / or detected by an input means (21), an association between the type / type of plastic and a target temperature in the extruder (4) / at the entrance of the extruder (4) is read from a memory (19) and the target temperature, which corresponds to the recognized / input type / type of plastic, in a control / regulation (9) for controlling / Rules of tempering (7) is loaded.
    [23]
    23. The method according to claim 22, characterized in that an association between the type / type of plastic and a desired temperature profile along at least part of the transport path of the plastic particles containing the target temperature in the extruder (4) / at the entrance of the extruder (4) , is read from the memory (19) and the desired temperature profile or parts thereof in further control circuit / control circuits in the transport path of the plastic particles, which are provided for controlling / regulating a temperature (T) of the plastic particles loaded.
    [24]
    24. The method according to any one of claims 14 to 23, characterized in that the temperature (T) of the plastic particles depending on the type / type in their entire transport process or up to a position in the extruder (4) is steadily increasing or steadily increasing, but in course the transport screw (3) is substantially constant or steadily rising, but sinking in the course of the transport screw (3).
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    同族专利:
    公开号 | 公开日
    US20180369770A1|2018-12-27|
    JP2018535128A|2018-11-29|
    AT517972B1|2017-09-15|
    WO2017089437A1|2017-06-01|
    CN108472855A|2018-08-31|
    EP3380298A1|2018-10-03|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA51001/2015A|AT517972B1|2015-11-24|2015-11-24|Apparatus and method for processing thermoplastic with a tempering device for a screw conveyor|ATA51001/2015A| AT517972B1|2015-11-24|2015-11-24|Apparatus and method for processing thermoplastic with a tempering device for a screw conveyor|
    PCT/EP2016/078622| WO2017089437A1|2015-11-24|2016-11-24|Device and method for processing thermoplastic material with a temperature control device for a conveying screw|
    CN201680075052.2A| CN108472855A|2015-11-24|2016-11-24|Utilize the device and method of the register processing thermoplastic material of screw conveyor|
    EP16800980.1A| EP3380298A1|2015-11-24|2016-11-24|Device and method for processing thermoplastic material with a temperature control device for a conveying screw|
    JP2018526775A| JP2018535128A|2015-11-24|2016-11-24|Apparatus and method with temperature controller for transfer screw processing thermoplastics|
    US15/778,262| US20180369770A1|2015-11-24|2016-11-24|Device and method for processing thermoplastic material with a temperature control device for a conveying screw|
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