• 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 for pretreating and subsequently conveying or plasticizing plastics with a container (1) having a mixing and / or comminution tool (3) rotatable about an axis of rotation (10), wherein an opening (8) is provided in a side wall (9) ) is formed, through which the plastic material can be carried out, wherein a conveyor (5) is provided, with a in a housing (16) rotating screw (6). The invention is characterized in that the imaginary extension of the longitudinal axis (15) of the conveyor (5) against the conveying direction (17) on the axis of rotation (10) passes, wherein the longitudinal axis (15) on the outlet side to the longitudinal axis (15) parallel radials (11) is offset by a distance (18), and that the radial distance of the tool (mb) to the inner surface of the side wall (9) of the container (1) is in the range of 15 mm to 120 mm, and satisfies the following relationship : mb = k * DBwobeiDB ... the inner diameter of the container (1) in mm is undk ... a constant in the range of 0.006 to 0.16.
    公开号:AT512146A1
    申请号:T1501/2011
    申请日:2011-10-14
    公开日:2013-05-15
    发明作者:
    申请人:Erema；
    IPC主号:
    专利说明:

    16408/5/5
    Device for processing plastic material
    The invention relates to a device according to the preamble of claim 1.
    Numerous similar devices of various types are known in the prior art, comprising a receptacle or cutting compactor for comminuting, heating, softening and processing a plastic material to be recycled and a conveyor or extruder connected thereto for melting the material prepared in this way. The aim is to obtain a high quality end product, usually in the form of granules.
    Thus, for example, in EP 123 771 or EP 303 929 devices are described with a receptacle and an extruder connected thereto, wherein the plastic material supplied to the receptacle crushed by rotating the crushing and mixing tools and brought into thrombus circulation and heated simultaneously by the introduced energy , This forms a mixture with sufficiently good thermal homogeneity. This mixture is discharged after appropriate residence time from the receptacle in the screw extruder, promoted and thereby piastifiziert or melted. The screw extruder is arranged approximately at the height of the crushing tools. In this way, the softened plastic particles are actively pressed or stuffed by the mixing tools into the extruder.
    However, most of these long-known constructions are not satisfactory in view of the quality of the machined plastic material obtained at the outlet of the screw and / or with regard to the output or throughput of the screw.
    Of crucial importance for the final quality of the product is, on the one hand, the quality of the pretreated or softened polymer material reaching the conveyor or extruder from the cutter compactor, and, on the other hand, the situation during feeding and conveying or the possible extrusion. Here, inter alia, the length of the individual regions or zones of the screw, as well as the parameters of the screw, e.g. whose thickness, flight depths etc. are relevant.
    Accordingly, there are special conditions in the cutter compactor-conveyor combinations present here, since the material which enters the conveyor is not introduced directly, untreated and cold, but has already been produced in the cutting compressor 2. This has been pretreated, i. heated, softened and / or partially crystallized !, " Decisive for the collection and the quality of the material.
    The two systems, the cutter compactor and the conveyor, influence each other, and the results of drawing in and further conveying or susceptible compaction depend heavily on the pretreatment and consistency of the material.
    An important area is therefore the interface between the cutting compressor and the conveyor, ie the area in which the homogenized pretreated material is transferred from the cutting compressor into the conveyor or extruder. On the one hand, this is a purely mechanical problem because two differently operating devices must be coupled together here. In addition, this interface is also delicate for the polymer material, since the material is usually present in a strongly softened state near the melting region, but must not melt. If the temperature is too low, the throughput and the quality decrease, the temperature is too high and in some places an unwanted melting takes place, so the collection clogged.
    In addition, a precise metering and feeding of the conveyor is difficult because it is a closed system and there is no direct access to the feeder, but the feeding of the material from the cutting compressor out, so not directly, for example via a gravimetric dosing, be influenced can.
    It is therefore crucial to make this transition both mechanically considered, so also with an understanding of the polymers own switching, and at the same time to pay attention to the efficiency of the overall process, ie on high throughput and appropriate quality. Here are partly conflicting requirements to consider.
    The above-mentioned, known from the prior art devices have in common that the conveying or rotating direction of the mixing and crushing tools and thus the direction in which the material particles circulate in the receptacle, and the conveying direction of the extruder substantially equal or in the same direction are. This deliberately chosen arrangement was guided by the desire to stuff the material as possible into the screw or to force-feed this idea, the particles in Schneckenförderrichtung in the conveyor or. To stuff extruder screw, was also quite obvious and corresponded to the common ideas of the expert, since the particles do not have to reverse their direction of movement and thus no additional force is needed for the reversal of direction. It became thereby and with it outgoing * * '111 ίί. Ji * ^ m
    Further developments always sought to create the highest possible filler filling and reinforcement of this stuffing effect. For example, attempts have also been made to conically expand the intake area of the extruder or to curve the shredding tools in a sickle-shaped manner so that they can feed the softened material into the screw in a spatula-like manner. Due to the inflow-side displacement of the extruder from a radial to a tangential position to the container, the stuffing effect was further enhanced and the plastic material from the rotating tool even more pressed or pressed into the extruder.
    Such devices are basically functional and work satisfactorily, albeit with recurrent problems:
    Thus, for example, with materials having a low energy content, e.g. PET fibers or sheets, or for materials having an early tack or softening point, such as e.g. Polylactic acid (PLA), observed over and over again the effect that the conscious same-sense plugging of the plastic material in the intake area of the extruder under pressure leads to premature melting of the material immediately after or in the intake area of the extruder. As a result, on the one hand, the conveying effect of the extruder is reduced, and it can also lead to a partial reflux of this melt in the area of the cutting compressor or receiving container, which means that still unmelted flakes adhere to the melt, thereby cooling the melt again and partially solidifies and forms in this way a schwulstartiges structure or conglomerate of partially solidified melt and solid plastic particles. As a result, the intake of the extruder clogged and stick the mixing and crushing tools. As a result, the throughput of the extruder is reduced because there is no longer sufficient filling of the screw. In addition, the mixing and comminution tools can get stuck. As a rule, in such cases, the system must be shut down and completely cleaned.
    Additionally, problems arise with those polymeric materials that have been heated in the cutter compactor to near their melting range. If the catchment area is overfilled, the material melts and the feeder sinks.
    Even with, mostly stretched, stripy, fibrous materials with a certain length extension and a small thickness or stiffness, so for example in cut into strips of plastic films, problems arise. This primarily by the fact that the elongated material adheres to the downstream end of the feed opening of the screw, wherein one end of the strip protrudes into the receptacle and the other end in the catchment area. Since both the mixing tools and the screw run in the same direction or the same Förderrichtungs- and printing component to 4 ψ · · ··· · · ·. J * apply the material, both ends of the strip in the same direction tensile and pressurized and the strip can not solve. This in turn leads to an accumulation of the material in this area, to a narrowing of the cross section of the intake opening and to a poor intake behavior and subsequently to loss of revenue. In addition, it may be due to the increased feed pressure in this area to melt, which in turn occur the problems mentioned above.
    At such co-rotating cutter compressors different extruder or conveyor were connected, the results were basically quite acceptable and appealing. However, the Applicant has done extensive research to further improve the overall system.
    The present invention has set itself the task of overcoming the disadvantages mentioned and to improve a device of the type described above, that, in addition to the usual materials, even sensitive or strip-like materials easily recovered from the screw and with high material quality, energy-saving and with high and constant throughput can be processed or treated.
    This object is achieved in a device of the type mentioned by the characterizing features of claim 1.
    It is initially provided that the imaginary extension of the central longitudinal axis of the conveyor, in particular extruder, if this has only a single screw, or the longitudinal axis of the feed opening nearest screw when it has more than one screw, against the conveying direction of the conveyor on the Rotation axis passes without cutting them, wherein the longitudinal axis of the conveyor, if this has a single screw, or the longitudinal axis of the feed opening closest screw downstream to the longitudinal axis parallel to the axis of rotation of the mixing and / or
    Crushing tool is offset in the conveying direction of the conveyor outwardly directed radials of the container by a distance.
    Thus, the conveying direction of the mixing tools and the conveying direction of the conveyor is no longer, as known from the prior art, in the same direction, but at least slightly in opposite directions, whereby the initially mentioned Stopfeffekt is reduced. By deliberately reversing the direction of rotation of the mixing and crushing tools in comparison to previously known devices, the 5 5 "" ♦ "* * f ···" 4 φ *
    Loading pressure on the catchment area decreases and Öäs reduces risk of overfilling. Excess material is not stuffed or filled in this way with excessive pressure in the catchment area of the conveyor, but on the contrary, excess material is even tending to be removed from there, so that although always sufficient material voriiegt in the catchment area, but almost without pressure or only with low Pressure is applied. In this way, the screw can be filled sufficiently and always enough material to move in without causing it to overfill the screw and subsequently to local pressure peaks, where the material could melt.
    In this way, the melting of the material in the area of the feeder is prevented, which increases the operational efficiency, lengthens the maintenance intervals and reduces the downtime due to possible repairs and cleaning measures.
    By reducing the feed pressure react slider, with which the degree of filling of the screw can be regulated in a known manner, much more sensitive and the degree of filling of the screw can be adjusted even more accurately. Especially for heavier materials, such as high-density polyethylene (HDPE) or PET regrind, it is easier to find the optimum operating point of the system.
    In addition, it has proved to be surprisingly advantageous that materials which have already been softened to near melt, are better fed in the counter-rotating operation according to the invention. In particular, when the material is already in doughy or softened state, the screw cuts the material from the doughy ring, which is close to the container wall. In a direction of rotation in the conveying direction of the screw, this ring would rather be pushed further and there could be no scraping by the screw, whereby the indentation would ease, This is avoided by reversing the direction of rotation according to the invention.
    In addition, in the processing of the above-described streaky or fibrous materials, the formed impurities or accumulations are easily solved or are not even formed because of the direction of rotation of the mixing tools downstream or downstream edge of the opening of the direction vector of the mixing tools and the directional vector of the conveyor in almost opposite or at least slightly opposite directions show, making an elongated strip can not bend and impose around this edge, but is carried along by the Mischtrombe in the receptacle again. f'if W il'VlKrf * aA * l. ä ** ** ·· «~ 9 ·
    Overall, the infeed behavior improves as a result of the inventive design, and the throughput increases significantly. The overall system of cutter compactor and conveyor is thus more stable and efficient.
    Furthermore, the Applicant has found that can be achieved by a particular embodiment of the mixing and crushing tools relative to the container wall and by the Provision of particular distances of the knife, surprising beneficial effects that have a direct impact on the intake behavior of the conveyor or extruder.
    Thus, the invention also provides that the radial distance of the tool mb, measured from the radially outermost point of the ground nearest mixing and / or crushing tool or tool and / or knife or defined by this point circle, to the inner surface of the side wall of the container in Range of 15 mm to 120 mm, preferably in the range of 20 mm to 80 mm.
    In addition, the radial distance mb satisfies the relationship mb = k * Dβ where
    Db is the inner diameter of a circular cylindrical container in mm or the
    Inner diameter in mm of a same volume of volume converted fictitious circular cylindrical container of the same height, and k ... is a constant in the range of 0.006 to 0.16.
    The distance of the tools to the container wall should be kept advantageously low, as this causes an improved intake behavior and a " tweaking " of material when moving in avoids. Nevertheless, sufficient tolerance intervals must be maintained. The distance too big, this leads to a worse feed.
    It has surprisingly been found that, due to the gentle feed behavior of the screw caused by the opposite direction of rotation of the mixing tools, more aggressive tools can be used in the cutting compressor, which introduce more energy into the material. The cutter compactor can therefore be operated at a higher temperature, which in turn has a better homogeneity with reduced residence time result. According to the invention, a particularly good and effective energy input by the particular spacing conditions in combination with the reverse direction of rotation of the tools.
    In addition, such a combination of cutter compactor and extruder unexpectedly results in an improved melting performance of the material in a connected extruder, since already strongly preheated particles enter the screw. As a result, any inhomogeneities are compensated and that of the container in the
    Snail housing entering and then compressed and 'melted material has a high thermal and mechanical homogeneity. Accordingly, the Endquatität the plasticizer or agglomerate at the end of the extruder or Agglomerierschnecke is very high and it can be used screws, which - due to the pretreatment and the feeder - treat the polymer gently and bring very little cutting power into the material, to melt this.
    In addition, the throughput consistency is higher over time or the throughput more even and the feeder works reliably without problems in the filling of the screw.
    Further advantageous embodiments of the invention are described by the following features:
    According to an advantageous further development it is provided that in the container at least one rotatable about the rotation axis, circulating valuer is provided on / in which the mixing and / or crushing tool (s) are arranged or formed.
    It is advantageous if the tool carrier is a carrier plate, in particular arranged parallel to the bottom surface. Then the tools can be easily and simply mounted.
    In this context, it is advantageous if the mixing and / or comminution tool and / or the tool carrier comprises tools and / or knives, which act in the direction of rotation or movement on the plastic material, crushing, cutting and / or heating.
    A variant in which the blades are very easy to change, provides that the mixing and / or crushing tool or tools and / or knives are arranged or formed on the top of the tool carrier.
    Advantageously, it can also be provided that the tools and / or knives are arranged on the radially outermost, facing the inner surface of the side wall, usually vertical, outer edge of the tool carrier, reversibly releasably secured or formed or incorporated therein.
    An advantageous further development provides that the radial distance of the tool carrier mc, measured from the radially outermost point of the ground nearest tool carrier or the circle defined by this point, to the inner surface of the side wall of the container in the range of 30 mm to 210 mm, preferably in the range from 40 mm to 150 mm.
    It is particularly advantageous if the ratio between the inner diameter DB of the container and the diameter of the circle formed by the radially outermost point of the toolholder lying closest to the ground fulfills the following relationship: DB = k2 * Dw where
    Db ... the inner diameter of the container in mm,
    Dw - the diameter of the radially outermost point of the tool carrier formed
    Circle in mm, k2 ... is a constant in the range of 1.01 to 1.5.
    According to an advantageous further development, it is provided that the constant k2 in containers with an inner diameter of DB greater than or equal to 1300 mm is in the range from 1.01 to 1.12. Here, the impact of the tools has proven to be particularly effective and the throughput can be kept very constant.
    Advantageously, it is provided that the radial distance of the tool carrier mc is greater than or equal to the radial distance of the tool mb. The tools protruding or protruding from the tool carrier promote the effect on the material in addition.
    According to an advantageous development of the invention it is provided that the conveyor is arranged on the receptacle, that the scalar product from the tangential to the circle of the radially outermost point of the mixing and / or crushing tool or to the opening passing plastic material and normal to a radial The direction vector (direction vector of the direction of rotation) and the direction vector of the conveying direction of the conveyor aligned in the direction of rotation or movement of the mixing and / or comminution tool in each individual point or in the entire region of the opening or in each individual point or in the entire area immediately radially in front of the opening, zero or negative. The area immediately radially in front of the opening is defined as the area in front of the opening at which the material is just before passing through the opening but has not yet passed through the opening. In this way, the advantages mentioned above are achieved and effectively avoided any agglomeration caused by stuffing effects in the region of the intake opening. In particular, it does not depend on the spatial arrangement of the mixing tools and the screw to each other, for example, the axis of rotation must not be aligned normal to the bottom surface or to the longitudinal axis of the conveyor or the screw. The direction vector of the direction of rotation and the direction vector of the conveying direction lie in one, preferably horizontal, plane, or in a plane oriented normal to the axis of rotation.
    A further advantageous embodiment results from the fact that the direction vector of the direction of rotation of the mixing and / or crushing tool with the direction vector of the conveying direction of the conveyor an angle greater than or equal to 90 ° and less than or equal 180 ° includes, wherein the angle at the intersection of the two Direction vectors is measured at the upstream of the rotational or moving direction edge of the opening, in particular in the furthest upstream point on this edge or the opening. As a result, that angle range is described in which the conveyor must be arranged on the receptacle in order to achieve the advantageous effects. In the entire region of the opening or in each individual point of the opening, an at least slight opposing orientation of the forces acting on the material or, in the extreme case, a pressure-neutral transverse alignment occurs. At no point in the opening is the scalar product of the directional vectors of the mixing tools and the screw positive, not even in a portion of the opening thus occurs too much stuffing effect.
    A further advantageous embodiment of the invention provides that the direction vector of the direction of rotation or movement with the direction vector of the conveying direction includes an angle between 170 ° and 180 °, measured at the intersection of the two directional vectors in the middle of the opening. Such an arrangement applies, for example, when the conveyor is arranged tangentially on the cutting compressor.
    To ensure that no excessive stuffing occurs, it may be advantageously provided that the distance or the offset of the longitudinal axis to the radial is greater than or equal to half the inner diameter of the housing of the conveyor or the piebald.
    Furthermore, it may be advantageous in this sense, the distance or the offset of the longitudinal axis to the radial greater than or equal to 7%, even more advantageously equal to 20%, to dimension the radius of the receptacle. For conveyors with an extended catchment area or a grooved or extended pocket, it may be advantageous if this distance or this offset is greater than or equal to the radius of the receptacle. In particular, this applies to cases in which the conveyor is tangentially connected to the receptacle or tangent to the cross section of the container.
    In this case, it is particularly advantageous if the longitudinal axis of the conveyor or the screw or the longitudinal axis of the screw closest to the intake opening or the inner wall of the housing or the envelope of the pawter are tangential to the 10.
    Inside the side wall of the container, wherein preferably W6 screw is connected at its front side with a drive and promotes at its opposite end to a front end of the housing arranged outlet opening, in particular an extruder head.
    At radially offset, but not tangentially arranged, conveyors is advantageously provided that the imaginary extension of the longitudinal axis of the conveyor against the conveying direction, the interior of the receptacle at least partially passes through as a secant.
    It is advantageous if it is provided that the opening directly and directly and without a longer spacing or transfer distance, e.g. a screw conveyor, is connected to the intake opening. This makes an effective and gentle transfer of material possible.
    The reversal of the direction of rotation of the circulating in the container mixing and crushing tools can not be done only arbitrarily or accidentally, and you can not rotate the mixing tools in the opposite direction, either in the known devices or in the device according to the invention, especially not, because the mixing and crushing tools are arranged asymmetrically in a certain way so that they act only on a single side or in one direction. If one deliberately turned such an apparatus in the wrong direction, neither a good mixed-atom bomb would be formed, nor would the material be sufficiently comminuted or heated. Each cutter compressor thus has its fixed predetermined direction of rotation of the mixing and crushing tools.
    In this connection, it is particularly advantageous if it is provided that the front regions or front edges of the mixing and / or comminution tools, which act on the plastic material and are oriented in the direction of rotation or movement, are differently shaped, curved, adjusted or arranged in comparison to in the direction of rotation or movement rear or trailing areas.
    The tools and / or knives can either be fastened directly to the shaft or are preferably arranged on a, in particular parallel to the bottom surface, arranged rotatable tool carrier or a carrier disk or formed therein or, optionally in one piece, angefomnt.
    In principle, the effects mentioned are relevant not only for compressing extruders or agglomerators, but also for non-compressing or less-compressing screw conveyors. Again, local overfeeding is avoided.
    In a further particularly advantageous embodiment it is provided that the receptacle is substantially cylindrical with a flat bottom surface and a 11 11 * Mil * · f * · «* • > In addition, it is structurally simple when the axis of rotation coincides with the central central axis of the receptacle, In a further advantageous embodiment it is provided that the axis of rotation or the central center axis of the receptacle is vertical and / or vertical These special geometries optimize the pull-in behavior of a structurally stable and simply constructed device.
    In this context, it is also advantageous to provide that the mixing and / or crushing tool, or if more superimposed mixing and / or crushing tools are provided, the lowest, ground-level mixing and / or crushing tool, and the opening in a small Distance to the bottom surface, in particular in the region of the lowest quarter of the height of the receptacle are arranged. The distance is defined and measured from the lowest edge of the opening or the intake opening to the container bottom in the edge region of the container. Since the corner edge is usually rounded, the distance from the lowest edge of the opening along the imaginary extensions of the side wall down to the imaginary extension of the container bottom is measured outwards. Well suitable distances are 10 to 400 mm.
    The container does not necessarily have a circular cylindrical shape, although this form is advantageous for practical and manufacturing reasons. Beyond the circular cylindrical shape Behäiterformen, such as frusto-conical container or cylindrical container with elliptical or oval outline, must be converted to a circular cylindrical container same volume, assuming that the height of this fictitious container is equal to its diameter. Container heights, which in this case substantially exceed the mixing drum (taking into account the safety distance), are not taken into consideration, since this excessive container height is not used and therefore has no influence on the material processing.
    In the present case, the term conveyor means systems with non-compressing or decompressing screws, that is to say pure conveying screws, as well as systems with compressing screws, ie extruder screws having an agglomerating or plasticizing effect.
    In the present text, the terms extruder or extruder screw mean both extruders or screws, with which the material is completely or partially melted, as well as extruders, with which the softened material only agglomerates, but is not melted. In the case of agglomeration screws, the 12 × * · · ·;; · ·
    Material only strongly compressed and sheared for a short time, not abraded. The Agglomerierschnecke therefore provides at its output material which is not completely melted, but consists of only on its surface melted particles, which are zusammengebackt as a sintering. In both cases, however, pressure is applied to the material via the screw and this compacted.
    In the examples described in the following figures, conveyors with a single screw, for example single-screw or single-screw extruders, are represented throughout. Alternatively, however, the provision of conveyors with more than one screw, for example double or multi-shaft conveyors or extruders, in particular with a plurality of identical screws, which have at least the same diameter d, is also possible.
    Further features and advantages of the invention will become apparent from the description of the following non-limiting embodiments of the subject invention, which are shown schematically in the drawings and not to scale:
    Fig. 1 shows a vertical section through a device according to the invention with approximately tangentially connected extruder.
    FIG. 2 shows a horizontal section through the embodiment of FIG. 1. FIG.
    Fig. 3 shows a further embodiment with minimum offset.
    Fig. 4 shows a further embodiment with greater displacement.
    Figs. 5 and 6 show the results of experiments
    Neither the containers, nor the screws or the mixing tools are to scale in the drawings, either as such, or in relation to each other. Thus, e.g. in reality, the containers are usually larger or the snails longer than shown here.
    The advantageous cutter compactor / extruder combination shown in FIGS. 1 and 2 for processing or recycling plastic material has a circular cylindrical container or cutter 1 with a flat, horizontal bottom surface 2 and a vertical, cylinder jacket-shaped one Side wall 9 on.
    At a small distance to the bottom surface 2, at most in about 10 to 20%, possibly less, the height of the side wall 9 - measured from the bottom surface 2 to the top edge of the side wall 9 - is parallel to the bottom surface 2 aligned, ·· ··· t4 a central axis of rotation 10, which is also the central center axis of the container 1, is rotatable in the direction of rotation or movement 12 marked with an arrow 12. The carrier disk 13 is driven by a motor 21 which is located below the container 1. On top of the carrier disk 13 are knives or tools, e.g. Cutting knife, 14 arranged, which together with the carrier plate 13, the mixing and / or crushing tool 3.
    As indicated schematically, the knives 14 are not arranged symmetrically on the support plate 13, but are particularly formed on their pointing in the direction of rotation or movement 12 front edges 22, employed or arranged to be able to act on the plastic material mechanically specific. The radially outermost edges of the mixing and crushing tools 3 extend to relatively close, about 5% of the radius 11 of the container 1, to the inner surface of the side wall 9 zoom.
    The container 1 has at the top a filling opening, through which the material to be processed, e.g. Portions of plastic films, e.g. is inserted by means of a conveyor in the direction of the arrow. Alternatively it can be provided that the container 1 is closed and at least evacuated to a technical vacuum, wherein the material is introduced via a lock systems. This material is detected by the rotating mixing and / or crushing tools 3 and swirled up in the form of a Mischtrombe 30, the good rises along the vertical side wall 9 and approximately in the range of effective container height H by gravity back in and out in the field of Tank center falls back. The effective height H of the container 1 is approximately equal to its inner diameter D. In the container 1 thus forms a Mischtrombe, in which the material is swirled both from top to bottom and in the direction of rotation 12. Such a device can thus be operated only with the predetermined direction of rotation or movement 12 due to the particular arrangement of the mixing and crushing tools 3 and the knife 14 and the direction of rotation 12 can not be made without further or without additional changes, be reversed.
    The introduced plastic material is comminuted by the circulating mixing and crushing tools 3, mixed and thereby heated by the introduced mechanical friction energy and softened, but not melted. After a certain residence time in the container 1, the homogenized, softened, doughy but not molten material, as will be discussed in detail below, discharged through an opening 8 from the container 1, brought into the catchment area of an extruder 5 and there by a screw 6th recorded and subsequently melted.
    At the height of the present in the single case erkfeinerungs- and mixing tool 3, said opening 8 is formed in the side wall 9 of the container 1, through which the pretreated plastic material from the interior of the container 1 can be ausbrlngbar. The material is transferred to a single-screw extruder 5 arranged tangentially on the container 1, the housing 16 of the extruder 5 having an intake opening 80 in its casing wall for the material to be detected by the screw 6. Such an embodiment has the advantage that the screw 6 can be driven by the lower front end in the drawing by a drive shown only schematically, so that the upper end of the screw 6 in the drawing can be kept free from the drive. This makes it possible to arrange the outlet opening for the plastified or agglomerated plastic material conveyed by the screw 6 at this right front end, e.g. in the form of an extruder head, not shown. The plastic material can therefore be conveyed through the outlet opening without deflection by the screw 6, which is not readily possible in the embodiments according to FIGS. 3 and 4.
    The intake opening 80 communicates with the opening 8 in material conveying or transfer connection and is in the present case directly, directly and without a longer intermediate piece or spacing connected to the opening 8. Only a very short transfer area is provided.
    In the housing 16, a compressing screw 6 is rotatably supported about its longitudinal axis 15. The longitudinal axis 15 of the screw 6 and the extruder 5 coincide. The extruder 5 conveys the material in the direction of arrow 17. The extruder 5 is a conventional extruder known per se, in which the softened plastic material is compressed and thereby melted, and the melt then emerges on the opposite side of the extruder head.
    The mixing and / or crushing tools 3 and the blades 14 are at almost the same height or level as the central longitudinal axis 15 of the extruder 5. The outermost ends of the blades 14 are sufficiently spaced from the webs of the screw 6.
    In the embodiment according to FIGS. 1 and 2, the extruder 5, as mentioned, is connected tangentially to the container 1 or extends tangentially to its cross section. The imaginary extension of the central longitudinal axis 15 of the extruder 5 or the screw 6 against the conveying direction 17 of the extruder 5 to the rear, leads in the drawing next to the axis of rotation 10 over without cutting them. The longitudinal axis 15 of the extruder 5 or the screw 6 is on the outlet side to the longitudinal axis 15 parallel, from the axis of rotation 10 of the mixing and / or crushing tool 3 in the conveying direction 17 of the extruder 5 outwardly directed ** ** · '* 4' ! · *
    Radial 11 of the container 1 offset by a distance 18. In the present case, the rearward extension of the longitudinal axis 15 of the extruder 5 does not penetrate the interior of the container 1, but runs just past it.
    The distance 18 is slightly larger than the radius of the container 1. The extruder 5 is thus slightly offset from the outside or the catchment area is slightly deeper.
    Under the terms "opposite", "opposite" " or "opposing" is understood herein to mean any orientation of the vectors to each other which is not acute-angled, as will be explained in detail below.
    In other words, the scalar product is a directional vector 19 of the direction of rotation 12, which is tangent to the circle of the outermost point of the mixing and / or comminution tool 3 or tangential to the plastic material passing past the opening 8 and the direction of rotation 12 the mixing and / or crushing tools 3, and a direction vector 17 of the conveying direction of the extruder 5, which is parallel to the central longitudinal axis 15 in the conveying direction at each point of the opening 8 and in the region radially immediately in front of the opening 8, zero everywhere or negative, but nowhere positive.
    In the intake opening in FIGS. 1 and 2, the dot product of the direction vector 19 of the direction of rotation 12 and the direction vector 17 of the conveying direction in each point of the opening 8 is negative.
    The angle α between the directional vector 17 of the conveying direction and the directional vector of the direction of rotation 19, measured in the most upstream of the direction of rotation 12 point 20 of the opening 8 and at the most upstream edge of the opening 8, is almost maximum, about 170 ° ,
    If you move along the opening 8 in Fig. 2 down, so in the direction of rotation 12, on, so the obtuse angle between the two direction vectors is always larger. In the middle of the opening 8 the angle between the directional vectors is about 180 "and the scalar product is maximally negative, further below that the angle is even > 180 ° and the scalar product decreases again, but always remains negative. However, these angles are no longer referred to as angles α, since they are not measured in point 20.
    A not shown in Fig. 2, measured in the middle or in the center of the opening 8 angle ß between the direction vector of the direction of rotation 19 and the direction vector of the conveying direction 17 is about 178 ° to 180 °.
    The device according to FIG. 2 represents the first limiting case or extreme value. In such an arrangement, a very gentle stuffing action or a particularly advantageous feeding is possible and such a device is particularly suitable for sensitive 16
    Materials that are worked near the smelting area or favorable for aft ^ streaked good.
    The radial distance of the tool mb, measured from the radially outermost point or from the outermost tip of the blade 14 or the circle defined thereby, to the inner surface of the side wall 9 of the container 1 is shown by way of example in FIG. This satisfies the relationship mb = k * DB.
    Likewise, the radial distance of the tool carrier mc, measured from the radially outermost point of the round carrier disk 13, to the inner surface of the side wall 9 of the container 1 is located. This satisfies the relation DB = k2 * Dw.
    The distance mc is greater than the distance mb, the tools or knives 14 are thus projecting beyond the support disk 13.
    In FIGS. 3 and 4, the distances mc and mb have not been drawn. These figures serve primarily to illustrate the connectivity of the extruder.
    In Fig. 3, an alternative embodiment is shown, in which the extruder 5 is not connected tangentially, but with its end face 7 to the container 1. The screw 6 and the housing 16 of the extruder 5 are adapted in the region of the opening 8 to the contour of the inner wall of the container 1 and set back flush. No part of the extruder 5 protrudes through the opening 8 into the interior of the container 1.
    The distance 18 here corresponds to about 5 to 10% of the radius 11 of the container 1 and about half the inner diameter d of the housing 16. This Ausführungsfrom thus represents the second limiting case or extreme value with the smallest possible offset or distance 18, in which the rotary or the direction of movement 12 of the mixing and / or crushing tools 3 of the conveying direction 17 of the extruder 5 is at least slightly opposite, namely over the entire surface of the opening eighth
    The scalar product is exactly zero in FIG. 3 at the most upstreammost point 20 located at the most upstream edge of the orifice 8. The angle α between the direction vector 17 of the conveying direction and the direction vector of the direction of rotation 19, measured at point 20 of Fig. 3, exactly 90 °. If you continue along the opening 8 down, ie in the direction of rotation 12, on, so the angle between the direction vectors is always larger and at an obtuse angle > 90 "and the scalar product becomes negative at the same time. At no point or in any area of the opening 8 is the scale product 17 "positive, however, or the angle smaller than 90 °. As a result of this, local overfeeding can not take place in a partial area of the opening 8 or, in any region of the opening 8, can not result in a damaging excessive tamping action.
    This also makes a decisive difference to a purely radial arrangement, since at point 20 or at the edge 20 'bet a fully radial arrangement of the extruder 5 is an angle α < 90 ° and those areas of the opening 8, which are located in the drawing above the radial 11 and upstream or upstream thereof, would have a positive scalar product. This could lead to accumulation of locally melted plastic goods in these areas.
    FIG. 4 shows a further alternative embodiment in which the extruder 5 is displaced slightly more downstream than in FIG. 3, but not yet tangentially as in FIGS. 1 and 2. In the present case, as in FIG. 3, the extension of the longitudinal axis 15 of the extruder 5, which is intended to be rearward, penetrates the interior of the container 1 in a secant manner. This has the consequence that - measured in the circumferential direction of the container 1 - the opening 8 is wider than in the embodiment of FIG. 3, Also, the distance 18 is correspondingly larger than in FIG. 3, but slightly smaller than the smaller radius 11th The angle α measured at point 20 is about 150 ", which reduces the stuffing effect compared with the device of Fig. 3, which is more advantageous for certain sensitive polymers. The viewed from the container 1 from right inner edge or the inner wall of the housing 16 connects tangentially to the container 1, whereby, in contrast to Fig. 3 no blunt transitional edge is formed. In this furthest downstream point of the opening 8, in Fig. 4 leftmost, the angle is about 180 °. EXAMPLE:
    Representation of a comparative experiment between a plant according to the prior art (Fig. 5) and a plant according to the invention (Fig. 6):
    Both plants were plants with a cutting compressor with a diameter of 1100 mm, with a tangentially connected 80 mm extruder (basically constructed as in Fig. 1 and 2). The operating parameters were the same. The material used was un-shredded polypropylene film (PP).
    In contrast to the known system, the direction of rotation of the tools in the cutting compressor was reversed in opposite directions, as shown in Fig. 2 in the inventive system. In addition, the distance of the protruding over the support disk tools to the wall was determined to be 35 mm. 18; ··· *. , ,,, * .. *: · '
    It is shown in the respective lower curves da's OfeTiffioment the cutting compressor, which reflects the cutting or compaction work.
    The respective upper curves show the melt pressure upstream of a filtration device. This reflects the throughput and the constancy of the throughput again.
    It can be seen clearly that in the plant of the prior art, the throughput constant over time was lower than in the system according to the invention. Furthermore, it can be seen that the state of the art system has had a problem with the filling of the screw at least once (around 12:30).
    权利要求:
    Claims (19)
    [1]
    19

    1. Apparatus for pretreating and subsequently conveying, plasticizing or agglomerating plastics, in particular thermoplastic waste plastic for recycling purposes, with a container (1) for the material to be processed, wherein in the container (1) at least one about an axis of rotation (10) rotatable circulating mixing and / or crushing tool (3) for mixing, heating and optionally comminution of the plastic material is arranged, wherein in a side wall (9) of the container (1) in the region of the height of the bottom or bottom mixing and / or Crushing tool (3) an opening (8) is formed through which the pretreated plastic material from the interior of the container (1) can be discharged, wherein at least one conveyor (5), in particular an extruder (5), is provided for receiving the pretreated material , with at least one in a housing (16) rotating, in particular plasticizing or agglomerating worm (6), wherein the housing (16) has a feed opening (80) on its end face (7) or in its jacket wall for the material to be detected by the worm (6), and the feed opening (80) with the Opening (8) is connected, characterized in that the imaginary extension of the central longitudinal axis (15) of the conveyor (5) or of the intake opening (80) nearest the screw (6) against the conveying direction (17) of the conveyor (5) the axis of rotation (10) passes without cutting them, wherein the longitudinal axis (15) of the conveyor (5) or of the intake opening (80) nearest screw (6) on the drain side or in the direction of rotation or movement (12) of the mixing and / or crushing tool (3) to the longitudinal axis (15) parallel, from the axis of rotation (10) of the mixing and / or crushing tool (3) in the conveying direction (17) of the conveyor (5) outwardly directed radials (11) of the container (1) by a distance (18) ve is replaced, and that the radial distance of the tool (mb), measured from the radially outermost point of the ground nearest mixing and / or crushing tool (3), or there provided tools and / or knives (14), or defined by this point Circle, to the inner surface of the side wall (9) of the container (1) in the range of 15 mm to 120 mm, preferably in the range of 20 mm to 80 mm, and satisfies the following relation: mb = k * DB 20 »♦ where DB ... is the inner diameter of a circular cylindrical container (1) in mm, or the inner diameter in mm of a fictitious Kreiszyiische container of the same height converted to the same Fassungsvoiumen, and k ... is a constant in the range of 0.006 to 0.16.
    [2]
    2. Apparatus according to claim 1, characterized in that in the container (1) at least one about the axis of rotation (10) rotatable, circulating Wertzeugträger (13) is provided on / in which the / the mixing and / or crushing tool (s) (3) are arranged or formed, wherein the tool carrier (13) is preferably a, in particular parallel to the bottom surface (12) arranged, carrier plate (13).
    [3]
    3. Device according to one of claims 1 or 2, characterized in that the mixing and / or crushing tool (3) and / or the tool carrier (13) tools and / or knives (14), in the rotational or movement direction (12) on the plastic material crushing, cutting and / or heating act, the mixing and / or crushing tool (3) or the tools and / or knife (14) preferably arranged or formed on the top of the tool carrier (13) are.
    [4]
    4. Device according to one of claims 1 to 3, characterized in that the radial distance of the tool carrier (mc), measured from the radially outermost point of the ground closest tool carrier (13) or of the defined by this point circle, to the inner surface of the side wall ( 9) of the container (1) in the range of 30 mm to 210 mm, preferably in the range of 40 mm to 150 mm.
    [5]
    5. Device according to one of claims 1 to 4, characterized in that the ratio between the inner diameter DB of the container (1) and the diameter (Dw) of the radially outermost point of the bottom tool carrier (13) formed circle fulfills the following relationship; Db - k2 * Dw where Dß ... the inner diameter of the container (1) in mm, Dw. k2 ... the diameter of the circle formed by the radially outermost point of the tool holder (13) in mm, is a constant in the range of 1.01 to 1.5.
    [6]
    6. Device according to one of claims 1 to 5, characterized in that the constant k2 in containers (1) with an inner diameter of DB is greater than or equal to 1300 mm in the range of 1.01 to 1.12.
    [7]
    7. Device according to one of claims 1 to 6, characterized in that the radial distance of the tool carrier (mc) is greater than or equal to the radial distance of the tool (mb).
    [8]
    8. Device according to one of claims 1 to 7, characterized in that the tools and / or knives (14) on the radially outermost, to the inner surface of the side wall (9) facing, usually vertical, outer edge of the tool carrier (13). arranged, reversibly releasably secured or formed therein or incorporated.
    [9]
    9. Device according to one of claims 1 to 8, characterized in that for an associated with the container (1) conveyor (5) the scalar product formed from the tangential to the circle of the radially outermost point of the mixing and / or crushing tool ( 3) or tangentially to the plastic material moved past the opening (8) and oriented normal to a radial (11) of the container (1), pointing in the direction of rotation or movement (12) of the mixing and / or comminution tool (3) Direction vector of the direction of rotation (19) and the direction vector (17) of the conveying direction of the conveyor (5) in each individual point or in the entire region of the opening (8) or immediately radially in front of the opening (8) is zero or negative.
    [10]
    10. Device according to one of claims 1 to 9, characterized in that the direction vector of the direction of rotation (19) of the radially outermost point of the mixing and / or crushing tool (3) and the directional vector (17) of the conveying direction of the conveyor (5) Include angle (a) greater than or equal to 90e and less than or equal to 180 °, measured at the intersection of the two directional vectors (17,19) with respect to the rotational or movement direction (12) of the mixing and / or crushing tool (3) upstream located upstream edge of the opening (8), in particular in the furthest upstream point (20) on this edge or the opening (8).
    [11]
    11. Device according to one of claims 1 to 10, characterized in that the direction vector (19) of the rotational or movement direction (12) and the direction vector (17) of the conveying direction of the conveyor (5) an angle (ß) between 170 " and 180 °, measured at the intersection of the two directional vectors (17,19) in the middle of the opening (8).
    [12]
    12. Device according to one of claims 1 to 11, characterized in that the distance (18) is greater than or equal to half the inner diameter of the housing (16) of the conveyor (5) or the screw (6), and / or greater than or equal to 7%, preferably greater than or equal to 20%, of the radius of the container (1) or that the distance (18) is greater than or equal to the radius of the container (1).
    [13]
    13. Device according to one of claims 1 to 12, characterized in that the imaginary extension of the longitudinal axis (15) of the conveyor (5) counter to the conveying direction in the manner of a secant to the cross section of the container (1) is arranged and the interior of the container ( 1) interspersed at least in sections.
    [14]
    14. Device according to one of claims 1 to 13, characterized in that the conveyor (5) is connected tangentially to the container (1) or tangential to the cross section of the container (1) or that the longitudinal axis (15) of the conveyor (5) or the screw (6) or the longitudinal axis of the screw (6) closest to the intake opening (80) or the inner wall of the housing (16) or the envelope of the check (6) tangentially to the inside of the side wall (9) of the Container (1) extends, wherein preferably the screw (6) on its end face (7) is connected to a drive and at its opposite end to a front end of the housing (16) arranged outlet opening, in particular an extruder head promotes.
    [15]
    15. Device according to one of claims 1 to 14, characterized in that the opening (8) directly and directly and without significant spacing, in particular without transfer path or screw conveyor, with the intake opening (80) is connected.
    [16]
    16. Device according to one of claims 1 to 15, characterized in that the material acting in the direction of rotation or movement (12) facing the front areas or leading edges (22) of the mixing and / or crushing tools (3) or Knife (14) are formed differently, employed, curved and / or arranged in comparison to those in rotational or BewegungsricTituηξ (* 17) * trailing or trailing areas.
    [17]
    17. Device according to one of claims 1 to 16, characterized in that the container (1) is formed substantially circular cylindrical with a flat bottom surface (2) and a vertically oriented cylinder jacket-shaped side wall (9) and / or the axis of rotation (10). the mixing and / or comminution tools (3) coincide with the central center axis of the container (1) and / or the axis of rotation (12) or the central center axis are aligned vertically and / or normal to the bottom surface (2).
    [18]
    18. Device according to one of claims 1 to 17, characterized in that the lowermost, bottom tool carrier (13) and the lowest of the mixing and / or crushing tools (3) and / or the opening (8) near the ground at a small distance from Bottom surface (2), in particular in the region of the lowest part of the height of the container (1), preferably at a distance from the bottom surface (2) of 10 mm to 400 mm are arranged.
    [19]
    19. Device according to one of claims 1 to 18, characterized in that the conveyor (5) is a single screw extruder (6) with a single compressing screw (6) or is a double or multiple screw extruder, wherein the diameters d of the individual screws ( 6) are equal to each other.
    类似技术:
    公开号 | 公开日 | 专利标题
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    同族专利:
    公开号 | 公开日
    CN103857505B|2017-07-18|
    ZA201402102B|2015-03-25|
    BR112014008841A2|2017-04-25|
    RU2014119374A|2015-11-20|
    DE202012012573U1|2013-06-07|
    WO2013052980A1|2013-04-18|
    CA2851661A1|2013-04-18|
    TW201332733A|2013-08-16|
    RU2582710C2|2016-04-27|
    UA109962C2|2015-10-26|
    MX344509B|2016-12-19|
    ES2561721T3|2016-02-29|
    SI2766159T1|2016-04-29|
    AU2012323809B2|2016-02-25|
    US20140252147A1|2014-09-11|
    MX2014004454A|2014-09-22|
    AT512146B1|2015-02-15|
    JP2014530131A|2014-11-17|
    CA2851661C|2018-04-03|
    BR112014008841B1|2020-07-28|
    PL2766159T3|2016-06-30|
    AU2012323809A1|2014-05-15|
    KR20140078744A|2014-06-25|
    TWI501851B|2015-10-01|
    EP2766159A1|2014-08-20|
    HK1200763A1|2015-08-14|
    CN103857505A|2014-06-11|
    DK2766159T3|2016-03-14|
    HUE027085T2|2016-08-29|
    US9296128B2|2016-03-29|
    EP2766159B1|2015-12-16|
    KR101744267B1|2017-06-07|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA1501/2011A|AT512146B1|2011-10-14|2011-10-14|DEVICE FOR PREPARING PLASTIC MATERIAL|ATA1501/2011A| AT512146B1|2011-10-14|2011-10-14|DEVICE FOR PREPARING PLASTIC MATERIAL|
    RU2014119374/05A| RU2582710C2|2011-10-14|2012-10-12|Device for processing polymer material|
    DK12781256.8T| DK2766159T3|2011-10-14|2012-10-12|An apparatus for processing plastics material|
    MX2014004454A| MX344509B|2011-10-14|2012-10-12|Apparatus for processing plastic material.|
    SI201230486T| SI2766159T1|2011-10-14|2012-10-12|Apparatus for processing plastic material|
    TW101137665A| TWI501851B|2011-10-14|2012-10-12|Apparatus for the treatment of plastics material|
    ES12781256.8T| ES2561721T3|2011-10-14|2012-10-12|Device for pretreating synthetic materials|
    US14/351,871| US9296128B2|2011-10-14|2012-10-12|Apparatus for the pretreatment and subsequent conveying, plastification, or agglomeration of plastics|
    KR1020147013009A| KR101744267B1|2011-10-14|2012-10-12|Apparatus for processing plastic material|
    CN201280050443.0A| CN103857505B|2011-10-14|2012-10-12|Device for preparing synthetic material|
    HUE12781256A| HUE027085T2|2011-10-14|2012-10-12|Apparatus for processing plastic material|
    AU2012323809A| AU2012323809B2|2011-10-14|2012-10-12|Apparatus for processing plastic material|
    EP12781256.8A| EP2766159B1|2011-10-14|2012-10-12|Apparatus for processing plastic material|
    PCT/AT2012/050152| WO2013052980A1|2011-10-14|2012-10-12|Apparatus for processing plastic material|
    PL12781256T| PL2766159T3|2011-10-14|2012-10-12|Apparatus for processing plastic material|
    CA2851661A| CA2851661C|2011-10-14|2012-10-12|Apparatus for the pretreatment and subsequent conveying, plastification or agglomeration of plastics|
    DE201220012573| DE202012012573U1|2011-10-14|2012-10-12|Device for processing plastic material|
    BR112014008841-1A| BR112014008841B1|2011-10-14|2012-10-12|device for pre-treatment and subsequent transport, plasticization or agglomeration of plastics, in particular thermoplastic waste for recycling|
    JP2014534872A| JP2014530131A|2011-10-14|2012-10-12|Plastic material processing equipment|
    UAA201403397A| UA109962C2|2011-10-14|2012-10-12|DEVICES FOR PRE-TREATMENT AND FURTHER TRANSPORT, PLASTIFICATION, OR AGLOMERATION OF PLASTIC MATERIALS|
    ZA2014/02102A| ZA201402102B|2011-10-14|2014-03-20|Apparatus for processing plastic material|
    HK15101327.5A| HK1200763A1|2011-10-14|2015-02-06|Apparatus for processing plastic material|
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