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[0001] 1. Field of the Invention
[0002] This invention relates to an extrusion head with an extrusion die for extruding a tube-shaped strand from at least one thermoplastic melt for producing blown films, wherein the extrusion head has an internal member arranged around a center axis and an external member, and an annular space is formed between the internal member and the external member. The annular space extends concentrically with respect to the center axis and terminates in the extrusion die, and the external member has at least one extrusion module with two extrusion members, which are arranged on top of each other and are ring-shaped and plate-shaped. A separating gap, which terminates in the annular space, is formed between the two extrusion members of each one of the extrusion modules, and each extrusion module has a feed line for a plastic melt and a channel system for distributing the plastic melt as far as into the annular space is formed in each extrusion module.
[0003] 2. Description of Related Art
[0004] A channel system for distributing a plastic melt into an annular space of an extrusion head has an important part in achieving even product quality, because it is intended with the channel system to provide an even distribution of the molten thermoplastic material customarily supplied through a peripheral channel in as even as possible portions into the entire annular space. In this case a distinction is made between so-called vertical spiral coil distributors, wherein there is a channel system for distributing the plastic melt in the axial direction of the extrusion head. Reference is made in this connection to U.S. Pat. No. 4,182,603, for example.
[0005] Extrusion heads in accordance with U.S. Pat. No. 4,895,744 and U.S. Pat. No. 5,069,612 are known, wherein the extrusion head is constructed in a module-like manner from several extrusion modules. Each extrusion module has a channel system for distributing the plastic melt provided, which is embodied on conical surfaces extending in the axial direction of the extrusion head toward the annular space.
[0006] An extrusion head for producing blown films is known from U.S. Pat. No. 3,809,515, wherein the extrusion head is divided into extrusion modules vertically in relation to its center axis and the channel system for distributing the melt is arranged vertically with respect to the axial direction, wherein the plastic melt is fed centrally in the center axis and from there is distributed into the annular space radially toward the exterior.
[0007] An extrusion head for producing a blown film is known from German Patent Reference DE 42 18 095 C2, wherein the channel system inside the extrusion head is embodied on a level extending vertically with respect to the axis of the extrusion head, wherein feeding of the plastic melt takes place from the outside and the plastic melt is distributed moving from the outside toward the inside.
[0008] An extrusion head for producing single-layered or multi-layered tubular films is known from French Patent Reference FR 26 25 941, wherein the extrusion head is also divided vertically with respect to its axial direction into a plurality of extrusion modules, each of which has an annular plate. The channel system for distributing the melt is distributed to the individual annular plates of the extrusion head, for example from the feeding of the plastic melt at the circumference of the extrusion head to the entry into the annular space, the channel system, and therefore the plastic melt, passes through five annular plates, which form one extrusion module.
[0009] Extrusion heads with several extrusion modules make possible the extrusion of multi-layered tube-shaped strands from different thermoplastic melts, which are thereafter blown to form appropriate multi-layered blown films. A goal is a construction of the extrusion head which is a compact as possible and space-saving and has a multitude of identical parts for embodying the individual extrusion modules for supplying respectively one plastic melt in order to assure low production and operating costs. Another goal is a modular construction of the extrusion members, along with as simple as possible an assembly and disassembly. At the same time as homogeneous and even a distribution as possible of the supplied plastic melt in the channel system of each extrusion module should take place, wherein it is also intended to work thermoplastic melts of different raw materials in one extrusion head, and an even distribution and supply of the melt into the annular space is intended to be assured.
[0010] It is one object of this invention to provide an extrusion head in accordance with the species which is distinguished by a particularly compact and space-saving embodiment, and which offers an efficient channel system for distributing the plastic melt, which makes possible as even a distribution of the plastic melt as possible over a short distance into the annular space, and thus the even extrusion of different raw materials to form single-layered or multi-layered blown films. The extrusion head is intended to be assembled from as great as possible a number of identical parts, and also from parts which are easy to produce.
[0011] To attain this object, the invention proposes the design of an extrusion head having characteristics of described in this specification and in the claims.
[0012] The above object is accomplished with an extrusion head having a channel system of each extrusion module which comprises an inlet area, a branching area and a spiral area, wherein the spiral area terminates into the annular space in a ring-shaped distribution surface with a ring-shaped outlet opening. The inlet area, the branching area and the spiral area of the channel system each extend on a separate level, wherein the level of the inlet area extends between the level of the branching area and the level of the spiral area. The channel system of the inlet area is connected with the channel system of the branching area by a first group of connecting channels, which lead from the level of the inlet area to the level of the branching area. The channel system of the branching area is connected with the channel system of the spiral area by a second group of connecting channels leading from the level of the branching area to the level of the spiral area.
[0013] For creating the particularly compact and variable modular construction, as well as the even distribution of the plastic melt within the extrusion head, or respectively within each extrusion module, which is one object of this invention, the channel system is divided and an inlet area and a branching area are placed upstream of the spiral area, by which an effective pre-distribution of the plastic melt fed in is already provided. Moreover, all distribution areas of the channel system of an extrusion module of the extrusion head designed in accordance with this invention are arranged on different levels, so that a particularly space-saving design of the extrusion head from a multitude of extrusion modules results, and uniformity of the melt distribution is also achieved.
[0014] In accordance with this invention, the plastic melt fed in a manner known per se to an extrusion module of the extrusion head in accordance with this invention initially passes through an inlet area on a mid-level, is transferred from there through a group of first connecting channels to a second level, identified as a branching area and which is a multitude of branching channels, and at the end of the branching channels the plastic melt finally reaches a third level through a group of second connecting channels, in which the spiral channels are arranged, which form the spiral area and cause the even feeding of the molten plastic material into the annular space. Because of the arrangement selected, having a level of the inlet area arranged between the level of the branching area and the level of the spiral area, the plastic melt passes through the group of second connecting channels to the level of the inlet area during its passage from the branching area into the spiral area, so that an extremely compact multiple branching is created.
[0015] Each extrusion module of the extrusion head in accordance with this invention is formed from two extrusion members, which are arranged stack-like one above the other and between which a separating gap is formed, which is used for supplying the plastic melt, which was evenly distributed by the channel system, to the annular space. The distribution surface adjoining the spiral area extends along the separating gap toward the annular space.
[0016] In accordance with this invention, the channel system is formed only on one extrusion member of each extrusion module. Preferably, the channel system with the inlet area, the branching area, the spiral area and the two groups of connecting channels is embodied in the extrusion member of each extrusion module which is facing away from the extrusion die and is identified as the lower member of the extrusion module. The second extrusion member, identified as the upper member of the extrusion module, is placed on the surface of the lower member of the extrusion module having the spiral area, so that the separating gap is formed. The extrusion members are embodied in a ring shape and a plate shape or disk shape. The spiral area of the channel system is formed in the surface of the lower member of the extrusion module facing the separating gap. The branching area of the channel system is formed in the oppositely located surface, facing away from the separating gap, of the lower member of the extrusion module. The inlet area of the channel system is formed between these surfaces within the lower member of the extrusion module. The three levels of the channel system of this invention in an extrusion module for the even distribution of the plastic melt supplied to the extrusion module are only realized in one extrusion member, for example a component of each one of the extrusion modules, namely the spiral area and the branching area at the upper and underside of the one extrusion member, and the inlet area between these two levels within the same extrusion member.
[0017] For forming the flow cross-section for the plastic systems, the channel system of the spiral area is formed by known spiral channels and the channel system of the branching area by branching channels, wherein the spiral channels forming the spiral area and/or the branching channels forming the branching area are cut, for example milled, in the form of grooves into the surfaces of the one extrusion member.
[0018] It is more elaborate, though also possible within the scope of this invention, to form the spiral channels of the spiral area on both sides of the spiral level in the surface of the lower member of the extrusion module, as well as complementary in the surface of the adjoining upper member of the extrusion module along the separating gap.
[0019] In accordance with a another embodiment of this invention, it is possible to provide the lower member of the extrusion module in which the channel system is embodied with a circumferential annular groove on the surface located opposite the surface having the spiral channels, into which a pre-distribution ring can be inserted. The pre-distribution ring has a surface resting against the groove bottom of the annular groove. The branching area is formed on the surface of the lower member of the extrusion module in the area of the groove bottom of the annular groove. It is thus possible to move the level of the branching area out of the separating gap of two adjoining extrusion modules and to seal it with the pre-distribution ring inserted into the annular groove.
[0020] In this case the branching channels forming the branching area are advantageously formed with a part of their cross section in the groove bottom of the annular groove of the lower member of the extrusion module, and with a complementary part in the area of the pre-distribution ring resting against the groove bottom, for example, one half in each one, so that one half of corresponding branching channels of a circular cross section, for example, is respectively formed in the lower member of the extrusion module and in the pre-distribution ring, for appropriately joining together during assembly and closing. It is also possible to form the branching channels exclusively in the lower member of the extrusion module, or exclusively in the pre-distribution ring, and to sealingly close the cross sections of the branching channels by placing the members against each other.
[0021] With one embodiment of the extrusion head in accordance with this invention having several extrusion modules arranged on top of each other, the pre-distribution ring inserted into one extrusion member can also advantageously be used as an adapter ring for the extrusion modules to be placed on top of each other. For this purpose, the pre-distribution ring has a greater thickness than would correspond to the depth of the annular groove of the lower member of the extrusion module provided with the channel system, so that the pre-distribution ring protrudes with a portion of its cross section beyond the annular groove in the direction toward the adjoining extrusion module, and the projecting portion of the pre-distribution ring can be fitted into a complementary designed annular groove on the top of the upper member of the extrusion module of an adjoining following extrusion module. It is thus possible to effectively reduce the structural height of the extrusion head in accordance with this invention, even when it has several extrusion modules arranged on top of each other, and at the same time the pre-distribution ring of each extrusion module is arranged and seated exactly within the extrusion head.
[0022] The pre-distribution ring can be releasably fastened in the annular groove of the lower member of the extrusion module, for example, it can be screwed into this annular groove using suitable screws, in order to form the branching channels forming the branching area of the lower member of the extrusion module, in particular in an exactly positioned manner.
[0023] The inlet area of each extrusion module of the extrusion head in accordance with this invention is advantageously formed by two inlet channels, which are arranged in a V-shape relative to each other and extend from the circumference of the first extrusion member, and respectively lead to a first connecting channel, which provides communication with the branching area. Thus a division of the plastic melt into two portions of equal size is performed in the inlet area formed by the two inlet channels, which portions are transferred through the first connecting channels to the branching area and are further divided there, until finally they are uniformly fed from the spiral area into the annular groove. The arrangement of the inlet channels in such a way that they start at the circumference of the first extrusion member also allows the connection at the circumference of the extrusion installations for producing and feeding of the plastic melt without further structural outlay.
[0024] Two branching systems are formed symmetrically with respect to each other, starting at the connecting channels emanating from the inlet channels, and each branching system again branches into four identical branching channels. The eight ends of the four identical branching channels are evenly distributed on a circular ring coaxially with respect to the center axis of the extrusion head, and respectively communicate with a connecting channel leading to the spiral area. Thus the branching area of the extrusion head in accordance with this invention includes, for example, a system of branching channels leading to eight second connecting channels, so that the plastic melt entering via the inlet area, which transitions via the first group of connecting channels into the branching area, is divided into eight partial flows in the branching channels. These eight partial flows enter into the spiral area through the second connecting channels.
[0025] The spiral area itself advantageously comprises several spiral channels placed inside each other and extending in a converging manner, which run radially from the outside toward the inside and which communicate at their radially outside located ends with a connecting channel coming from the branching area. In the case of eight communicating channels routed from the eight ends of the branching channels, eight spiral channels are thus advantageously provided. Depending on the size and layout of the extrusion head in accordance with this invention, varying embodiments regarding the number of inlet channels, group of the first connecting channels, branching channels and group of the second connecting channels, as well as spiral channels, are of course possible.
[0026] To assure as even as possible a distribution of the plastic melt when it enters into the annular space, the spiral channels have a flow cross section for the plastic melt which decreases from the outside toward the inside, so that the melt is accelerated when flowing toward the annular space.
[0027] In a particularly advantageous embodiment of the extrusion head in accordance with this invention, all flow paths for the plastic melt through the channel system in one extrusion module are designed to be of equal length, so that there is an even effect of the channel system on all partial flows of the plastic melt, and in particular a homogeneous temperature and distribution of plastic melt is obtained.
[0028] A particularly compact structure of the extrusion head is achieved in accordance with this invention because the levels of the inlet area, the distribution area and the spiral area of one extrusion module are arranged parallel with respect to each other. These levels are advantageously arranged so they extend vertically with respect to the center axis of the extrusion head. It is also possible, according to this invention, to provide different orientations of the levels in relation to the center axis.
[0029] A further advantageous construction of the extrusion head of this invention has connecting channels of the first group, which connect the inlet area of the channel system with the branching area of the channel system. The connecting channels of the second group, which connect the branching area of the channel system with the spiral area of the channel system, are embodied to extend vertically with respect to the levels of the channel system and coaxially with respect to the center axis of the extrusion head.
[0030] All extrusion modules of the extrusion head in accordance with this invention can be separately heated, so that the plastic melts conducted through these extrusion modules can be discharged within the respectively optimum temperature range, and damaging thermal effects are kept away to a great extent from the plastic melt.
[0031] This invention is explained in further detail in what follows by means of the drawings, which represent only one exemplary embodiment, wherein:
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[0042] A device for extruding and blowing a multi-layered blown film
[0043] This invention relates to the structure and design of the extrusion head
[0044] The external member
[0045] With an uneven number of extrusion modules, an extrusion module located on the exterior respectively remains which can only be screwed together with a half-length screw
[0046] Each extrusion module
[0047] Each extrusion module
[0048] In
[0049] On its circumference, the lower member
[0050] The level EE of the inlet area E extends between the two other levels EV and ES of the branching area V and of the spiral area S, wherein all three levels EE, EV and ES essentially extend parallel with each other, and in the exemplary embodiment the three levels also extend essentially vertically with respect to the center axis A of the extrusion head
[0051] A circumferential annular groove
[0052] It is possible to cut the required flow cross section of the branching area V completely into the surface
[0053] A mirror-reversed channel system
[0054] For example, it is possible to see in
[0055] The pre-distribution ring
[0056] Respective connecting channels
[0057] Starting on the level EV of the branching area, these second connecting channels
[0058] The arrangement of the second connecting channels
[0059] On the top
[0060] Because of the spiral-shaped arrangement of the individual spiral channels
[0061] The level ES of the spiral area borders on the separating gap
[0062] The plastic melt entering the extrusion module through the inlet opening
[0063] The individual spiral channels having a decreasing flow cross section toward their end
[0064] It is important for good homogenization that all paths in the above explained channel system
[0065] Based on the fact that the entire channel system
[0066] It can be seen from the drawings that all levels EE, EV, ES of the inlet, branching, or spiral areas extend parallel with respect to each other and vertically in relation to the longitudinal axis A of the extrusion head
[0067] However, this geometry is only shown by way of example, orientations of the levels EE, EV and ES and/or the connecting channels
[0068] A particularly efficient construction of the extrusion head is assured because a large number of identical parts is employed, which can be clearly perceived in
[0069] For achieving a particularly compact and space-saving construction, for several extrusion models, such as shown in
[0070] The bores
[0071] The internal member of the extrusion head embodied as an interior mandrel
[0072] Since moreover, based on the previously explained melt distribution system of each extrusion module