Interfacial surface generator

Abstract: Multilayer films are generated by dividing a first stream comprised of discrete layers of one or more materials into a plurality of branch streams (14,16,18,20), redirecting or repositioning (40) the branch streams, expanding (48) and contracting (54) the branch streams in a symmetrical fashion, and recombining (56) the branch streams to form a second stream having a greater number of discrete layers than the first stream. Alternatively, the branch streams are redirected or repositioned (64), recombined (68) to form a second stream having a greater number of discrete layers than the first stream, and the second stream expanded and contracted (66) in a symmetrical fashion. A gradient in, or other distribution of, thickness is provided by independently controlling (58,60) the flow rates of the branch streams.

Description: This invention relates to interfacial surface generators and to methods of generating interfacial surfaces in a fluid mass. A number of multilayer film structures have been devised wherein an ordered arrangement of layers of various materials in particular layer thicknesses is desired. Exemplary of these structures are those which produce an optical or visual effect because of the interaction of contiguous layers of materials having different refractive indices and layer thicknesses. In films such as those described in US-A-3,711,176 to Schrenk et al., it is further desirable that a gradient or other distribution in the thicknesses of layers of one or more materials be established through the thickness of the film. Multilayer films have previously been made or suggested to be made by the use of complex coextrusion feedblocks alone, see, for example, US-A-3,773,882 and US-A-3,884,606 to Schrenk, and the suggestion has been made to modify such a device to permit individual layer thickness control, see US-A-3,687,589 to Schrenk. Such modified feedblocks could be used to make a multilayer film with the desired layer thickness gradient or distribution of layer thicknesses from one major surface of the film to an opposing surface. These devices are very difficult and costly to manufacture, however, and are limited in practical terms to making films of no more than about three hundred total layers. Moreover, these devices are complex to operate and not easily changed over from the manufacture of one film construction to another. Multilayer films have also been made or suggested to be made by a combination of a feedblock and one or more interfacial surface generators (ISG's) in series, for example as described in US-A-3,565,985 to Schrenk et al. Such a combination would generally be preferred for producing a film of a given number of layers over the use of only the modified, multilayer feedblocks discussed previously, because of the greater flexibility or adaptability and lesser manufacturing costs associated with a feedblock/ISG combination. Previous ISG's have not been designed for the manufacture of multilayer films, however, but for the mixing of highly viscous materials such as melts of various thermoplastics. These known ISG's have operated generally by forcing the viscous fluids to be mixed through a series of passageways which repeatedly separate and recombine stream elements during the flow of a stream of viscous fluids through the apparatus, with the intent generally of creating interfacial surfaces by repeated divisions of layers or aggregations generally of a given material. Distortions and disruptions of the layers in a given stream of materials result from these divisions and recombinations, so that a second stream of materials exiting even one ISG may depart significantly from the desired character and/or configuration of the layers in a coextruded first composite stream from a feedblock. These distortions, moreover, are multiplied where several ISG's are used in series. Additionally, conventional ISG's which divide an incoming layered stream of materials into several layered branch streams, and which then rearrange and stack the branch streams simply perpetuate with the aforementioned distortions the original configuration of the layers in the first composite stream, rather than extending this configuration throughout the thickness of the second composite stream or the multilayer film prepared therefrom. For example, a monotonic distribution of the thicknesses of layers of a material A within a first composite stream would be repeated as a sawtooth-like pattern in a film prepared by a combination of a feedblock and a conventional ISG. The present invention solves these problems by a novel method and apparatus for making multilayer films having a prescribed layer thickness gradient in, or other distribution of, the thicknesses of layers of one or more materials from one major surface of the film to an opposing surface. According to the present invention, there is provided a method for making multilayer films having a prescribed distribution of layer thicknesses from one major surface of the film to an opposing surface, comprising the steps of: dividing a first composite stream comprised of discrete layers of one or more materials, of which at least a pair of said layers define a planar layer interface therebetween which lies in an x-z plane of a Cartesian coordinate system, wherein the z-axis is taken as extending in the direction of flow of the first composite stream, the x-axis extends transversely of the first composite stream and defines a transverse dimension of the layer interface, and the y-axis extends perpendicularly away from said layer interface in the thickness direction of said pair of layers, along the x-axis such that said pair of layers and said layer interface are distributed among at least branch streams; and, in any practical order, repositioning said at least two branch streams along both of the x- and y-axes as the branch streams flow along the z-axis; symmetrically expanding along the x-axis a transverse dimension and symmetrically contracting along the y-axis the thickness of the individual or combined said at least two branch streams; independently controlling the flow rates of said at least two branch streams; and recombining the branch streams to form a second composite stream having a greater number of discrete layers than the first composite stream and distributed in the prescribed distribution. In a first embodiment, a first stream comprising discrete layers of the one or more materials is divided into a plurality of branch streams, these branch streams are redirected or repositioned and individually symmetrically expanded and contracted, the resistance to flow through the apparatus and thus the flow rates of each of the branch streams are independently adjusted, and the branch streams recombined to form a second stream having a greater number of discrete, overlapping layers of the one or more materials distributed in the prescribed gradient or other distribution. In a second, alternate embodiment, the branch streams are created, repositioned, independently adjusted to a desired flow rate and recombined, and the second stream is symmetrically expanded and contracted. Figure 1 is a schematic illustration of the practice of a method of the present invention for forming a multilayer stream from a first composite stream comprising two discrete and substantially continuous layers of diverse thermoplastic materials. Figure 2 is an isometric view of a first embodiment of an apparatus of the present invention as a whole. Figure 3-6 are views in isolation of conduits within a first portion or sub-element of the apparatus of Figure 2, taken from the front or upstream side of the first sub-element and showing the flow paths of fluids moving through the apparatus and through the conduits. Figure 7 is a rear or downstream face view of the first sub-element shown in Figures 3-6. Figure 8 is a front view of a second portion or sub-element of the apparatus of Figure 2, showing conduits within the second sub-element corresponding to the conduits in the first sub-element. Figure 9 is a top view of the conduits within the second sub-element of Figure 8, showing the direction of fluid flow through the conduits and through the second sub-element. Figure 10 is a side view of the conduits of the second sub-element, showing again the flow path of fluids through the conduits. Figure 11 is a rear view of the second sub-element depicted in Figures 8-10. Figure 12 is a front view of the third sub-element of the apparatus of Figure 2, showing conduits which correspond at their entrances to the exits of the conduits in the second sub-element, and which converge to a common exit. Figure 13 is a view in cross-section of the convergence of the conduits in a first embodiment of the third sub-element of Figure 12 toward a common exit, showing by arrows the flow path of fluids through the conduits of the third sub-element. Figure 14 is a view in cross-section of the convergence of the conduits in a second, alternate embodiment toward a common exit, showing by arrows the flow path of fluids through the conduits of the third sub-element. Figure 15 is a rear or downstream face view of each of the embodiments of the third sub-element shown in Figures 12-14. Figure 16 depicts an alternate embodiment of an apparatus of the present invention, with the conduits and cavities defined therein for fluid flow being shown in solid outline for clarity of viewing. Figure 17 is a front view of the second sub-element of the apparatus of Figure 16. As suggested in the summary description above of the drawings, an apparatus or element of the present invention in a first embodiment comprises three functionally distinct but not necessarily physically separable sub-elements. The first sub-element performs the functions of dividing a first composite stream into branch streams and redirecting or repositioning the branch streams so created. The second sub-element expands the branch streams, and the third sub-element performs the functions of contracting the branch streams, independently adjusting their flow rates and recombining them into an integrated whole. While these steps may be discretely and sequentially performed, it will be understood that steps may be combined or overlap if desired. Thus, the independent adjustment of the flow rates of the individual branch streams through an apparatus may be accomplished by individually, controllably contracting the branch streams to selected degrees. Similarly, the expanding and contracting steps may coincide or overlap. The performance of the dividing, repositioning, expanding, contracting, adjusting and recombining steps by these three sub-elements will typically and preferably be as shown schematically in Figure 1. As may be seen by reference to that drawing, a layered first composite stream of two discrete and continuous layers 10 and 12 of diverse thermoplastic materials, such as might proceed from a conventional coextrusion feedblock, enters the ISG and is divided into four branch streams 14, 16, 18 and 20 within the first sub-element. Generally the materials in one or both of the layers 10 and 12 will be such that they will be desirably distributed in a gradient or other distribution throughout a second composite stream. It is to be understood also that "a conventional coextrusion feedblock" as used in the preceding paragraph embraces a multilayer feedblock of the type disclosed in US-A-3,773,882 to Schrenk. The first composite stream can thus comprise a number of layers and materials substantially exceeding the two layers shown in Figure 1. By the same token, it is to be understood that the first composite stream can manifest the desired gradient or distribution in layer thicknesses, or can possess a different distribution or be comprised of layers of equal thickness as illustrated in Figure 1. The illustrated first composite stream has been selected, however, in the interest of simplifying as much as possible the explanation and description of the present invention. The layered first composite stream in Figure 1 defines a planar layer interface 22 between the layers 10 and 12 which lies generally in the x-z plane of an x-y-z coordinate system, wherein the z-direction is taken as corresponding to the direction of fluid flow generally through the apparatus (shown by the arrows 24 in Figure 1), the x-direction defines a transverse dimension of the interface 22 and layers 10 and 12, and the y-direction is in the thickness direction of the layers 10 and 12 and extends generally perpendicularly away from the planar layer interface 22. The division of the first composite stream is generally along the x-axis, so that the planar layer interface 22 is divided up generally among two or more of the branch streams 14, 16, 18, and 20, depending on the extent of the layers 10 and 12 and thus of the layer interface 22 in the x-direction. Where the layers 10 and 12 and the layer interface 22 therebetween span the first composite stream in the x- direction as shown in Figure 1, for example, the interface 22 is divided among each of the branch streams 14, 16, 18 and 20. At least two of those branch streams into which the interface 22 was divided, and preferably all of the branch streams 14, 16, 18 and 20, are then redirected and repositioned with respect to both the x- and y-axes and with respect to one another in flowing through the conduits of the first sub-element, so that at the exit of the first sub-element the streams 14, 16, 18 and 20 are preferably stacked along the y-axis. Or, expressed differently, the branch streams 14, 16, 18, and 20 are, in flowing through the first sub-element, divergently displaced along the "y" axis from their original positions while being convergently displaced along the "x" axis. In the second sub-element, at least two branch streams, and preferably all of the stacked branch streams 14, 16, 18 and 20, independently undergo a symmetrical expansion along the x-axis (in the plane of the layer interface 22 of interest) in their transverse (or x) dimension, preferably until the transverse width of a branch stream is substantially as great as the width of the first composite stream entering the apparatus. This expansion is initiated from a central location in the apparatus along the y- axis, and occurs uniformly with respect to each of the layers 10 and 12 in a given branch stream as shown. Preferably the branch streams 14, 16, 18 and 20 also expand uniformly with respect to one another as shown. At the exit of the second sub-element, the at least two branch streams, and preferably all of the branch streams 14, 16, 18 and 20, enter into the third sub-element wherein they each independently undergo a similar progressive, symmetrical contraction or reduction of their thickness along the y-axis or in the y-direction and are recombined to form a layered second composite stream. The extent to which each branch stream is contracted is preferably controlled so as to restrict the flow of a particular branch stream or streams as these streams are recombined with the other branch streams. Layers 10 and 12 in those branch streams which are contracted to the greatest extent or whose flow is most greatly restricted become proportionately thinner than in other branch streams which are restricted to a lesser extent. In this way, by individually restricting the flow rates of the branch streams, a layer thickness gradient or distribution of layer thicknesses generally can be established for layers 10 and 12 of materials within a second composite stream formed of the recombined branch streams. Each of the branch streams 14, 16, 18 and 20 have been equally contracted in Figure 1, for example, so that successive layers 10 and 12 through the thickness of the second composite stream are equally thick to one another. The contraction of each branch stream occurs evenly along the x-axis (that is, in the plane of the layer interface 22 of greatest interest) with respect to the layers 10 and 12 in a given branch stream as shown. An apparatus for performing the steps schematically illustrated in Figure 1 and described above may be understood by reference to Figures 2-15, wherein a first embodiment of the ISG apparatus as a whole is given by the number 26. In Figure 2, the ISG 26 comprises first, second, and third sub-elements 28, 30, and 32. A first composite stream comprised of discrete overlapping layers of diverse polymeric or thermoplastic materials, of which at least one pair defines a generally planar layer interface therebetween lying generally in an x-z plane, enters the ISG 26 through regularly-shaped inlet openings 34 in the first sub-element 28 and flows through the elements 28, 30 and 32 as indicated by the arrows 36. Referring now to Figures 3 through 6, it can be seen that these inlet openings 34 have preferably substantially identical rectangular or square cross-sections and are aligned generally along the x-axis in the previously-defined x-y-z coordinate system. The four inlet openings 34 are defined by three dividing wall portions 38 (Figure 2) which can serve as dividing means for dividing the first composite stream of Figure 1 into the four separate branch streams 14, 16, 18, and 20. The branch streams 14, 16, 18, and 20 in the first sub-element 28 proceed from the inlet openings 34 through first conduits 40 (Figures 3-6). These first conduits 40 act as means for redirecting or repositioning each of the streams 14, 16, 18, and 20 with respect to both of the x- and y- axes, the general direction and degree of displacement associated with each conduit 40 being indicated by the arrows 42 in Figures 3-6. Preferably these conduits 40 are substantially of the same length. The streams 16 and 18 entering through the inner two inlet openings 34 are displaced to the greatest extent along the y-axis and the least along the x-axis (see Figures 4 and 5). Similarly, the branch streams 14 and 18 are displaced least along the y-axis, and most along the x-axis (see Figures 3 and 6) so that at the exit of the first sub-element 28, the outlet ports 44 associated with the conduits 40 are in a preferred embodiment stacked generally along the y-axis (Figures 2, 7). Preferably, the repositioning described above is effected without substantially changing or distorting the cross-sections of the various branch streams, such as by rotating the laminae within a given branch stream with respect to the laminae of another branch stream. The conduits 40 and outlet ports 44 are preferably also substantially identical in true cross-section to one another and to the square or rectangular inlet openings 34. As may be seen in Figure 2, and now more particularly in Figure 8, the outlet ports 44 from the first sub-element 28 communicate with second inlet openings 46 of the second sub-element 30, which second inlet openings 46 are also preferably substantially identically square or rectangular in cross-section to the outlet ports 44 and to one another. After passing through the outlet ports 44 and second inlet openings 46, the streams 14, 16, 18, and 20 are preferably progressively and symmetrically expanded in their transverse (x) dimension by passage through respective second conduits 48 (see Figures 2, 8, 9 and 11). The second conduits 48 are preferably substantially identically configured to one another in cross-section so as to accomplish a uniform expansion of the branch streams 14, 16, 18 and 20. This common configuration in its preferred form gives the impression of a flattened funnel having a rectangular end portion (Figures 8-11), so that the branch streams in passing through the second conduits 48 each possess a gradually progressively greater transverse dimension along the x-axis. Referring now to Figure 12, the streams 14, 16, 18, and 20 are then communicated to the third inlet openings 50 of the third sub-element 32 via the outlet ports 52 of the second sub-element 30 (see Figure 2 also), the third inlet openings 50 thus communicating with the downstream ends of the conduits 48 and being preferably substantially identically square or rectangular in true cross-section therewith. The branch streams 14, 16, 18, and 20 are then conveyed through third conduits 54 (Figures 13 and 14) which symmetrically and individually controllably contract the dimensions of the various branch streams in the y- or thickness direction, and recombine the streams in overlapping relationship so that the second composite stream leaving the device 26 possesses more of the layers 10 and 12 than the first composite stream entering the device 26. The individual control over the thicknesses of the branch streams 14, 16, 18 and 20 enables the thicknesses of the collective layers 10 and 12 within a branch stream to be controlled, as explained above. Where a gradient in the layer thicknesses of repeated layers 10 and 12 is desired in a second composite stream from one major surface to an opposing surface, for example, the branch stream 18 of Figure 1 is contracted the most, branch stream 14 is contracted secondmost, and the branch stream 20 is contracted to a greater extent than branch stream 16 but to a lesser extent than the branch stream 14. The corresponding layers 10 and 12 will be thinnest in branch stream 18, will be thicker in branch streams 14 and 20, and will be thickest in branch stream 16 on recombination of the streams. The third conduits 54 are preferably of a basically constant transverse or "x" dimension (Figures 12 and 15) and convey or direct the streams passing therethrough toward a common exit 56. This common exit 56, where the apparatus 26 is but one of several such devices in series, will preferably be of substantially the same overall dimensions in the x- and y-directions as the combined inlet openings 34. The independent, controllable contraction of the branch streams in a third sub-element can preferably be accomplished by one of the two devices illustrated in cross-section in Figures 13 and 14. In the embodiment of the third sub-element shown in Figure 13, the means employed for independently controllably contracting the thickness of the branch streams flowing therethrough comprises replaceable vanes 58 which define sides of the third conduits 54 at a downstream end thereof, just prior to recombination of the branch streams. Where a different layer thickness profile is desired of the layers of a particular material or materials in the second composite stream leaving the ISG 26, the vanes 58 are simply replaced with vanes 58 providing a contraction and restriction of flow in the branch streams which will produce this profile. This replacement is conveniently accomplished by sectioning the apparatus along line 3-3 as shown in Figure 2, so that this portion of the apparatus may be removed and replaced as a unit. In an alternate embodiment shown in Figure 14, vanes 60 are rotatable about pivot pins 62. Rotation of the vanes 60 could be accomplished manually or by automated means. One advantage of the embodiment of Figure 14 over that shown in Figure 13 is that the process of coextruding the first composite stream and forming a second composite stream does not have to be stopped as with the former embodiment to change vanes 58, and for this reason it is expected that the embodiment of Figure 14 is to be generally preferred over the embodiment of Figure 13. It is to be understood that still other means of controllably restricting the flow of the various branch streams could be employed in the present invention, for example, by the interposition and use of valves, dams, spacers or restrictor bars in any of the conduits corresponding to a selected branch stream, provided of course that these devices do not cause a destructive intermixing of the layers within the branch stream. An alternate embodiment of an apparatus for producing multilayered streams from a first composite stream is shown in Figures 16 and 17 and designated by the numeral 63. The embodiment 63 is comprised in part of a first sub-element 64 which divides a first composite stream into branch streams, repositions the branch streams as they flow through conduits 40, and independently adjusts the flow rates of the various branch streams as they are recombined and enter a second sub-element 66. The second sub-element 66 thereafter symmetrically expands and contracts the recombined branch streams or second composite stream, in proceeding from an inlet opening 68 aligned with the y-axis to an outlet opening 70 aligned with the x-axis. Second sub-element 66 shown in Figures 16 and 17 defines a tetrahedral cavity through which the second composite stream flows and is symmetrically expanded and contracted, the tetrahedral cavity being formed for this purpose by the intersection of sides 72 in the form of four truncated isosceles (or equilateral, depending on the dimensions of the inlet opening 68 and outlet opening 70 in the y- and x-directions, respectively) triangles. The layer thickness gradient or layer thickness distribution established in the apparatus 26 by the independent, controllable contraction of the branch streams and thus by the independent restriction of the flow rates of the branch streams in the third sub-element, can be established also in the apparatus 63 by the same means. Thus, instead of using replaceable vanes 58 (Figure 13) or rotatable vanes 60 (Figure 14) in a third sub-element 32, vanes 58 or preferably vanes 60 are employed at the conclusion of the first sub-element 64 of the apparatus 63 just prior to the branch streams' entry into the cavity defined by the sides 72. The second composite stream emerging from an apparatus 26 or 63 may itself become the feed stream (that is, the first composite stream) to a second ISG of the present invention and so on; and while the focus of the present disclosure has been on the making of multilayer films wherein a layer gradient is desirable, the second composite stream from an apparatus 26 or 63 may be formed into such a film or may instead be formed into multilayer sheet or a multilayer, molded article such as by a thermoforming process. A feature of common significance in the embodiments of Figures 2-15 and of Figures 16 and 17 is the symmetrical expansion and contraction of the divided and stacked branch streams in the apparatus 26, or of the second composite stream comprised of the recombined branch streams in the apparatus 63. A symmetrical expansion in the x- or transverse dimension of the branch streams or of the second composite stream from along the y-axis, rather than unevenly from a peripheral portion of the given apparatus, prevents the bulk of the materials in a given branch stream or in the second composite stream from being funneled or channeled along the near wall of the apparatus relative to such peripheral portion. Distortions in individual layer thicknesses (in the plane of the layers or along the x-axis) because of this channeling effect (due to the flow path being shorter along the nearer wall as opposed to the far wall) are in this manner discouraged from occurring. In the same manner, the symmetrical (along the x-axis) reduction of the thickness of the layers in a given branch stream or in the second composite stream is designed to avoid causing distortions in the thickness of such layers along the x-axis or in the transverse direction, as well as to avoid creating flows in the y-direction which might tend to disrupt the thinly-layered character of a branch stream or the second composite stream. One of the difficulties in achieving a prescribed layer thickness gradient or other distribution of layer thicknesses with known feedblock-ISG combinations, as mentioned earlier, is the tendency of existing ISG's to distort the layers of an incoming first composite stream. This difficulty is addressed in part as described in the preceding paragraphs, by expanding and contracting the branch streams from a first composite stream or the second composite stream in a symmetrical fashion. Preferably the distorting tendencies of previous ISG's are avoided also by manipulating the first composite stream, the branch streams, and/or the second composite stream gradually. Obviously, limitations of space or concerns about thermal degradation of materials in a stream may limit the length over which these manipulations may be carried out to achieve a second stream having a desired number of layers of the one or more materials. In such cases, modifications to the illustrated apparatus may be appropriate, for example, dividing the first composite stream into more than four branch streams, shortening one or more of the sub-elements, and/or changing the feedblock to initially produce a first composite stream having more layers of the materials of interest. The person of ordinary skill in the art is, however, well-equipped to select between and to make these modifications for particular applications of the invention. While preferred embodiments of the method and apparatus of the present invention have been described, it will be appreciated that numerous changes in these embodiments can be made.

Claims: A method for making multilayer films having a prescribed distribution of layer thicknesses from one major surface of the film to an opposing surface, comprising the steps of: dividing a first composite stream comprised of discrete layers of one or more materials, of which at least a pair of said layers define a planar layer interface therebetween which lies in an x-z plane of a Cartesian coordinate system, wherein the z-axis is taken as extending in the direction of flow of the first composite stream, the x-axis extends transversely of the first composite stream and defines a transverse dimension of the layer interface, and the y-axis extends perpendicularly away from said layer interface in the thickness direction of said pair of layers, along the x-axis such that said pair of layers and said layer interface are distributed among at least branch streams; and, in any practical order, repositioning said at least two branch streams along both of the x- and y-axes as the branch streams flow along the z-axis; symmetrically expanding along the x-axis a transverse dimension and symmetrically contracting along the y-axis the thickness of the individual or combined said at least two branch streams; independently controlling the flow rates of said at least two branch streams; and recombining the branch streams to form a second composite stream having a greater number of discrete layers than the first composite stream and distributed in the prescribed distribution. A method as defined in Claim 1, wherein said distribution is a gradient. A method as defined in Claim 1 or Claim 2, wherein the branch streams are repositioned and then expanded and contracted before recombining. A method as defined in Claim 1 or Claim 2, wherein the branch streams are repositioned and than recombined before being expanded and contracted. A method as defined in any one of the preceding claims, wherein said repositioning aligns the branch streams along the y-axis. A method as defined in any one of the preceding claims, wherein all of the branch streams are subjected to said repositioning, expansion and contraction. A method as defined in any one of the preceding claims, wherein the flow rates of said at least two branch streams are independently adjusted by independently controllably contracting their thicknesses along the y-axis. A method as defined in any one of the preceding claims, wherein the first composite stream is divided into branch streams of substantially identical rectangular or square cross-section. A method as defined in any one of the preceding claims, wherein the step of repositioning the branch streams is accomplished without significantly altering their cross-sections. A method as defined in any one of the preceding claims, wherein the first composite stream is divided into an even number of branch streams. A method as defined in any one of the preceding claims, wherein at least some of the discrete layers in the first composite stream are of a generally planar, substantially continuous nature and span the first composite stream along the x-axis. A method as defined in any one of the preceding claims, wherein the first composite stream is originally possessed of layers in a gradient or other layer thickness distribution. A method of making a multilayered plastic article, comprising molding into a desired configuration a product stream of a method as defined in any one of the preceding claims. An apparatus for making multilayer films by a method as defined in Claim 3, said apparatus comprising: dividing means (34) for dividing the first composite stream into the branch streams along the x-axis; first conduits (40) for repositioning the branch streams along both the x-axis and the y-axis; second conduits (48) in fluid communication with the first conduits (40), with each second conduit (48) having a progressively greater transverse dimension along the x-axis from an inlet opening (46) to an outlet port (52) thereof, the inlet opening (46) being positioned centrally in the apparatus; third conduits (54) in fluid communication with the second conduits (48), with each third conduit (54) having a dimension in the y-direction which becomes progressively lesser from an inlet opening (50) to an outlet port thereof; means (58,60) for individually controlling the dimension in the y-direction of each of the third conduits (54) at a downstream end thereof; and means (56) for recombining the branch streams from the third conduits (54) to form the second composite stream. An apparatus as defined in Claim 14, wherein the means for individually adjusting the dimension in the y-direction of each of the third conduits (54) at a downstream end thereof comprises a plurality of replaceable or rotatable vanes (58,60), with each vane forming a portion of a respective third conduit (54) adjacent the downstream end of the conduit (54). An apparatus for making multilayer films by a method as defined in Claim 4, said apparatus comprising: dividing means (34) for dividing the first composite stream into the branch streams along the x-axis; first conduits (40) for repositioning the branch streams along both the x-axis and the y-axis; means (58,60) for individually controlling the dimension in the y-direction of each of the first conduits at a downstream end thereof; and a conduit wherein the branch streams are recombined and symmetrically expanded and contracted, said conduit defining a tetrahedral cavity through which the recombined branch streams flow, the cavity being formed by the intersection of the sides (72) of the conduit in the form of four isosceles or equilateral triangles. An apparatus as defined in Claim 16, wherein the means for individually adjusting the dimension in the y-direction of each of the first conduits (40) at a downstream end thereof comprises a plurality of replaceable or rotatable vanes (58,60), with each vane forming a portion of a respective first conduit (40) adjacent the downstream end of the conduit (40).

Inventors: AYRES RALPH E, GOSEN DANIEL J, SCHRENK WALTER J, SHASTRI RANGANATH K, AYRES, RALPH E., GOSEN, DANIEL J., SCHRENK, WALTER J., SHASTRI, RANGANATH K.
Applicants: DOW CHEMICAL CO, THE DOW CHEMICAL COMPANY
Application year: 1991
Main classification: B29C47
IPC codes: B29C47, B01F5, B29L7, B29L9