Extrusion of channel profiles are well known in the art. Typically, single or two-piece dies are constructed to generate the channel profile (see, e.g., U.S. Pat. No. 3,274,315 (Kawamura). A typical extrusion die may have an outer manifold and an inner manifold. The inner manifold includes a port for allowing air to enter within the channel as the extrusion is formed, which prevents the collapse of the channel structure. Machining of these dies is limited to the precision at which die parts can be formed.
The extrusion of smaller channels to form film-like webs typically requires higher precision extrusion dies. This is because the flow rate of material is very dependent upon the resistance within the die. Small changes in the cavity size have significant effects on the resultant extruded part. Thus, uniformity of flow passageway resistance within the die is important for the formation of uniform channel webs.
Coextrusion of polymers is well known in the art. Polymer melt streams from two or more extruders are combined together to form articles with unique properties. Successful coextrusion is dependent upon polymer weld lines to hold together based on the needs of the article. The compatibility of coextruded polymers and the methods of welding the streams together are important considerations for the article construction.
Channel webs are useful for many applications such as spacer webs and cushioning materials. There is a need to create thin channel webs which are uniform in mechanical properties.
In one aspect, the present disclosure describes a first article comprising first and second layers each having first and second opposed major surfaces and between the first and second layers a series of first walls providing a series of microchannels, wherein there are at least 3 (in some embodiments, at least 5, 10, 15, 20, 25, 30, 35, or even up to 40) first walls per cm, wherein each wall has a height extending from the first layer to the second layer, and wherein the aspect ratio of the walls, the aspect ratio determined by dividing wall height by average wall width, is between 1.5 and 5, and wherein the first and second layers and first walls are coextruded.
Embodiment of coextruded articles described herein may be useful, for example, in cushioning applications where high levels of compression are desired. Conventional foamed sheets are typically limited in the amount of void space that can be generated, whereas embodiments of coextruded articles described herein can have relatively high void content (i.e., greater than 50%).
Embodiments of coextruded articles described herein may be useful, for example, in applications using liquid or gas materials for heat transfer. For example, a coextruded article described herein can be placed in contact with components requiring temperature control, wherein the channels contain heat transfer media.
Embodiments of coextruded articles described herein may also be used as spacer webs. For example, coextruded articles described herein can provide significant spacing with a minimal amount of material usage. For example, coextruded articles which require beam strength with minimal weight can be created with rigid films separated by a coextruded article described herein.
Referring to
Referring to
In some embodiments of coextruded articles described herein, there are lines of demarcation at the region where the wall joins each layer. A demarcation line or boundary region can be detected as described in the Examples using Differential Scanning Calorimetry (DSC).
In general, the first and second layers and the wall are joined together to form a continuous coextruded article after the polymer melts exit the die, with microchannels formed between the outside surfaces. The article is extruded, similar to the way that plastic films are extruded. Thus, while the cross direction is composed of a combination of features the machine direction is uniform in structure and can continue for great length. The coextruded article in end use can be cut to short length dependent upon desired application.
These first and second layer orifices are generally parallel to each other. Positioned between these first and second orifices is a plurality of orifices to create the wall section of the channel web. This plurality of orifices is fed typically from a third cavity within the extrusion die. These orifices typically have an aspect ratio greater than 1:1 oriented perpendicular to the layer orifices. The top and bottom of these orifices is positioned close to the first and second layer such that the polymer melt from the plurality of walls will weld to the first and second layer, almost immediately as it exits the die. The slight gap before bonding enables air to access the newly formed channel between the layers to prevent the collapse of the channel as the channel web is formed and pulled from the die. The close proximity of the wall to the layer enables welding with minimal rounding of features as is typical with profile polymer extrusion. Nevertheless, with some rounding of features it will be noted that the walls created in this microchannel coextruded article are narrower in cross sectional thickness near the weld portion, than at say the center of the wall. The difference in the wall thickness at the wall center versus the wall intersection by the distance between the wall orifice and the layer orifices can be controlled, for example, by the distance between orifices used to create the wall and the top and bottom layer. Die designs with very close orifice distances allows the molten polymer to weld together before polymer flow converts the wall shape into a round like strand. Typically, polymer die swell will initiate contact between the flow streams to create a weld line. Very close distances between these orifices enables this coextruded article to be made with wall shapes which are long with narrow cross sections. Typically, the distance between the wall orifice and the layer orifice is less than 1 mm to minimize the wall thickness difference.
The cavities, passageways, and orifices formed to create the layers and walls are formed from shims that are positioned next to each other. Some shims have slots cut to form the passageways. Other shims do not, which create the sidewalls of the passageways. The width of the passageways, and the walls created from adjacent shims are thus formed from the thickness dimension of the shimstock. Shimstock with uniform thickness is used to form these dies. Shimstock thickness can be obtained with thickness variation less than +/−5 micrometers. This precision in thickness enables precision in wall thickness, due to uniform passageway and orifice dimensions.
In some embodiments, the second average widths are less than the third average widths.
In some embodiments of the first and second coextruded articles described herein, no width of a wall exceeds more than 20 (in some embodiments, not more than 25, 30, 40, or even not more than 50) percent of the average width for that wall, wherein there is an average width of the walls, and wherein no average width of a respective wall exceeds more than 5 (in some embodiments, not more than 10, 15, or even not more than 20) percent of the average width of the walls.
In some embodiments, there is an average minimum width for the first walls, and wherein the minimum width of an individual first wall is within ±10 (in some embodiments, ±20, ±30, ±40, or even ±50) percent of the average minimum width for the first walls.
In some embodiments, the microchannels have a width not greater than 2000 (in some embodiment, not greater than 1500, 1000, 500, 200, or even not greater than 100; in some embodiments, in a range from 100 to 2000, 100 to 1000, 100 to 500, 200 to 500, 300 to 400, 200 to 500, or even 100 to 500) micrometers.
In some embodiments, the walls have a height (i.e., between the first and second layers) not greater than 3000 (in some embodiments, not greater than 200, 1000, 500, 250, or up to 100) in some embodiments, in a range from 50 to 3000, 50 to 2000, 100 to 2000, 100 to 1500, 200 to 1500, 200 to 1000, or even 300 to 500) micrometers.
In some embodiments, there are at least plurality of first walls having a width not greater than 400 (in some embodiment, not greater than 300, 200, or even not greater than 100; in some embodiments, in a range from 50 to 400, 50 to 300, 50 to 200, or even 50 to 100) micrometers.
In some embodiments, there are at least 3 walls per centimeter width of the first or second layer. In other embodiments, there may be at least 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20 or more walls per centimeter.
In some embodiments, coextruded articles described herein or parts thereof, can be foamed at different porosity levels using, for example, chemical foaming agents (CFA) (also sometimes referred to as chemical blowing agents (CBA)). The mechanical properties (e.g., compression behavior) of coextruded articles described can be tuned by selectively making some of the segments porous. Other approaches to affecting the mechanical properties of the coextruded articles the quantity of CFA used and CFA activation temperature(s).
In some embodiments, CFAs are exothermic, in others endothermic. Exemplary exothermic CFAs include an azo-dicarbonamide and sulfonyl-hydrazide. Exemplary endothermic CFAs include sodium bicarbonate and citric acid, and available, for example, under the trade designation “HYDROCEROL BIH-40-E” from Clariant Corporation, Muttenz, Switzerland.
In some embodiments, at least one of the first or second layers are essentially free of closed-cell porosity (i.e., less than 5; in some embodiments, less than 4, 3, 2, or even less than 1) percent by volume closed-cell porosity based on the total volume of the respective layer) (in some embodiments, both the first or second layers are essentially free of closed-cell porosity).
In some embodiments, at least a portion (in some embodiments, at least 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 96, 97, 98, 99, or even 100 percent by number) of the first walls are essentially free of closed-cell porosity (i.e., less than 5; in some embodiments, less than 4, 3, 2, or even less than 1) percent by volume closed-cell porosity, based on the total volume of the respective wall).
In some embodiments, at least one of the first or second layers have a closed-cell porosity of at least 5 (in some embodiment, at least 10, 15, 20, 25, 30, 35, 40, 45, or even at least 50; in some embodiments, in a range from 5 to 90, 10 to 90, 25 to 90, 50 to 90, 60 to 90, 50 to 80, or even 60 to 80) percent by volume closed-cell porosity, based on the total volume of the respective layer.
In some embodiments, at least a portion (in some embodiments, at least 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 96, 97, 98, 99, or even 100 percent by number) of the first walls have a closed-cell porosity of at least 5 (in some embodiment, at least 10, 15, 20, 25, 30, 35, 40, 45, 50, or even at least 50; in some embodiments, in a range from 5 to 90, 10 to 90, 25 to 90, 50 to 90, 60 to 90, 50 to 80, or even 60 to 80) percent by volume closed-cell porosity, based on the total volume of the respective wall.
In some embodiments, all walls between the first and second layers are the first walls.
In some embodiments of coextruded articles described herein, all walls between the first and second layers are the first walls. In some embodiments, further comprising a plurality of second walls. In some embodiments, the second walls have a minimum width not greater than 400 (in some embodiment, not greater than 300, 200, or even not greater than 100; in some embodiments, in a range from 50 to 400, 50 to 300, 50 to 200, or even 50 to 100) micrometers. In some embodiments, there is an average minimum width for the second walls, and wherein the minimum width of an individual second wall is within ±10 (in some embodiments, ±20, ±30, ±40, or even ±50) for the second walls. In some embodiments, at least a portion (in some embodiments, at least 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 96, 97, 98, 99, or even 100 percent by number) of the second walls are essentially free of closed-cell porosity. In some embodiments, at least a portion (in some embodiments, at least 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 96, 97, 98, 99, or even 100 percent by number) of the second walls have a closed-cell porosity of at least 5 (in some embodiment, at least 10, 15, 20, 25, 30, 35, 40, 45, 50, or even at least 50; in some embodiments, in a range from 5 to 90, 10 to 90, 25 to 90, 50 to 90, 60 to 90, 50 to 80, or even 60 to 80) percent by volume closed-cell porosity, based on the total volume of the respective wall. In some embodiments, all walls between the first and second layers are first and second walls.
A plurality of second wall that alternates with the first walls through the width of the coextruded article can be made by minor variations of the shim dispensing surface. The second walls can be made porous or made with a different material than the first wall, for example, to tune mechanical properties of the coextruded article.
An optional fourth cavity can be used to dispense material to create the second walls. The second wall can be dispensed close to the first wall to create a cojoined wall that is formed when two melt streams for the walls fuse together by die swell phenomena right after exiting the die. In some embodiments of a cojoined wall, one walls can contain functional particles, while the other is free of such particles and provides strengthening to the wall. In some embodiment, the functional particles (e.g., aluminum oxide, aluminum nitride, aluminum trihydrate, boron nitride, copper, graphite, graphene, magnesium oxide, zinc oxide) provide desired electrical or thermal properties to articles described herein.
In some embodiments, the microchannels have a length of at least 15 cm (in some embodiment, at least 20 cm, 25 cm, 30 cm, 50 cm, 1 m, 5 m, 10 m, 25 m, 50 m, or even at least 100 m).
In some embodiments of the first and second coextruded articles described herein, the first layer comprises a first thermoplastic material. In some embodiments, the first thermoplastic material is at least one of polyolefins, ethylene vinyl acetate polymers, polyurethanes, or styrene block copolymers (e.g., styrene-isoprene-styrene block copolymers).
In some embodiments, the second layer comprises a thermoplastic material. In some embodiments, the second thermoplastic material is at least one of polyolefins, ethylene vinyl acetate polymers, polyurethanes, or styrene block copolymers (e.g., styrene-isoprene-styrene block copolymers), or polyurethanes or any resin with elastomeric properties.
The terms “elastomeric properties” or “elastomer” refers to a resin material that can undergo a substantial elongation and then return to its original dimensions upon release of the stress elongating the elastomer. In some cases an elastomer is able to undergo at least 10% elongation (at a thickness of 0.5 mm), and return to at least 50% recovery after being held at that elongation for 2 seconds and after being allowed 1 minute relaxation time. In some examples, an elastomer can undergo 25% elongation without exceeding its elastic limit. In some examples elastomers can undergo elongation to as much as 300% or more of its original dimensions without tearing or exceeding the elastic limit of the composition.
Elastomers can be defined to reflect this elasticity as in ASTM Designation D833-96 as a macromolecular material that at room temperature returns rapidly to approximately its initial dimensions and shape after substantial deformation by a weak stress and release of the stress. ASTM Designation D883-96 as a macromolecular material that, at room temperature, returns rapidly to approximately its initial dimensions and shape after substantial deformation by a weak stress and release of the stress. ASTM Designation D412-98 A can be an appropriate procedure for testing rubber properties in tension to evaluate elastomeric properties.
In some embodiments, the walls comprise a third thermoplastic material. In some embodiments, the third thermoplastic material is at least one of polyolefins, ethylene vinyl acetate polymers, or styrene block copolymers (e.g., styrene-isoprene-styrene block copolymers), or polyurethanes or any such resin with elastomeric properties.
In some embodiments, the first layer comprises a first material, the second layer comprises a second material, and the walls comprise a third material, and wherein the third material is different from both the first and second materials. “Different” as used herein means at least one of (a) a difference of at least 2% in at least one infrared peak, (b) a difference of at least 2% in at least one nuclear magnetic resonance peak, (c) a difference of at least 2% in the number average molecular weight, or (d) a difference of at least 5% in polydispersity. Examples of differences in polymeric materials that can provide the difference between polymeric materials include composition, microstructure, color, and refractive index. The term “same” in terms of polymeric materials means not different.
In some embodiments, the first layer comprises a non-elastomeric material and the second layer comprises an elastomeric material. In some embodiments, the walls comprise a thermoplastic material comprising an elastomer and at least the first and second layer comprise at least one thermoplastic material which is not an elastomer. In another embodiment, the first and second layers are either the same or different elastomers, and the walls are a non-elastomeric polyolefin. In another embodiment, the first layer is polyurethane, the walls are the same or a different elastomeric polyurethane, and the second layer is a non-elastomeric medium density polyethylene.
In some embodiments, wall aspect ratio (wall height divided by average wall thickness for a given wall) is at least 1.5. In other embodiments the aspect ratio could be at least 1, 1.25, 1.5, 1.75, 2.0, 2.25, 2.5, 2.75 3.0, 3.25, 3.5, 3.75, 4.0, 4.25, 4.5, 4.75, 5.0, 5.25, 5.5, 5.75, or 6.0. In some embodiments, the aspect ratio could be tween 1 to 6, or in narrower ranges between any of the two aspect ratio numbers listed in the preceding sentence. In some embodiments, aspect ratios are between 1.5 and 4.5, or any narrower ranges between 1.5 and 4.5 as delimited in 0.25 increments (e.g., 1.75-2; 3.5-4, etc.).
In some embodiments, the walls are orthogonal to the first and second layer. In other embodiments, the wall interface with the first and second layer is such that the wall is nonorthogonal relative to the first and second layers (that is, the interface between the first layer and the wall and the second layer and the same wall are offset—see, for example,
In some embodiments of the first, second, and third coextruded articles described herein, the first layer comprises a first material, the second layer comprises a second material, and the walls comprise a third material, and wherein at least two of the first material, the second material, or the third material are the same.
In some embodiments, the first layer comprises a first material, the second layer comprises a second material, and the walls comprise a third material, and wherein the first material, the second material, and the third material are the same.
In some embodiments, the first major surface of the first layer has functional particles thereon.
In some embodiments, the first layer has a thickness of at least 25 (in some embodiments, at least 50, 75, 100, 125, 150, 175, or even at least 200; in some embodiments, in a range from 25 to 300, 50 to 300, 75 to 300, 100 to 300, 150 to 300, 150 to 250, or even 200 to 250) micrometers.
In some embodiments of the first and second coextruded articles described herein, the second layer has a thickness of at least 25 (in some embodiments, at least 50, 75, 100, 125, 150, 175, or even at least 200; in some embodiments, in a range from 35 to 300, 50 to 300, 75 to 300, 100 to 300, 150 to 300, 150 to 250, or even 200 to 250) micrometers.
In some embodiments having has a thickness of at least 100 (in some embodiments, at least 200, 300, 400, 500, 600, or even at least 700; in some embodiments, in a range from 100 to 2500, 200 to 2500, 300 to 2500, 300 to 2000, 400 to 1500, or even 500 to 1000) micrometers.
In some embodiments of the third coextruded article described herein, for each wall there is a first average width along the first 2 percent of the height of the wall, wherein for each wall there is a second average width along the last 2 percent of the height of the wall, wherein for each wall there is a third average width along the remaining 96 percent of the height of the wall, and wherein for at least 50 (in some embodiments, at least 60, 70, 75, 80, 90, 95, or even 100) percent by number of the walls, the first average widths are less than the third average widths.
Coextruded polymeric articles described herein (including those shown in
Exemplary coextruded articles described herein can be made, for by extrusion from a die. An exemplary has a variety of passageways from cavities within the die to a dispensing slot, including exemplary dies described herein (see, e.g.,
In some embodiments, the shims will be assembled according to a plan that provides a sequence of shims of diverse types. Since different applications may have different requirements, the sequences can have diverse numbers of shims. The sequence may be a repeating sequence that is not limited to a particular number of repeats in a particular zone. Or the sequence may not regularly repeat, but different sequences of shims may be used. The shape of the passageways within, for example, a sequence of shims, may be identical or different. Examples of passageway cross-sectional shapes include round, square, and rectangular shapes. In some embodiments, the shims that provide a passageway between one cavity and the dispensing slot might have a flow restriction compared to the shims that provide a passageway between another cavity and the dispensing slot. The width of the distal opening within, for example, a different sequence of shims, may be identical or different. For example, the portion of the distal opening provided by the shims that provide a passageway between one cavity and the dispensing slot could be narrower than the portion of the distal opening provided by the shims that provide a passageway between another cavity and the dispensing slot.
Individual cavities and passageways provide a conduit for polymer to orifices to create the first and second layers and the walls. These individual flowstreams merge together to form a continuous, solid polymeric coextruded article, at the die slot portion of the die. Spacing between the walls and layer slots form demarcation lines connecting the first and second layers and the walls.
In some embodiments, extrusion dies described herein include a pair of end blocks for supporting the plurality of shims. In these embodiments, it may be convenient for one, or even all, of the shims to each have at least one through-holes for the passage of connectors between the pair of end blocks. Bolts disposed within such through-holes are one convenient approach for assembling the shims to the end blocks, although the ordinary artisan may perceive other alternatives for assembling the extrusion die. In some embodiments, the at least one end block has an inlet port for introduction of fluid material into one, or both, of the cavities.
In some embodiments, the shims will be assembled according to a plan that provides a repeating sequence of shims of diverse types. The repeating sequence can have diverse numbers of shims per repeat. For a first example, a repeating sequence utilizing four shim types is described below to create the orifice pattern shown in
In some embodiments, the assembled shims (conveniently bolted between the end blocks) further comprise a manifold body for supporting the shims. The manifold body has at least one (e.g., in some embodiments two three, four, or more) manifold therein, the manifold having an outlet. An expansion seal (e.g., made of copper or alloys thereof) is disposed to seal the manifold body and the shims, such that the expansion seal defines a portion of at least one of the cavities (in some embodiments, a portion of both the first and second cavities), and such that the expansion seal allows a conduit between the manifold and the cavity.
Typically, the passageway between cavity and dispensing orifice is up to 5 mm in length. Sometimes the fluid passageways leading to one array has greater fluid restriction than the fluid passageways leading to one or more of the other arrays.
The shims for dies described herein typically have thicknesses in the range from 50 micrometers to 125 micrometers, although thicknesses outside of this range may also be useful. Typically, the fluid passageways have thicknesses in a range from 50 micrometers to 750 micrometers, and lengths less than 5 mm (with generally a preference for smaller lengths for decreasingly smaller passageway thicknesses), although thicknesses and lengths outside of these ranges may also be useful. For large diameter fluid passageways, several smaller thickness shims may be stacked together, or single shims of the desired passageway width may be used.
The shims are tightly compressed to prevent gaps between the shims and polymer leakage. For example, 12 mm (0.5 inch) diameter bolts are typically used and tightened, at the extrusion temperature, to their recommended torque rating. Also, the shims are aligned to provide uniform extrusion. To aid in alignment, an alignment key can be cut into the shims. Also, a vibrating table can be useful to provide a smooth surface alignment of the extrusion tip.
In practicing methods described herein, the polymeric materials might be solidified simply by cooling. This can be conveniently accomplished passively by ambient air, or actively by, for example, quenching the extruded first and second polymeric materials on a chilled surface (e.g., a chilled roll). In some embodiments, the first and/or second and/or third polymeric materials are low molecular weight polymers that need to be cross-linked to be solidified, which can be done, for example, by electromagnetic or particle radiation. In some embodiments, it is desirable to maximize the time to quenching to increase the bond strength.
Referring now to
Shim 500 has several holes 547 to allow the passage of, for example, bolts, to hold shim 500 and others to be described below into an assembly. Shim 500 also has dispensing surface 567, and in this particular embodiment, dispensing surface 567 has indexing groove 580 which can receive an appropriately shaped key to ease assembling diverse shims into a die. This embodiment has shoulders 590 and 592 which can assist in mounting the assembled die with a mount of the type shown in
Referring to
Shim 600 has several holes 647 to allow the passage of, for example, bolts, to hold shim 600 and others to be described below into an assembly. Shim 600 also has dispensing surface 667, and in this particular embodiment, dispensing surface 667 has indexing groove 680 which can receive an appropriately shaped key to ease assembling diverse shims into a die. The shim may also have identification notch 682 to help verify that the die has been assembled in the desired manner. This embodiment has shoulders 690 and 692 which can assist in mounting the assembled die with a mount of the type shown in
Referring to
Shim 700 has several holes 747 to allow the passage of, for example, bolts, to hold shim 700 and others to be described below into an assembly. Shim 700 also has dispensing surface 767, and in this particular embodiment, dispensing surface 767 has indexing groove 780 which can receive an appropriately shaped key to ease assembling diverse shims into a die. This embodiment has shoulders 790 and 792 which can assist in mounting the assembled die with a mount of the type shown in
Referring to
Referring to
Referring to
In this embodiment, inlet fittings provide a flow path for three streams of molten polymer through end blocks 2244a and 2244b to cavities 562a, 562b, and 562c, and 562d. Compression blocks 2204 have notch 2206 that conveniently engages the shoulders on shims (e.g., 590 and 592) on 500. When mount 2000 is completely assembled, compression blocks 2204 are attached by, for example, machine bolts to backplates 2208. Holes are conveniently provided in the assembly for the insertion of cartridge heaters 52.
Referring to
Referring to
Herein, a pressure sensitive adhesive (PSA) is used in its conventional manner according to the Pressure-Sensitive Tape Council, which states that PSAs are known to possess properties including the following: (1) aggressive and permanent tack, (2) adherence with no more than finger pressure, (3) sufficient ability to hold onto an adherend, and (4) sufficient cohesive strength to be removed cleanly from the adherend. Materials that have been found to function well as PSAs include polymers designed and formulated to exhibit the requisite viscoelastic properties resulting in a desired balance of tack, peel adhesion, and shear holding power. PSAs are characterized by being normally tacky at room temperature (e.g., 20° C.). Central to all PSAs is a desired balance of adhesion and cohesion that is often achieved by optimizing the physical properties of the elastomer, such as glass transition temperature and modulus. For example, if the glass transition temperature (Tg) or modulus of the elastomer is too high and above the Dahlquist criterion for tack (storage modulus of 3×106 dynes/cm2 at room temperature and oscillation frequency of 1 Hz), the material will not be tacky and is not useful by itself as a PSA material.
Methods to make specific coextruded articles described herein may involve use of particular materials (e.g., same, different, or a combination thereof first, second and third materials). Example methods for making coextruded articles described herein include the following.
Coextruded articles described herein can be made for example, by a method comprising:
providing an extrusion die comprising a first cavity, a second cavity, a third cavity, and a first die slot, a second die slot, and a plurality of third die slots, wherein each die slot has a distal opening, wherein there is a fluid passageway between the first cavity and the first die slot, a fluid passageway between the second cavity and a second die slot, and a plurality of fluid passageways between the third cavity and the plurality of third die slots;
providing via extrusion a first material to the first cavity of the extrusion die, a second material to the second cavity of the extrusion die, and a third material to the third cavity of the extrusion die;
extruding the layers from the distal opening of the die slots; and forming together the extrusion melt from first and second die slot with the plurality of extrudate from the third die slots into one continuous coextruded article; and
quenching the extruded layer.
In certain embodiments, one or both opposed major sides of the coextruded article may then be coated with a PSA, either directly or with further intervening layers (for example, tie layers or primer layers, as needed).
Embodiment of articles and coextruded articles described herein are useful, for example, in cushioning applications where high levels of compression are desired. Conventional foamed sheets are typically limited in the amount of void space that can be generated, whereas embodiments of coextruded articles described herein can have relatively high void content (i.e., greater than 50%).
Embodiments of articles and coextruded described herein are useful, for example, in applications using liquid or gas materials for heat transfer. For example, a coextruded article described herein can be placed in contact with components requiring temperature control, wherein the channels contain heat transfer media.
Embodiments of coextruded articles described herein may also be used as spacer webs. For example, coextruded articles described herein can provide significant spacing with a minimal amount of material usage. For example, coextruded articles which require beam strength with minimal weight can be created with rigid films separated by a coextruded article described herein.
Advantages and embodiments of this invention are further illustrated by the following examples, but the particular materials and amounts thereof recited in these examples, as well as other conditions and details, should not be construed to unduly limit this invention. All parts and percentages are by weight unless otherwise indicated.
A co-extrusion die as generally depicted in
The inlet fittings on the two end blocks were each connected to two conventional single-screw extruders. The top and bottom layer cavities of the die were fed with a single extruder loaded with polypropylene homopolymer (obtained under the trade designation “PP1024” from ExxonMobil, Irving, Tex.). The cavity feeding the cavity for the connecting walls was connected to an extruder loaded with polypropylene elastomer (obtained under the trade designation “VISTAMAXX 7810” from ExxonMobil, Irving, Tex.) dry blended with 2% red color concentrate (obtained under the trade designation “PP3TEX17690” from Clariant, Minneapolis, Minn.). Extruder flow rates were adjusted to achieve the channel web cross section shown in
The melt was extruded at a slight angle from vertical into an extrusion quench takeaway. This slight angle enables the bonding of the top and bottom layers to the wall extruded features. The quench roll was a smooth temperature controlled chrome plated 20 cm diameter steel roll. The quench nip temperature was controlled with internal water flow. The web path wrapped 180 degrees around the chrome steel roll and then to a windup roll. Under these conditions a polymeric layer generally as depicted in
Other process conditions are listed below:
An optical microscope was used to measure web dimensions in the crossweb:
Foreseeable modifications and alterations of this disclosure will be apparent to those skilled in the art without departing from the scope and spirit of this invention. This invention should not be restricted to the embodiments that are set forth in this application for illustrative purposes.
Filing Document | Filing Date | Country | Kind |
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PCT/IB2020/062213 | 12/18/2020 | WO |
Number | Date | Country | |
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62951104 | Dec 2019 | US |