EP0587581A1 - Nondistorted polyolefin foam structures and process for making - Google Patents

Nondistorted polyolefin foam structures and process for making

Info

Publication number
EP0587581A1
EP0587581A1 EP92908512A EP92908512A EP0587581A1 EP 0587581 A1 EP0587581 A1 EP 0587581A1 EP 92908512 A EP92908512 A EP 92908512A EP 92908512 A EP92908512 A EP 92908512A EP 0587581 A1 EP0587581 A1 EP 0587581A1
Authority
EP
European Patent Office
Prior art keywords
foam
foam structure
polyolefin composition
geometry
orifices
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP92908512A
Other languages
German (de)
French (fr)
Other versions
EP0587581A4 (en
Inventor
Bruce A. Malone
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dow Chemical Co
Original Assignee
Dow Chemical Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Dow Chemical Co filed Critical Dow Chemical Co
Publication of EP0587581A4 publication Critical patent/EP0587581A4/en
Publication of EP0587581A1 publication Critical patent/EP0587581A1/en
Withdrawn legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34—Auxiliary operations
    • B29C44/36—Feeding the material to be shaped
    • B29C44/46—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length
    • B29C44/468—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length in a plurality of parallel streams which unite during the foaming
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers

Definitions

  • the invention relates to a closed-cell, non- crosslinked polyolefin foam structure of relatively small cell size and relatively low cross-section minor to major dimension ratio.
  • the extruded structure is substantially free of distortion, convolution, or corrugation from its intended shape or geometry.
  • Solid closed-cell polyolefin foam structures of relatively low cross-section minor to major dimension ratio, height to width in the case of those of rectangular cross-section, have found numerous commercial applications such as cushioning, packaging, insulation, sheeting, and the like. To enhance insulative performance, softness, sound absorption, and nonabrasiveness of such structures, it would be desirable to reduce the cell size of the polyolefin foam comprising the structure.
  • a problem with making solid closed-cell, non- crosslinked polyolefin foam structures of relatively small cell sizes (e.g. 0.02 to 0.5 millimeters (mm)) and relatively low cross-section dimension ratios (e.g. 1/8 or less) is that the structure actually formed may be in a geometry or shape other than that intended.
  • the foamable composition from which the structure is made exits the die, it is not able to expand directionally outward with respect to the major dimension of the die orifice at a rate sufficient to prevent the structure from becoming distorted, convoluted, or corrugated along its major dimension.
  • the structure cannot expand rapidly enough because relatively small cell size foams
  • a 5 closed-cell, non-crosslinked foam structure of a ratio of minor dimension to major dimension of about 1/8 or less in cross-section comprised of coalesced strands or profiles of a foamed polyolefin composition having an average cell size of from 0.02 to 0.5 millimeters.
  • the 0 foam structure substantially corresponds in cross- sectional geometry to the geometry of the overall arrangement of the orifices of the die from which it was extruded.
  • the extrusion of the foam structure in the form of coalesced strands or profiles allows structures of such relative cross-sectional dimension ratios (e.g.
  • a process for making a closed-cell, non-crosslinked foam structure of a ratio of minor dimension to major dimension in cross-section of 1/8 or less and comprised of a foamed polyolefin composition having an average cell size of from 0.02 to 0.5 millimeters comprises extruding a foamable polyolefin composition through a die defining a plurality of orifices therein to form a plurality of coalesced extruded strands or profiles of the foamed polyolefin composition forming the above foam structure substantially corresponding to the geometry of the overall arrangement of the orifices of the die.
  • the present foam structure is formed of coalesced closed-cell, non-crosslinked polyolefin foam strands or profiles having an average cell size of from 0.02 to 0.5 millimeters and minor to major dimension ratios of less than 1/8 or less to be made substantially corresponding to the shape or geometry of the overall arrangement of the orifices of the die from which the structure was extruded.
  • the present foam structure circumvents the problems associated with prior art foam structures of that cell size range and relative dimension by its ability to accommodate the high rate of foaming without being distorted, convoluted, or corrugated.
  • the present foam structure is formed by extrusion of a molten foamable, non-crosslinked polyolefin composition through a multiorifice die.
  • the foamable composition is formed by melt plastifying the polyolefin and blending therein a blowing agent and other additives such as a nucleating agent.
  • the streams of molten extrudate exiting the die take the form of strands or profiles, which desirably foam, coalesce, and adhere to one another to form a unitary structure.
  • the coalesced individual strands or profiles 0 of polyolefin foam should remain adhered into unitary structure to prevent strand delamination under stresses encountered in preparing, shaping, and using the foam. Apparatuses and methods for producing foam structures of strand form are seen in U.S. Patents 3,573 * 152 and 5 4,82-4, 720.
  • the strands or profiles will vary in cross- sectional shape or geometry according to the shape or geometry of the orifices in the die.
  • the strands or 0 profiles may be the same or different shape or geometry than the foam structure which they coalesce to form.
  • the orifices may take on a circular shape or a noncircular shape though circular is preferred. Suitable noncircular shapes include X-shaped, cross- or star-shaped, or polygonal-shaped.
  • the various orifices in the die may be specially arranged in a desired configuration or array such as a sine wave, honeycomb, square saw tooth, or a triangular saw tooth wave pattern.
  • the individual strands have a major dimension in cross-section, diameter in the case of circular strands, of between 0.5 and 10 millimeters and most preferably between 1.0 and 5.0 millimeters.
  • the orifices in the die will be of shape or
  • the streams of molten extrudate may foam to either partly or completely fill the open channel volume 0 between the strands or profiles.
  • the geometry or shape of the resulting foam structure will substantially correspond to the overall arrangement or geometry of the die orifices or, in other 5 words, to the intended or desired shape or geometry. For instance, a plurality or multiplicity of circular orifices arranged in a rectangular pattern will yield a rectangular foam structure. A plurality or multiplicity of circular orifices arranged in a circular pattern will 0 yield a cylindrical or circular foam structure.
  • the geometry or shape of the present foam structure will correspond to the overall arrangement or geometry of the orifices in the die from which it is extruded without substantial distortion, convolution, or corrugation therefrom.
  • the foam structure typically will have cross- sectional dimensions larger than the dimensions defined by the overall arrangement or geometry the die orifices of the die from which it was extruded due to foaming of the molten extrudate, but the relative cross-sectional dimensions of the foam structure will substantially correspond to the relative dimensions of the overall
  • the resulting foam structure will have rectangular cross-sectional dimensions exceeding _.,- that of the overall arrangement or geometry of the die orifices, but will have substantially the same relative cross-sectional dimensions.
  • a mixer, extruder, or other suitable blending device is employed to obtain a homogeneous melt.
  • the extruder or other 5 suitable blending device is also employed to incorporate a blowing agent. Nucleating agents, extrusion aids, antioxidants, colorants, pigments, etc. may also be incorporated as desired.
  • Suitable foamable polyolefin compositions include polyethylene or polypropylene. Preferred are copolymers of ethylene and a monoethylenically unsaturated polar monomer copolymerizable therewith, especially carboxyl-containing comonomers.
  • Examples include copolymers of ethylene and acrylic acid or methacrylic acid and C ⁇ _4 alkyl ester or ionomeric derivatives thereof; ethylene vinyl-acetate copolymers; ethylene/carbon monoxide copolymers; anhydride containing olefin copolymers of a diene and a polymerizable; copolymers of ethylene and an ⁇ -olefin having ultra low molecular weight (i.e., densities less than 0.92 grams/cubic centimeter); blends of all of the foregoing resins; blends thereof with polyethylene (high, intermediate or low density); etc.
  • ultra low molecular weight i.e., densities less than 0.92 grams/cubic centimeter
  • compositions are copolymers of ethylene and acrylic acid, (EAA copolymers) having up to about 30 percent by weight of copolymerized acrylic acid; ionomeric derivatives of the foregoing, copolymers of ethylene and vinyl acetate; ultra low density polyethylene; and blends of the foregoing with one another and with low density polyethylene.
  • EAA copolymers having up to about 30 percent by weight of copolymerized acrylic acid
  • ionomeric derivatives of the foregoing, copolymers of ethylene and vinyl acetate ultra low density polyethylene
  • blends of the foregoing with one another and with low density polyethylene are particularly preferred compositions.
  • the polymers of ethylene and a polar comonomer may be prepared by known addition polymerization techniques, or by a grafting reaction of the reactive comonomer with a preformed polymer of ethylene. Additional elastomeric components such as polyiso- butylene, polybutadiene, ethylene/propylene copolymers, and ethylene/propylene diene interpolymers may be included in the blend if desired.
  • a most preferred resin composition comprises a copolymer of ethylene and acrylic acid or ethylene and vinyl acetate containing from 85 percent to 98 percent ethylene by weight.
  • a most preferred polyolefin composition comprises a homogeneous, random copolymer of ethylene and acrylic acid. Copolymers of ethylene and acrylic acid or of ethylene and vinyl acetate may be obtained from The Dow Chemical Company. Ethylene vinyl acetate copolymer may also be obtained under tradename Elvax from E. I. duPont deNemours & Company. Anhydride modified copolymers or ethylene are available under the tradename Plexar from Norchem, Inc. Ionomeric copolymers are available under the tradename Surlyn from E. I. duPont deNemours & Company.
  • the polyolefin composition comprises greater than 50 percent, preferably greater than 80 percent, and more preferably greater than 95 percent polyolefin by weight of the foam structure.
  • blowing agents include halocarbons such as fluorocarbons and chlorofluorocarbons; hydrohalocarbons 5 such as hydrofluorocarbons and hydrochlorofluorocarbons; alkylhalides such as methyl chloride and ethyl chloride; hydrocarbons such as the alkanes or alkenes of 2 to 9 carbon atoms; common gases such as air, carbon dioxide, Q nitrogen, argon; water; or mixtures of any of the above.
  • halocarbons such as fluorocarbons and chlorofluorocarbons
  • hydrohalocarbons 5 such as hydrofluorocarbons and hydrochlorofluorocarbons
  • alkylhalides such as methyl chloride and ethyl chloride
  • hydrocarbons such as the alkanes or alkenes of 2 to 9 carbon atoms
  • common gases such as air, carbon dioxide, Q nitrogen, argon; water; or mixtures of any of the above.
  • blowing agents are alkanes such as butane, isobutane, pentane, isopentane, hexane, isohexane, heptane, and the like.
  • a most preferred C blowing agent is isobutane.
  • hydrocarbons such as alkanes are preferred due to their relatively low ozone depletion potential.
  • Suitable blowing agents also include chemical blowing agents such as ammonium and azo type compounds. Such compounds include ammonium carbonate, ammonium bicarbonate, potassium bicarbonate, diazoaminobenzene, diazoaminotoluene, azodicarbonamide, diazoisobutyronitrile, and the like.
  • non-crosslinked foam structure means that the foam composition comprising the strands from which the foam structure is formed is substantially free of crosslinking.
  • non-crosslinked is inclusive however, of the slight degree of crosslinking which may occur naturally without the use of crosslinking agents.
  • Suitable foam structures have gross densities (that is bulk densities or densities of the closed-cell foam including interstitial channels or voids between strands or profiles), preferably varying from 3.2 to 48 kilograms per cubic meter (kg/m3). Most preferred foam
  • a preferable alternate embodiment comprises portions having densities less than 32 kg/m3.
  • the individual * - strands of foam comprising the foam structure preferably possess a local or strand density from 8.0 to 96 kg/m3, and most preferably from 16 to 48 kg/m3.
  • the present foam structure is comprised of foam 0 strands having an average cell size of between 0.02 to 0.5 millimeters.
  • a particularly preferred foam structure is comprised of foam strands having an average cell size of between 0.1 and 0.3 millimeters.
  • closed-cell foam structure preferably at least 70 percent closed-cell according to ASTM D-2856 not including interstitial channels or voids between the foam strands comprising the foam structure.
  • a polyolefin foam structure of the present invention was formed by extruding a composition of polyethylene/ Surlyn ® 8660 ionomer in a 90/10 weight ratio, 26 parts per hundred CFC-114/CFC-12 in a 80/20 weight ratio, and 0.8 parts per hundred at a rate of 136 kilograms per hour through a multiorifice die containing 1500 circular orifices arranged in a rectangular configuration.
  • the resulting structure had a cross- sectional dimension of 3.8 centimeters by 62.2 centimeters and an average cell size of 0.3 millimeters.
  • the structure was substantially free of distortion

Abstract

Structure de mousse cellulaire non réticulée dont le rapport entre les dimensions mineures et les dimensions majeures est de 1/8 au moins, comprenant une pluralité de filaments ou de profilés extrudés fusionnés d'une composition polyoléfinique cellulaire ayant une grosseur cellulaire moyenne comprise entre 0,02 et 0,5 millimètres. La géométrie en sections transversales de la structure de mousse correspond sensiblement à l'agencement global des orifices de la matrice à partir de laquelle la composition polyoléfinique cellulaire a été extrudée. L'invention concerne également un procédé de production de la structure de mousse précitée consistant à extruder une composition polyoléfinique expansible par la matrice à orifices multiples afin de former ladite structure.Structure of non-crosslinked cellular foam whose ratio between the minor dimensions and the major dimensions is at least 1/8, comprising a plurality of filaments or extruded profiles fused with a cellular polyolefin composition having an average cell size of between 0, 02 and 0.5 millimeters. The geometry in cross sections of the foam structure corresponds substantially to the overall arrangement of the orifices of the matrix from which the cellular polyolefin composition was extruded. The invention also relates to a method for producing the above-mentioned foam structure consisting in extruding an expandable polyolefin composition through the multi-orifice matrix in order to form said structure.

Description

NONDISTORTED POLYOLEFIN FOAM STRUCTURES AND PROCESS FOR MAKING
Background of the Invention
The invention relates to a closed-cell, non- crosslinked polyolefin foam structure of relatively small cell size and relatively low cross-section minor to major dimension ratio. The extruded structure is substantially free of distortion, convolution, or corrugation from its intended shape or geometry.
Solid closed-cell polyolefin foam structures of relatively low cross-section minor to major dimension ratio, height to width in the case of those of rectangular cross-section, have found numerous commercial applications such as cushioning, packaging, insulation, sheeting, and the like. To enhance insulative performance, softness, sound absorption, and nonabrasiveness of such structures, it would be desirable to reduce the cell size of the polyolefin foam comprising the structure.
A problem with making solid closed-cell, non- crosslinked polyolefin foam structures of relatively small cell sizes (e.g. 0.02 to 0.5 millimeters (mm)) and relatively low cross-section dimension ratios (e.g. 1/8 or less) is that the structure actually formed may be in a geometry or shape other than that intended. As the foamable composition from which the structure is made exits the die, it is not able to expand directionally outward with respect to the major dimension of the die orifice at a rate sufficient to prevent the structure from becoming distorted, convoluted, or corrugated along its major dimension. The structure cannot expand rapidly enough because relatively small cell size foams
10 have relatively high foaming rates, which result from the relatively high levels of nucleator required to make foams having relatively small cell size.
It would be desirable to have a closed-cell, * *. non-crosslinked polyolefin foam structure of relatively low cross-section minor to major dimension ratio comprised of a polyolefin foam of relatively small cell size. Such foam structure would be substantially free of deviation or distortion from its intended shape or 0 geometry.
Summary of the Invention
According to the present invention, there is a 5 closed-cell, non-crosslinked foam structure of a ratio of minor dimension to major dimension of about 1/8 or less in cross-section comprised of coalesced strands or profiles of a foamed polyolefin composition having an average cell size of from 0.02 to 0.5 millimeters. The 0 foam structure substantially corresponds in cross- sectional geometry to the geometry of the overall arrangement of the orifices of the die from which it was extruded. The extrusion of the foam structure in the form of coalesced strands or profiles allows structures of such relative cross-sectional dimension ratios (e.g. height to width for rectangular structures) in such cell size range to be formed without distortion, convolution, or corrugation from the intended or desired shape or geometry. Distortion, convolution, or corrugation from the intended or desired shape or geometry is substantially avoided because the strands or profiles expand into the channels between themselves instead of foam expanding against itself as in a solid foam.
According to the present invention, there is a process for making a closed-cell, non-crosslinked foam structure of a ratio of minor dimension to major dimension in cross-section of 1/8 or less and comprised of a foamed polyolefin composition having an average cell size of from 0.02 to 0.5 millimeters. The process comprises extruding a foamable polyolefin composition through a die defining a plurality of orifices therein to form a plurality of coalesced extruded strands or profiles of the foamed polyolefin composition forming the above foam structure substantially corresponding to the geometry of the overall arrangement of the orifices of the die.
Detailed Description
The present foam structure is formed of coalesced closed-cell, non-crosslinked polyolefin foam strands or profiles having an average cell size of from 0.02 to 0.5 millimeters and minor to major dimension ratios of less than 1/8 or less to be made substantially corresponding to the shape or geometry of the overall arrangement of the orifices of the die from which the structure was extruded. The present foam structure circumvents the problems associated with prior art foam structures of that cell size range and relative dimension by its ability to accommodate the high rate of foaming without being distorted, convoluted, or corrugated.
The present foam structure is formed by extrusion of a molten foamable, non-crosslinked polyolefin composition through a multiorifice die. The foamable composition is formed by melt plastifying the polyolefin and blending therein a blowing agent and other additives such as a nucleating agent. The
10 orifices of the multiorifice die are arranged so that contact between adjacent streams of the molten extrudate occurs during the foaming process and the contacting surfaces adhere to one another with sufficient adhesion -j- to result in a unitary foam structure. The streams of molten extrudate exiting the die take the form of strands or profiles, which desirably foam, coalesce, and adhere to one another to form a unitary structure. Desirably, the coalesced individual strands or profiles 0 of polyolefin foam should remain adhered into unitary structure to prevent strand delamination under stresses encountered in preparing, shaping, and using the foam. Apparatuses and methods for producing foam structures of strand form are seen in U.S. Patents 3,573*152 and 5 4,82-4, 720.
The strands or profiles will vary in cross- sectional shape or geometry according to the shape or geometry of the orifices in the die. The strands or 0 profiles may be the same or different shape or geometry than the foam structure which they coalesce to form. The orifices may take on a circular shape or a noncircular shape though circular is preferred. Suitable noncircular shapes include X-shaped, cross- or star-shaped, or polygonal-shaped. The various orifices in the die may be specially arranged in a desired configuration or array such as a sine wave, honeycomb, square saw tooth, or a triangular saw tooth wave pattern. Preferably, the individual strands, have a major dimension in cross-section, diameter in the case of circular strands, of between 0.5 and 10 millimeters and most preferably between 1.0 and 5.0 millimeters.
The orifices in the die will be of shape or
10 geometry and be spacially arranged such that there will be sufficient channel volume or clearance between the streams of molten extrudate exiting from the same for them to foam to form the strands or profiles without
* r- substantial distortion, convolution, or corrugation of the resulting unitary foam structure relative to the geometry of the overall arrangement of the orifices. The streams of molten extrudate may foam to either partly or completely fill the open channel volume 0 between the strands or profiles.
The geometry or shape of the resulting foam structure will substantially correspond to the overall arrangement or geometry of the die orifices or, in other 5 words, to the intended or desired shape or geometry. For instance, a plurality or multiplicity of circular orifices arranged in a rectangular pattern will yield a rectangular foam structure. A plurality or multiplicity of circular orifices arranged in a circular pattern will 0 yield a cylindrical or circular foam structure. The geometry or shape of the present foam structure will correspond to the overall arrangement or geometry of the orifices in the die from which it is extruded without substantial distortion, convolution, or corrugation therefrom.
The foam structure typically will have cross- sectional dimensions larger than the dimensions defined by the overall arrangement or geometry the die orifices of the die from which it was extruded due to foaming of the molten extrudate, but the relative cross-sectional dimensions of the foam structure will substantially correspond to the relative dimensions of the overall
10 arrangement or geometry of the die orifices. For instance, in the case of a rectangular arrangement of circular die orifices, the resulting foam structure will have rectangular cross-sectional dimensions exceeding _.,- that of the overall arrangement or geometry of the die orifices, but will have substantially the same relative cross-sectional dimensions.
Blending of various components in the method of 0 the present invention in order to provide suitable foamable polyolefin compositions accomplished according to known techniques in the art. Suitably, a mixer, extruder, or other suitable blending device is employed to obtain a homogeneous melt. The extruder or other 5 suitable blending device is also employed to incorporate a blowing agent. Nucleating agents, extrusion aids, antioxidants, colorants, pigments, etc. may also be incorporated as desired.
0 Suitable foamable polyolefin compositions include polyethylene or polypropylene. Preferred are copolymers of ethylene and a monoethylenically unsaturated polar monomer copolymerizable therewith, especially carboxyl-containing comonomers. Examples include copolymers of ethylene and acrylic acid or methacrylic acid and Cι_4 alkyl ester or ionomeric derivatives thereof; ethylene vinyl-acetate copolymers; ethylene/carbon monoxide copolymers; anhydride containing olefin copolymers of a diene and a polymerizable; copolymers of ethylene and an α-olefin having ultra low molecular weight (i.e., densities less than 0.92 grams/cubic centimeter); blends of all of the foregoing resins; blends thereof with polyethylene (high, intermediate or low density); etc. Particularly preferred compositions are copolymers of ethylene and acrylic acid, (EAA copolymers) having up to about 30 percent by weight of copolymerized acrylic acid; ionomeric derivatives of the foregoing, copolymers of ethylene and vinyl acetate; ultra low density polyethylene; and blends of the foregoing with one another and with low density polyethylene.
The polymers of ethylene and a polar comonomer may be prepared by known addition polymerization techniques, or by a grafting reaction of the reactive comonomer with a preformed polymer of ethylene. Additional elastomeric components such as polyiso- butylene, polybutadiene, ethylene/propylene copolymers, and ethylene/propylene diene interpolymers may be included in the blend if desired.
A most preferred resin composition comprises a copolymer of ethylene and acrylic acid or ethylene and vinyl acetate containing from 85 percent to 98 percent ethylene by weight. A most preferred polyolefin composition comprises a homogeneous, random copolymer of ethylene and acrylic acid. Copolymers of ethylene and acrylic acid or of ethylene and vinyl acetate may be obtained from The Dow Chemical Company. Ethylene vinyl acetate copolymer may also be obtained under tradename Elvax from E. I. duPont deNemours & Company. Anhydride modified copolymers or ethylene are available under the tradename Plexar from Norchem, Inc. Ionomeric copolymers are available under the tradename Surlyn from E. I. duPont deNemours & Company.
The polyolefin composition comprises greater than 50 percent, preferably greater than 80 percent, and more preferably greater than 95 percent polyolefin by weight of the foam structure. 0
The present foam structure is extruded with one or more of any blowing agents known in the art. Suitable blowing agents include halocarbons such as fluorocarbons and chlorofluorocarbons; hydrohalocarbons 5 such as hydrofluorocarbons and hydrochlorofluorocarbons; alkylhalides such as methyl chloride and ethyl chloride; hydrocarbons such as the alkanes or alkenes of 2 to 9 carbon atoms; common gases such as air, carbon dioxide, Q nitrogen, argon; water; or mixtures of any of the above.
Preferred blowing agents are alkanes such as butane, isobutane, pentane, isopentane, hexane, isohexane, heptane, and the like. A most preferred C blowing agent is isobutane. hydrocarbons such as alkanes are preferred due to their relatively low ozone depletion potential. Suitable blowing agents also include chemical blowing agents such as ammonium and azo type compounds. Such compounds include ammonium carbonate, ammonium bicarbonate, potassium bicarbonate, diazoaminobenzene, diazoaminotoluene, azodicarbonamide, diazoisobutyronitrile, and the like.
The term non-crosslinked foam structure means that the foam composition comprising the strands from which the foam structure is formed is substantially free of crosslinking. The term non-crosslinked is inclusive however, of the slight degree of crosslinking which may occur naturally without the use of crosslinking agents.
Suitable foam structures have gross densities (that is bulk densities or densities of the closed-cell foam including interstitial channels or voids between strands or profiles), preferably varying from 3.2 to 48 kilograms per cubic meter (kg/m3). Most preferred foam
10 structures have a density from 8.0 to 45 kg/m3. For specific uses in low weight cushioning applications a preferable alternate embodiment comprises portions having densities less than 32 kg/m3. The individual * - strands of foam comprising the foam structure preferably possess a local or strand density from 8.0 to 96 kg/m3, and most preferably from 16 to 48 kg/m3.
The present foam structure is comprised of foam 0 strands having an average cell size of between 0.02 to 0.5 millimeters. A particularly preferred foam structure is comprised of foam strands having an average cell size of between 0.1 and 0.3 millimeters.
5 In the present closed-cell foam structure, preferably at least 70 percent closed-cell according to ASTM D-2856 not including interstitial channels or voids between the foam strands comprising the foam structure.
0 To further illustrate the present invention, a nonlimiting example of same is provided below.
EXAMPLE
A polyolefin foam structure of the present invention was formed by extruding a composition of polyethylene/ Surlyn® 8660 ionomer in a 90/10 weight ratio, 26 parts per hundred CFC-114/CFC-12 in a 80/20 weight ratio, and 0.8 parts per hundred at a rate of 136 kilograms per hour through a multiorifice die containing 1500 circular orifices arranged in a rectangular configuration. The resulting structure had a cross- sectional dimension of 3.8 centimeters by 62.2 centimeters and an average cell size of 0.3 millimeters. The structure was substantially free of distortion,
10 convolution, or corrugation from its intended rectangular shape.
While embodiments of the method and the foam of the present invention have been shown with regard to
* c specific details, it will be appreciated that depending upon the manufacturing process and the manufacturer's desires, the present invention may be modified by various changes while still being fairly within the scope of the novel teachings and principles herein set 0 forth.
5
0

Claims

WHAT IS CLAIMED IS:
1. A process for making a closed-cell, non- crosslinked, nondistorted extruded foam structure of a ratio of minor dimension to major dimension in cross- section of about 1/8 or less and comprised of a foamed polyolefin composition having an average cell size of from 0.02 to 0.5 millimeters, comprising: a) forming a foamable polyolefin composition capable of forming a foamed polyolefin composition having an average cell size of from 0.02 to 0.5 millimeters, b) extruding the foamable composition through a die defining a plurality of orifices therein having an overall arrangement of minor to major dimension in cross-section of 1/8 or less to form a plurality of foamable strands and c) allowing the foamable strands to expand and coalesce to form the foam structure.
2. The process of Claim 1, wherein the foam structure is generally rectangular in cross-section.
3. The process of Claim 1, wherein the polyolefin comprises polyethylene or a copolymer thereof.
4. The process of Claim 1, wherein the polyolefin comprises polypropylene or a copolymer thereof.
5. The process of Claim 1, wherein the foamed polyolefin composition has an average cell size of between 0.1 and 0.3 millimeters.
6. A foam structure made according to the process of Claim 1.
EP92908512A 1991-03-25 1992-02-21 Nondistorted polyolefin foam structures and process for making Withdrawn EP0587581A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US67400791A 1991-03-25 1991-03-25
US674007 1991-03-25

Publications (2)

Publication Number Publication Date
EP0587581A4 EP0587581A4 (en) 1993-12-16
EP0587581A1 true EP0587581A1 (en) 1994-03-23

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JP (1) JPH06505935A (en)
KR (1) KR100195552B1 (en)
AU (1) AU1581292A (en)
CA (1) CA2104961C (en)
FI (1) FI934187A (en)
HU (1) HU213639B (en)
MX (1) MX9201305A (en)
NO (1) NO933415D0 (en)
TW (1) TW257774B (en)
WO (1) WO1992016363A1 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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MX9201305A (en) 1992-10-01
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TW257774B (en) 1995-09-21
FI934187A (en) 1993-09-24
WO1992016363A1 (en) 1992-10-01
AU1581292A (en) 1992-10-21
JPH06505935A (en) 1994-07-07
EP0587581A4 (en) 1993-12-16
HUT65896A (en) 1994-07-28
HU213639B (en) 1997-08-28
CA2104961A1 (en) 1992-09-26
NO933415L (en) 1993-09-24
NO933415D0 (en) 1993-09-24
KR100195552B1 (en) 1999-06-15

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