WO1996018501A1 - Multi-laser heat-shrinkable film - Google Patents
Multi-laser heat-shrinkable film Download PDFInfo
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- WO1996018501A1 WO1996018501A1 PCT/US1995/016202 US9516202W WO9618501A1 WO 1996018501 A1 WO1996018501 A1 WO 1996018501A1 US 9516202 W US9516202 W US 9516202W WO 9618501 A1 WO9618501 A1 WO 9618501A1
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- film
- ethylene
- shrink
- heat
- temperature
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/30—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/30—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
- B32B27/306—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers comprising vinyl acetate or vinyl alcohol (co)polymers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/34—Layered products comprising a layer of synthetic resin comprising polyamides
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B7/00—Layered products characterised by the relation between layers; Layered products characterised by the relative orientation of features between layers, or by the relative values of a measurable parameter between layers, i.e. products comprising layers having different physical, chemical or physicochemical properties; Layered products characterised by the interconnection of layers
- B32B7/04—Interconnection of layers
- B32B7/12—Interconnection of layers using interposed adhesives or interposed materials with bonding properties
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B38/00—Ancillary operations in connection with laminating processes
- B32B2038/0052—Other operations not otherwise provided for
- B32B2038/0076—Curing, vulcanising, cross-linking
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2270/00—Resin or rubber layer containing a blend of at least two different polymers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/70—Other properties
- B32B2307/732—Dimensional properties
- B32B2307/734—Dimensional stability
- B32B2307/736—Shrinkable
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2323/00—Polyalkenes
- B32B2323/04—Polyethylene
- B32B2323/046—LDPE, i.e. low density polyethylene
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2329/00—Polyvinylalcohols, polyvinylethers, polyvinylaldehydes, polyvinylketones or polyvinylketals
- B32B2329/04—Polyvinylalcohol
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2331/00—Polyvinylesters
- B32B2331/04—Polymers of vinyl acetate, e.g. PVA
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2377/00—Polyamides
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2439/00—Containers; Receptacles
- B32B2439/70—Food packaging
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D75/00—Packages comprising articles or materials partially or wholly enclosed in strips, sheets, blanks, tubes, or webs of flexible sheet material, e.g. in folded wrappers
- B65D75/002—Packages comprising articles or materials partially or wholly enclosed in strips, sheets, blanks, tubes, or webs of flexible sheet material, e.g. in folded wrappers in shrink films
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S428/00—Stock material or miscellaneous articles
- Y10S428/91—Product with molecular orientation
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/24—Structurally defined web or sheet [e.g., overall dimension, etc.]
- Y10T428/24942—Structurally defined web or sheet [e.g., overall dimension, etc.] including components having same physical characteristic in differing degree
- Y10T428/2495—Thickness [relative or absolute]
- Y10T428/24967—Absolute thicknesses specified
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31855—Of addition polymer from unsaturated monomers
- Y10T428/31909—Next to second addition polymer from unsaturated monomers
- Y10T428/31913—Monoolefin polymer
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31855—Of addition polymer from unsaturated monomers
- Y10T428/31909—Next to second addition polymer from unsaturated monomers
- Y10T428/31913—Monoolefin polymer
- Y10T428/3192—Next to vinyl or vinylidene chloride polymer
Definitions
- the present invention relates to a multi-layer heat-shrinkable film showing a specific shrink behavior suitable for use as a packaging film.
- the present invention is also related to a process of making such a film and to packages comprising it.
- Heat-shrinkable multilayer films comprising a core layer comprising an ethylene-vinyl alcohol copolymer, two outer layers comprising blends of ethylene- ⁇ -olefin copolymers and ethylene-vinyl acetate copolymers, and two adhesive layers, are known.
- US-A-4,457,960 discloses the use of ethylene-vinyl alcohol copolymers and blends thereof in a multi-layer film which may be heat-shrinkable and comprise blends of ethylene- ⁇ -olefin copolymers and ethylene-vinyl acetate copolymers in the outer layers.
- EP-A-87,080 relates to films having the above general structure and characterized by the fact that the ratio of the weight of the ethylene-vinyl acetate copolymer to the total weight of the polymers of the two outer layers is higher than 0.4.
- EP-A-141 ,555 discloses an oriented five-layer film having a core layer of a blend of an ethylene-vinyl alcohol copolymer and nylon or nylon copolymer, two adhesive layers and two surface layers of a blend of ethylene- ⁇ -olefin copolymers and ethylene-vinyl acetate copolymers.
- EP-A-217,596 describes a heat-shrinkable multilayer film comprising a cross- linked core layer comprising a blend of an ethylene-vinyl alcohol copolymer and a polyamide resin, two cross-linked inner layers each comprising an adhesive resin, and two cross-linked surface layers each comprising a three component blend of an ethylene- ⁇ -olefin copolymer of low density, an ethylene- ⁇ -olefin copolymer of medium density and an ethylene-vinyl acetate copolymer.
- a general method of manufacture of the heat-shrinkable films involves the co-extrusion of a thick tubular shape laminate film (called "tape") which is quenched just under the die, collapsed by a pair of nip rolls and then heated to a predetermined temperature above the glass transition temperature (Tg) but below the melting temperature of the composition and stretched in both the longitudinal (machine) and the transverse directions to get a cylindrically-shaped laminate thin film. After being so stretched the film is rapidly cooled to somehow freeze-in the resulting film a latent shrinkability.
- the film thus obtained when heated to a temperature close to the temperature at which it has been stretched (or oriented) under conditions where nil or negligible restraint to inhibit shrinkage is present, will exhibit a rapid and irreversible reduction in its linear dimensions.
- a particularly high free shrink is one of the key attributes of a film for food packaging as it provides the package with a skin ⁇ tight wrapping, which remarkably improves the appearance of the package and enhances the commercial value of its content.
- the above films should have a thickness of at least 15 ⁇ , preferably at least 18 ⁇ , wherein the thickness of the gas-barrier layer is at least 3 ⁇ , preferably at least 4 ⁇ , and an orientation ratio, i.e., the multiplication product of the extent to which the tape is expanded in two directions perpendicular to one another, of at least 2x2, and preferably at least 2.5x2.5 to provide the desired high free shrink.
- an orientation ratio i.e., the multiplication product of the extent to which the tape is expanded in two directions perpendicular to one another, of at least 2x2, and preferably at least 2.5x2.5 to provide the desired high free shrink.
- a high shrink force particularly in one direction, may create severe problems as it may lead to a distortion of the packaged articles.
- thermoplastic multilayer films having a core layer comprising an ethylene-vinyl alcohol copolymer, two outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost outermost
- SUBSTITUTE SHEET (RULE 2& layers of blends comprising ethylene-vinyl acetate and ethylene- ⁇ -olefin copolymers, and two adhesive layers, such as for instance those films marketed by Cryovac® under the tradename BDF, is in the modified atmosphere packaging (MAP) of food products placed on trays or otherwise flexible lower support members.
- MAP modified atmosphere packaging
- the food product in the tray is wrapped into a film envelope under a gas flushing.
- the excess gas is removed from the envelope by means of a slight pressure on top of the package (to avoid the ballooning effect during shrinkage), the open end of the envelope is then sealed, and the loose package is passed into a hot air shrink tunnel set at a temperature of from 140 to 160X, for a short time sufficient to let the film reach a temperature of about 120 ⁇ 10'C, to provide a tight package.
- the known films will shrink by at least 40 % in both dimensions but at the same time they will release a very high shrink force.
- the high shrink tension in the transverse direction may lead to a more or less severe distortion of the tray that in any case impairs the package appearance.
- a first object of the present invention is therefore a heat-shrinkable film comprising a core layer comprising an ethylene-vinyl alcohol copolymer, two outer layers of blends comprising ethylene-vinyl acetate and ethylene- ⁇ -olefin copolymers, and two adhesive layers, characterized in that said film has a free shrink of at least 40 %, preferably at least 45 % and most preferably at least 50 %, in both dimensions at 120 ' C and a maximum shrink force in the transverse direction, throughout its range of shrink temperatures, not exceeding 0.5 N/cm.
- film is used in a generic sense to include any flat and flexible material having a thickness of between about 15 and about 150 ⁇ .
- biaxially oriented heat-shrinkable film is meant a film which has been drawn, at a temperature above the glass transition temperature (Tg) but below the melting temperature of the polymers, in two mutually perpendicular directions in the plane of the film to induce molecular orientation therein.
- Tg glass transition temperature
- the orientation in the two directions may be balanced or the film may be more highly oriented in a preferred direction than in the other.
- the orientation in the two directions is typically carried out simultaneously by a so-called "bubble" process.
- core refers to any internal film layer which has a primary function other than serving as an adhesive or compatibiliser for adhering two layers to one another.
- the core layer as used in the present application provides the multilayer film with the desired gas barrier properties.
- said core layer will comprise an ethylene-vinyl alcohol copolymer (EVOH), wherein said term refers to saponified products of ethylene-vinyl ester copolymers, generally of ethylene-vinyl acetate copolymers, wherein the ethylene content is typically comprised between 20 and 60 % by mole and the degree of saponification is generally higher than 85 and preferably higher than 95 %.
- EVOH ethylene-vinyl alcohol copolymer
- the ethylene-vinyl alcohol copolymer can be employed alone or blended with other EVOHs, ethylene-vinyl acetate copolymers, ionomers or, preferably with one or more polyamides.
- outer layer refers to either one of the two outermost layers of the multi-layer film which in the end package will be in contact with the food or with the environment.
- adhesive layer refers to an internal layer having the primary function of adhering two layers to one another. They will be comprised of materials which provide structural integrity to the multilayered barrier structure without substantially affecting the barrier properties of the gas-barrier layer or the mechanical and physical properties of the outer layers. Typically said adhesive layer will comprise modified polyolefins.
- polymer or “polymer resin” generally include but are not limited to, homopolymers, copolymers, such as for instance, block, graft, random, and alternating copolymers, etc. as well as blends and modifications thereof.
- copolymer as used herein is intended to denote polymers of two or more comonomers. Therefore, although the present specification generally refers to ethylene- ⁇ -olefin copolymers, such term is intended to encompass copolymers of ethylene with one or more ⁇ -olefins or of ethylene with an ⁇ -olefin and another comonomer.
- polyolefin refers to a thermoplastic resin obtained by polymerisation of an olefin or by copolymerisation of two or more olefins or of one or more olefins with other comonomers, wherein the olefin units are anyway present in larger amounts than any possibly present comonomer.
- Suitable examples of "polyolefins” are ethylene- ⁇ -olefin copolymers, ethylene-vinyl acetate copolymers, ethylene-acrylic acid or methacrylic acid copolymers, ethylene-propylene copolymers, ethylene-propylene-butylene copolymers, and the like.
- modified polyolefin means a polyolefin characterized by the presence of functional groups such as typically anhydride or carboxy groups.
- modified polyolefins are graft copolymers of maleic acid or anhydride onto ethylene-vinyl acetate copolymers, graft copolymers of fused ring carboxylic anhydrides onto polyethylene, resin mixtures of these and mixtures with polyethylene or ethylene- ⁇ -olefin copolymers.
- ethylene- ⁇ -olefin copolymer designates a copolymer of ethylene with one or more (C4-C8)- ⁇ -olefin preferably selected from the group consisting of copolymers or terpolymers of ethylene with 1-butene, 4-methyl-1-pentene, 1- hexene, and 1-octene.
- Ethylene- ⁇ -olefin copolymers can be prepared using Ziegler-Natta or metallocene single site (constrained geometry) catalyst.
- the heterogeneous ethylene- ⁇ -olefin copolymers prepared using Ziegler-Natta catalysts are generally classified as linear low density polyethylene (LLDPE), having a density usually in the range of from about 0.915 g/cc to about 0.925 g/cc, linear medium density polyethylene (LMDPE), having a density usually in the range of from about 0.926 to about 0.941 g/cc, and very low density polyethylene (VLDPE), having a density lower than 0.915 g/cc.
- LLDPE linear low density polyethylene
- LMDPE linear medium density polyethylene
- VLDPE very low density polyethylene
- ethylene-vinyl acetate copolymer refers to a copolymer formed from ethylene and vinyl acetate monomers wherein the ethylene derived units in the copolymer are present in major amounts and the vinyl acetate derived units in the copolymer are present in minor amounts.
- ethylene-vinyl acetate copolymer refers to a copolymer of ethylene with a copolymerizable ethylenically unsaturated acidic monomer, usually an ethylenically unsaturated carboxylic acid which may be di- or more basic but is generally mono-basic, for example acrylic or methacrylic acid.
- polyamide means a high molecular weight polymer having amide linkages, and as used herein it refers more specifically to synthetic polyamides, either aliphatic or aromatic, either in crystalline or amorphous form. It is intended to refer to both polyamides and co-polyamides. Exemplary of such polyamides are those polymers commonly referred to as e.g. nylon 6, nylon 66, nylon 6-66, nylon 610, nylon 12, nylon 69, and nylon 6-12.
- the present invention refers to a heat-shrinkable film comprising a core layer essentially consisting of ethylene-vinyl alcohol copolymer(s) optionally blended with polyamide(s), two outer layers of blends comprising ethylene-vinyl acetate and ethylene- ⁇ -olefin copolymers, and two adhesive layers, characterized in that said film has a free shrink of at least 40 %, preferably at least 45 % and most preferably at least 50 %, in both dimensions at 120'C and a maximum shrink force in the transversal direction, throughout its range of shrink temperatures, not exceeding 0.5 N/cm.
- the present invention refers to a heat- shrinkable film comprising a core layer essentially consisting of ethylene-vinyl alcohol copolymer(s) optionally blended with polyamide(s), two outer layers of blends essentially consisting of ethylene-vinyl acetate copolymer, and one or more ethylene- ⁇ -olefin copolymers of differing densities, and two adhesive layers, characterized in that said film has a free shrink of at least 40 %, preferably at least 45 % and most preferably at least 50 %, in both dimensions at 120 * C and a maximum shrink force in the transversal direction, throughout its range of shrink temperatures, not exceeding 0.5 N/cm.
- the present invention refers to a heat- shrinkable film comprising a core layer essentially consisting of a blend of ethylene-vinyl alcohol copolymer(s) with polyamide(s), two outer layers essentially consisting of a blend of an ethylene-vinyl acetate copolymer, an ethylene- ⁇ -olefin copolymer of low density (LLDPE) and an ethylene- ⁇ -olefin copolymer of medium density (LMDPE), and two adhesive layers, characterized in that said film has a free shrink of at least 45 % and preferably at least 50 %, in both dimensions at 120 " C and a maximum shrink force in the transversal direction, throughout its range of shrink temperatures, not exceeding 0.5 N/cm.
- the present invention refers to a heat- shrinkable film comprising a cross-linked core layer essentially consisting of a blend of an ethylene-vinyl alcohol copolymer with up to 20 % by weight of a polyamide, two outer cross-linked layers essentially consisting of a blend of an ethylene-vinyl acetate copolymer, an ethyiene- ⁇ -olefin copolymer of low density (LLDPE) and an ethylene- ⁇ -olefin copolymer of medium density (LMDPE), and two cross-linked adhesive layers, characterized in that said film has a free shrink of at least 45 % and preferably at least 50 %, in both dimensions at 120"C and a maximum shrink force in the transversal direction, throughout its range of shrink temperatures, not exceeding 0.5 N/cm.
- a cross-linked core layer essentially consisting of a blend of an ethylene-vinyl alcohol copolymer with up to 20 % by weight of a polyamide
- additives for instance plasticisers (for the core layer), antioxidizers, slip and antiblock agents, UV absorbers, pigments, antifog agents or compositions, antimicrobial agents, cross- linking agents, oxygen scavenging agents or compositions used to improve the film barrier properties, and the like agents.
- this term should not exclude the presence of minor amounts of different resins or blends of resins coming for instance from the recycle of polymer scrap material, as far as these minor amounts do not substantially alter the film attributes and performance.
- a general process used for the manufacture of the starting films involves coextruding the different polymers through a round die of suitable dimensions, quickly quenching the thus obtained thick tubular film just below the die, reheating said tape to a suitable temperature, and biaxially orienting it by inflation of air to achieve the transverse orientation and by a differential speed of the pinch rolls which hold the bubble to achieve the longitudinal orientation.
- the starting films can also be prepared by extrusion coating wherein the multilayer tube is formed by extruding or co-extruding a first tape (called the primary tape) and then coating said tape with the other layers which are either sequentially extruded or in a single step coextruded thereon.
- the starting film has to be cross-linked, this is generally achieved by submitting the film to an energetic radiation treatment, typically by high energy electron treatment. In such a case irradiation is most preferably performed prior to orientation. Radiation dosages are referred to herein in terms of the radiation units "Grays", with one thousand Grays being designated as "KGrays". A suitable radiation dosage of high energy may be in the range of up to about 120 KGrays, more preferably from about 20 to about 90 KGrays.
- the irradiation step can be carried out also after orientation.
- the irradiation step will be carried out on the primary tape.
- chemical cross-linking of the resins can be achieved by the addition of suitable cross-linking agents, e.g. peroxides, to the resins to be cross- linked or a combination of chemical cross-linking and irradiation can be used where the cross-linking agents added to the resins need some irradiation to trigger the cross-linking reaction.
- the films obtained as described above are subjected to a heat treatment under strictly controlled conditions.
- thermoplastic structures such as annealing or heat-setting
- heat treatment of thermoplastic structures are widely known processes in the field of plastic materials.
- the annealing process is defined as a heat-treatment process aiming at the removal of strains and stresses set up in the material during its forming and fabricating operations.
- the plastic is brought to a certain temperature called the annealing temperature, kept at this temperature for a definite period of time, and then slowly cooled to room temperature.
- the key effect of the annealing process is therefore to improve the dimensional stability of the polymer when exposed to elevated temperatures. Furthermore annealing frequently improves the impact strength and prevents cracking of excessively stressed items. This process is therefore widely used when a maximum dimensional stability or the enhancement of certain properties of the articles for specific applications are required in injection molding, blow molding, extrusion of heavy sheet or film extrusion.
- the films are very often drawn to cause molecular orientation therein and thereby improve the film physical properties and then subjected to a heat- treatment, called heat-setting, where the films, while restrained against shrinkage, are heated at a temperature above the glass transition temperature of the polymers and below their melting points, to stabilize the molecules in the oriented state and eliminating almost completely the shrinkage while retaining the improved mechanical properties.
- heat-setting a heat-treatment
- heat-treatments of the films before shrinkage are rarely described or used.
- GB-A-2,221,649 that is directed to a polyolefin film which, just owing to its specific structure (i.e. the specific polymers used for the core and for the outer layers and their ratio) exhibits a low shrink force, describes a heat- treatment of the film at low temperatures to avoid spontaneous shrinkage when the film is allowed to stand as it is.
- the heat treatment suitable to obtain the films according to the present invention involves heating the film obtained by the known extrusion and orientation processes to a temperature of from about 70 to about 100'C for a very short time and then quickly cooling it down to a temperature below room temperature, preferably below about 20 * C.
- heating of the film should last for a time at least sufficient to induce a decrease of the maximum transverse shrink force of the film to a value not exceeding 0.5 N/cm but not long enough to substantially affect the film % free shrink at 120'C.
- the heating time is comprised between about 0.1 and about 7.5 s.
- a further specific object of the present invention is therefore a method of selectively reducing the transverse shrink force of a heat-shrinkable film comprising a core layer comprising an ethylene-vinyl alcohol copolymer, two outer layers of blends comprising ethylene-vinyl acetate and ethylene- ⁇ -olefin copolymers, and two adhesive layers, to a value not exceeding 0.5 N/cm throughout its range of shrink temperatures, while maintaining substantially unaffected the % free shrink of the film at 120 * C, which comprises heating the film obtained by the known extrusion and orientation processes and having a transverse shrink force higher than 0.5 N/cm to a temperature of from about 70 to about 100'C for a time sufficient to induce a decrease of the maximum transverse shrink force of the film to a value not exceeding 0.5 N/cm without substantially affecting the film % free shrink at 120 ' C and then quickly cooling it down to a temperature below room temperature, preferably below about 20' C.
- the heating time is of from about 0.1 to about 7.5 s.
- the heat treatment according to the present invention might be carried out off- line, but preferably it is performed right on the line of all other processing operations.
- the heat-treatment may be carried out either before or after cross-linking, otherwise it is carried out, after orientation, on the flattened tubular film collected by the upper nip rolls before the film is wound up or on the mono-ply film obtained after slitting the tubular one.
- the thermal capacity of the films according to the present invention is such that they rapidly attain the temperature of the environment particularly when heated by direct contact with a heat source, such as a heated plate or roller.
- the heat treatment temperature is defined as the temperature of the heated elements with which the films are contacted or the ambient temperature to which the films are exposed during the treatment.
- the films may be heated to the treatment temperature by conventional techniques, such as, by exposure of the film to radiant elements, by passage of the film through a heated air oven or an IR oven, or - preferably - by contact of the films with the surface of one or more heated plates or rollers.
- the heat treatment is carried out by first running the film over and in contact with the surface of 2 to 8, preferably 4 or 6, revolving rollers heated at the suitably selected temperature, and then over and in contact with the surface of 2 to 4 rollers cooled to a temperature below room temperature.
- rollers are typically disposed, as described in the attached Fig. 1, on two vertical rows, whereas rollers (1), (3), (5), and (7) are mounted on a support member (9) by means of supporting bars (11), (13), (15) and (17) and rollers (2),
- (4), (6), and (8) are mounted on a similar support member (10) by means of supporting bars (12), (14), (16) and (18). While support (10) is fixed, support member (9), and rollers (1), (3), (5), and (7) jointly thereto, can be moved along the axis (19) to approach support member (9). On each support member the distance between two subsequent rollers is larger than the rollers' diameter and the rollers mounted on one support member are shifted with respect to those mounted on the other support member so that by reducing the distance between the two support members the row of rollers (1), (3),
- rollers (2), (4), (6), and (8) can come closer, align, or even go beyond that of rollers (2), (4), (6), and (8).
- the film (20) is driven through this unit at a speed which generally corresponds to the speed of the production line. Lower speeds may be envisaged but economic considerations would discourage this possibility.
- the contact time of the film with the heating and cooling rollers and therefore the length of the heating time and that of the cooling time will depend on the rollers diameters, on the speed line, and on the distance between the two rollers' rows. As a matter of fact, for a given line speed and rollers' diameter, the closer the two rows the longer is clearly the contact time.
- rollers' dimensions can be widely varied in diameter while their length is determined by the width of the film which has to be subjected to the heat- treatment.
- the rollers' length will be larger than the film width.
- the rollers' diameter typically range from 10 to 100 cm, and generally is comprised between 10 and 40 cm.
- the rollers are typically made of stainless steel, but any material which is highly heat conductive and heat-resistant and which the thermoplastic material does not stick to could in theory be employed.
- the heating or cooling system may be provided e.g. by the use of internal spirals where a heated or cooled medium is circulated.
- the heating temperature should not be higher than about 100'C and is preferably comprised between about 70 and about 95 * C and even more preferably between about 72 and about 90' C.
- the period for which the film is maintained at the heating treatment temperature must be very short and in most of the cases it should not exceed 7.5 s.
- An extended period at the heat treatment temperature would in fact be detrimental to the film characteristics, unacceptably decreasing the free shrink of the film at 120 ' C.
- the minimum period of heat treatment of the film in order to achieve the desired results can be as low as 0.1 s, depending on the film thickness, specific composition and shrink properties of the starting film.
- a period of time of at least 0.5 and preferably at least 1 s and not more than 5, preferably not more than 3 s, is employed.
- the cooling step that immediately follows the heat treatment, is then carried out as quickly as possible.
- the temperature of the film needs to be brought to a value below room temperature in less than 2 s, preferably in less than 1 s. While the temperature of the cooling rollers could be as low as possible, using appropriate fluids with a freezing point below O'C, it is generally preferred, in order to avoid condensation on the roller, cooling the rollers to a temperature of between 1 and 25' C, preferably between 8 and 20 * C.
- the film generally does not need to be constrained against shrinkage.
- a tolerable reduction in the film width occurs, generally of not more than 15-20 %, which reflects in a slight thickening of the film.
- Films treated according to the present invention may then be subjected to conventional after treatments - for example exposure to a corona discharge treatment to improve the bonding and print-receptive characteristics of the film surface.
- Conventional after treatments for example exposure to a corona discharge treatment to improve the bonding and print-receptive characteristics of the film surface.
- the following examples are representative of the preferred embodiments of the present invention.
- % Free Shrink (or % unrestrained linear thermal shrinkage), i.e. the percent dimensional change in a 10 cm x 10 cm specimen of film when subjected to a selected heat, has been measured by the ASTM Standard Test Method D 2732 -
- Gloss i.e. the surface reflectance or shine of a film specimen has been evaluated by ASTM Standard Test Method D-2457 (with an angle of incidence of 60 ' ).
- Haze i.e. the percentage of transmitted light which is scattered forward while passing through the film specimen has been measured by the ASTM Standard Test Method D-1003 (Method A).
- the transversal shrink force i.e. the force per original unit width developed by a film in the transverse direction at a specified temperature in its attempt to shrink while under restraint
- a 25.4 mm wide and 140 mm long strip of film is cut from the sample in the transverse direction.
- the force measurement is made by a load cell on which a clamping jaw is connected.
- a second one on which the specimen is fixed can be adjusted in position by an external hand knob to pretension the specimen.
- the two jaws keep the specimen in the center of a channel into which an impeller blows heated air. In the air channels three thermocouples are fixed to measure the temperature.
- the temperature of the specimen as measured by the thermocouples, is increased at a rate of about 2'C/s up to about 180 ' C and the force is measured continuously.
- the measured force is then divided by the specimen original width to obtain the shrink force.
- the shrink force is expressed in N/cm.
- this five-ply film was A/B/C/B/A wherein A was a blend of 25 % EVA, 25 % LMDPE, and 50 % LLDPE containing slip, antiblock, and antifog agents, C was a blend of EVOH and a polyamide, and B was a modified LLDPE based adhesive.
- the overall thickness of the film was 25 ⁇ .
- the manufacturing process corresponded to that described in the above referred to Example and the shrink properties of the thus obtained film [maximum
- the heat treatment according to the present invention was carried out by passing the tubular flattened film thus obtained through a processing unit consisting of 6 stainless steel Gross Equatherm heated rollers and two cooled rollers, 16 cm in diameter and 203 cm in length, disposed as described in Fig. 1.
- the unit was divided into four zones, three heating and one cooling zone.
- the first heating zone comprised the first roller
- the second heating zone comprised the second and third roller
- the third heating zone comprised the fourth, fifth, and sixth roller.
- the temperature of the roller(s) in each zone was the same and the temperature values of the four zones were as reported in Table I below.
- the revolving speed of the rollers was the same as the line speed (55 m/min).
- rollers were disposed in such a way that the contact time of the film web with each roller was 0.26 s and the total heating time was therefore 1.56 s.
- HFFS Form and Seal
Abstract
Description
Claims
Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE69510373T DE69510373T2 (en) | 1994-12-16 | 1995-12-15 | HOT SHRINKABLE MULTILAYER FILM |
EP95943419A EP0797507B1 (en) | 1994-12-16 | 1995-12-15 | Multi-layer heat-shrinkable film |
BR9510093A BR9510093A (en) | 1994-12-16 | 1995-12-15 | Multilayer heat shrinkable film |
MX9704389A MX9704389A (en) | 1994-12-16 | 1995-12-15 | Multi-laser heat-shrinkable film. |
NZ298960A NZ298960A (en) | 1994-12-16 | 1995-12-15 | A multi-layered heat-shrinkable film |
CA002207718A CA2207718C (en) | 1994-12-16 | 1995-12-15 | Multi-layer heat-shrinkable film |
AU44692/96A AU706626C (en) | 1994-12-16 | 1995-12-15 | Multi-laser heat-shrinkable film |
JP8519242A JPH10512506A (en) | 1994-12-16 | 1995-12-15 | Multilayer heat shrinkable film |
FI972512A FI972512A (en) | 1994-12-16 | 1997-06-13 | Multilayer heat-shrinkable film |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/357,487 US6150011A (en) | 1994-12-16 | 1994-12-16 | Multi-layer heat-shrinkage film with reduced shrink force, process for the manufacture thereof and packages comprising it |
US357,487 | 1994-12-16 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1996018501A1 true WO1996018501A1 (en) | 1996-06-20 |
Family
ID=23405826
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1995/016202 WO1996018501A1 (en) | 1994-12-16 | 1995-12-15 | Multi-laser heat-shrinkable film |
Country Status (17)
Country | Link |
---|---|
US (1) | US6150011A (en) |
EP (1) | EP0797507B1 (en) |
JP (1) | JPH10512506A (en) |
CN (1) | CN1190367A (en) |
AT (1) | ATE181282T1 (en) |
BR (1) | BR9510093A (en) |
CA (1) | CA2207718C (en) |
DE (1) | DE69510373T2 (en) |
ES (1) | ES2133844T3 (en) |
FI (1) | FI972512A (en) |
MX (1) | MX9704389A (en) |
MY (1) | MY131731A (en) |
NZ (1) | NZ298960A (en) |
RU (1) | RU2159186C2 (en) |
TW (1) | TW296997B (en) |
WO (1) | WO1996018501A1 (en) |
ZA (1) | ZA9510748B (en) |
Cited By (4)
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EP1135254A1 (en) * | 1998-11-06 | 2001-09-26 | Avery Dennison Corporation | Halogen-free, printable, multilayered shrink films and articles encapsulated therein |
US6808822B2 (en) | 2001-10-17 | 2004-10-26 | Avery Dennison Corporation | Multilayered shrink films and labels made therefrom |
WO2011029950A1 (en) * | 2009-09-14 | 2011-03-17 | Cryovac, Inc. | Gas barrier heat-shrinkable film |
EP1084035B2 (en) † | 1998-04-24 | 2014-06-25 | Kureha Corporation | Heat-shrinkable multilayer film |
Families Citing this family (26)
Publication number | Priority date | Publication date | Assignee | Title |
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US5744181A (en) * | 1995-03-01 | 1998-04-28 | W. R. Grace & Co.-Conn. | Packaging method using thermoplastic materials and package obtained thereby |
US6623821B1 (en) * | 1995-03-31 | 2003-09-23 | E. I. Du Pont De Nemours And Company | Heat-shrinkable, heat-sealable polyester film for packaging |
AUPP749398A0 (en) * | 1998-12-03 | 1999-01-07 | Sporos Sa | Multilayer heat shrinkable film |
US20040173932A1 (en) * | 2003-03-07 | 2004-09-09 | Douglas Michael J. | Methods of making multilayer structures |
US20040175592A1 (en) * | 2003-03-07 | 2004-09-09 | Douglas Michael J. | Thermoplastic multilayer barrier structures |
US20040175464A1 (en) | 2003-03-07 | 2004-09-09 | Blemberg Robert J. | Multilayer structures, packages, and methods of making multilayer structures |
US20040175465A1 (en) * | 2003-03-07 | 2004-09-09 | Buelow Duane H. | Thermoplastic multilayer structures |
US20040173944A1 (en) * | 2003-03-07 | 2004-09-09 | Mueller Chad D. | Methods of making multilayer barrier structures |
US20040175466A1 (en) * | 2003-03-07 | 2004-09-09 | Douglas Michael J. | Multilayer barrier structures, methods of making the same and packages made therefrom |
US20040175467A1 (en) * | 2003-03-07 | 2004-09-09 | Mueller Chad D. | Packages made from multilayer structures |
US20040173491A1 (en) * | 2003-03-07 | 2004-09-09 | Buelow Duane H. | Packages made from thermoplastic multilayer barrier structures |
US20040234797A1 (en) * | 2003-05-23 | 2004-11-25 | Cryovac, Inc. | Oxygen scavenging film with antifog properties |
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US20060099436A1 (en) * | 2004-11-05 | 2006-05-11 | Cryovac, Inc. | Reduced antifog level in oxygen scavenging film with antifog properties |
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FR2887801B1 (en) * | 2005-07-01 | 2007-09-07 | Bollore Sa | FILM WITH SEVERAL LAYERS |
CN101318577B (en) * | 2008-07-07 | 2011-08-17 | 苏州天加新材料有限公司 | Thermal contraction sheet film for bone and meat packaging |
PL2805821T6 (en) | 2013-05-21 | 2017-10-31 | Cryovac Inc | Gas-barrier heat-shrinkable film |
US20170198123A1 (en) * | 2014-05-28 | 2017-07-13 | Cryovac, Inc. | Multilayer Heat Shrinkable Films |
SG11201700905YA (en) * | 2014-08-06 | 2017-03-30 | Handy Technology Zhuhai Ltd | Self-heating insulating film and face mask and eye mask manufactured therefrom |
CN109195790B (en) | 2016-06-01 | 2021-07-23 | 克里奥瓦克公司 | Gas barrier heat shrinkable film |
US10633524B2 (en) | 2016-12-01 | 2020-04-28 | Cryovac, Llc | Multilayer heat shrinkable films |
CA3019433A1 (en) | 2017-10-02 | 2019-04-02 | Flexopack S.A. | Multilayer cling film |
JP7061930B2 (en) * | 2018-06-01 | 2022-05-02 | 株式会社クレハ | Heat shrinkable multilayer film |
CN113453897A (en) * | 2019-02-25 | 2021-09-28 | 克里奥瓦克公司 | Abrasion resistant heat shrinkable multilayer film |
CN111572998B (en) * | 2020-05-22 | 2022-01-04 | 温州市恒生包装有限公司 | Multidirectional crack arrest pyrocondensation membrane |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0087080A1 (en) * | 1982-02-19 | 1983-08-31 | Kureha Kagaku Kogyo Kabushiki Kaisha | Laminate film |
US4457960A (en) * | 1982-04-26 | 1984-07-03 | American Can Company | Polymeric and film structure for use in shrink bags |
EP0141555A1 (en) * | 1983-10-14 | 1985-05-15 | American Can Company | Oriented polymeric films, packaging made from such films and methods of making the films and packaging |
EP0217596A2 (en) * | 1985-09-17 | 1987-04-08 | W.R. Grace & Co.-Conn. | Oxygen barrier oriented film |
WO1994023945A1 (en) * | 1993-04-09 | 1994-10-27 | Viskase Corporation | Evoh oxygen barrier stretched multilayer film |
Family Cites Families (31)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA849081A (en) * | 1967-03-02 | 1970-08-11 | Du Pont Of Canada Limited | PRODUCTION OF ETHYLENE/.alpha.-OLEFIN COPOLYMERS OF IMPROVED PHYSICAL PROPERTIES |
US3595735A (en) * | 1968-05-06 | 1971-07-27 | Nat Distillers Chem Corp | Blown tubular films |
US3741253A (en) * | 1971-03-30 | 1973-06-26 | Grace W R & Co | Laminates of ethylene vinyl acetate polymers and polymers of vinylidene chloride |
US4064296A (en) * | 1975-10-02 | 1977-12-20 | W. R. Grace & Co. | Heat shrinkable multi-layer film of hydrolyzed ethylene vinyl acetate and a cross-linked olefin polymer |
BG24190A1 (en) * | 1976-09-08 | 1978-01-10 | Antonov | Method of synthesis of speech and device for effecting same |
JPS5382888A (en) * | 1976-12-29 | 1978-07-21 | Kureha Chem Ind Co Ltd | Co-extruded five-layered drawn cylindrical film and its manufacture |
JPS5391890A (en) * | 1977-01-24 | 1978-08-12 | Kureha Chemical Ind Co Ltd | Method of producing skin package |
US4284458A (en) * | 1977-07-25 | 1981-08-18 | W. R. Grace & Co. | Method for producing laminated film |
US4302566A (en) * | 1978-03-31 | 1981-11-24 | Union Carbide Corporation | Preparation of ethylene copolymers in fluid bed reactor |
US4302565A (en) * | 1978-03-31 | 1981-11-24 | Union Carbide Corporation | Impregnated polymerization catalyst, process for preparing, and use for ethylene copolymerization |
US4194039A (en) * | 1978-04-17 | 1980-03-18 | W. R. Grace & Co. | Multi-layer polyolefin shrink film |
US4188443A (en) * | 1978-08-30 | 1980-02-12 | W. R. Grace & Co. | Multi-layer polyester/polyolefin shrink film |
DE2838062C2 (en) * | 1978-08-31 | 1983-01-20 | Siemens AG, 1000 Berlin und 8000 München | Arrangement with parallel-connected DC converters |
US4399180A (en) * | 1978-09-15 | 1983-08-16 | Mobil Oil Corporation | Coextruded thermoplastic stretch-wrap |
US4352849A (en) * | 1981-03-26 | 1982-10-05 | W. R. Grace & Co. | Coextruded, heat-shrinkable, multi-layer, polyolefin packaging film |
US4399173A (en) * | 1982-01-04 | 1983-08-16 | Union Carbide Corporation | Multilayer films comprising low pressure, low density polyethylene |
US4532189A (en) * | 1982-02-19 | 1985-07-30 | W. R. Grace & Co., Cryovac Div. | Linear polyethylene shrink films |
US4590124A (en) * | 1984-05-10 | 1986-05-20 | W. R. Grace & Co., Cryovac Div. | Storm window film |
US4551380A (en) * | 1984-05-10 | 1985-11-05 | W. R. Grace & Co., Cryovac Div. | Oriented heat-sealable multilayer packaging film |
US4514465A (en) * | 1984-05-30 | 1985-04-30 | W. R. Grace & Co., Cryovac Div. | Storm window film comprising at least five layers |
US4726984A (en) * | 1985-06-28 | 1988-02-23 | W. R. Grace & Co. | Oxygen barrier oriented film |
CA1308012C (en) * | 1986-01-17 | 1992-09-29 | Robert Wayne Thies | Multilayered polyolefin high shrinkage, low-shrink force shrink film |
US4755419A (en) * | 1986-03-21 | 1988-07-05 | W. R. Grace & Co., Cryovac Div. | Oxygen barrier oriented shrink film |
US5004647A (en) * | 1986-03-21 | 1991-04-02 | W. R. Grace & Co.-Conn. | Oxygen barrier biaxially oriented film |
US4839235A (en) * | 1986-06-30 | 1989-06-13 | W. R. Grace & Co. | Oxygen barrier film |
US4833024A (en) * | 1987-04-03 | 1989-05-23 | W. R. Grace & Co. | Low shrink energy films |
US4837084A (en) * | 1987-07-02 | 1989-06-06 | W. R. Grace & Co.-Conn. | Thermoplastic multi-layer packaging film and bags made therefrom |
US5023143A (en) * | 1989-03-14 | 1991-06-11 | W. R. Grace & Co.-Conn. | Low shrink force shrink film |
US5272236A (en) * | 1991-10-15 | 1993-12-21 | The Dow Chemical Company | Elastic substantially linear olefin polymers |
US5278272A (en) * | 1991-10-15 | 1994-01-11 | The Dow Chemical Company | Elastic substantialy linear olefin polymers |
ES2096949T3 (en) * | 1992-10-02 | 1997-03-16 | Du Pont | IMPROVED RETRACTILE FILM AND PROCEDURES RELATED TO IT. |
-
1994
- 1994-12-16 US US08/357,487 patent/US6150011A/en not_active Expired - Lifetime
-
1995
- 1995-12-15 AT AT95943419T patent/ATE181282T1/en active
- 1995-12-15 MX MX9704389A patent/MX9704389A/en unknown
- 1995-12-15 CA CA002207718A patent/CA2207718C/en not_active Expired - Fee Related
- 1995-12-15 NZ NZ298960A patent/NZ298960A/en not_active IP Right Cessation
- 1995-12-15 WO PCT/US1995/016202 patent/WO1996018501A1/en not_active Application Discontinuation
- 1995-12-15 BR BR9510093A patent/BR9510093A/en not_active IP Right Cessation
- 1995-12-15 DE DE69510373T patent/DE69510373T2/en not_active Expired - Lifetime
- 1995-12-15 JP JP8519242A patent/JPH10512506A/en active Pending
- 1995-12-15 EP EP95943419A patent/EP0797507B1/en not_active Expired - Lifetime
- 1995-12-15 RU RU97113757/04A patent/RU2159186C2/en active
- 1995-12-15 CN CN95197566A patent/CN1190367A/en active Pending
- 1995-12-15 ES ES95943419T patent/ES2133844T3/en not_active Expired - Lifetime
- 1995-12-16 MY MYPI95003907A patent/MY131731A/en unknown
- 1995-12-18 ZA ZA9510748A patent/ZA9510748B/en unknown
- 1995-12-27 TW TW084113931A patent/TW296997B/zh active
-
1997
- 1997-06-13 FI FI972512A patent/FI972512A/en unknown
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0087080A1 (en) * | 1982-02-19 | 1983-08-31 | Kureha Kagaku Kogyo Kabushiki Kaisha | Laminate film |
US4457960A (en) * | 1982-04-26 | 1984-07-03 | American Can Company | Polymeric and film structure for use in shrink bags |
EP0141555A1 (en) * | 1983-10-14 | 1985-05-15 | American Can Company | Oriented polymeric films, packaging made from such films and methods of making the films and packaging |
EP0217596A2 (en) * | 1985-09-17 | 1987-04-08 | W.R. Grace & Co.-Conn. | Oxygen barrier oriented film |
WO1994023945A1 (en) * | 1993-04-09 | 1994-10-27 | Viskase Corporation | Evoh oxygen barrier stretched multilayer film |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1084035B2 (en) † | 1998-04-24 | 2014-06-25 | Kureha Corporation | Heat-shrinkable multilayer film |
EP1135254A1 (en) * | 1998-11-06 | 2001-09-26 | Avery Dennison Corporation | Halogen-free, printable, multilayered shrink films and articles encapsulated therein |
EP1135254A4 (en) * | 1998-11-06 | 2003-04-09 | Avery Dennison Corp | Halogen-free, printable, multilayered shrink films and articles encapsulated therein |
US6808822B2 (en) | 2001-10-17 | 2004-10-26 | Avery Dennison Corporation | Multilayered shrink films and labels made therefrom |
WO2011029950A1 (en) * | 2009-09-14 | 2011-03-17 | Cryovac, Inc. | Gas barrier heat-shrinkable film |
Also Published As
Publication number | Publication date |
---|---|
ATE181282T1 (en) | 1999-07-15 |
ES2133844T3 (en) | 1999-09-16 |
CA2207718C (en) | 2003-10-21 |
NZ298960A (en) | 1999-11-29 |
MX9704389A (en) | 1997-10-31 |
EP0797507B1 (en) | 1999-06-16 |
TW296997B (en) | 1997-02-01 |
AU706626B2 (en) | 1999-06-17 |
DE69510373D1 (en) | 1999-07-22 |
FI972512A0 (en) | 1997-06-13 |
AU4469296A (en) | 1996-07-03 |
ZA9510748B (en) | 1996-08-27 |
MY131731A (en) | 2007-08-30 |
US6150011A (en) | 2000-11-21 |
DE69510373T2 (en) | 2000-02-10 |
FI972512A (en) | 1997-08-13 |
EP0797507A1 (en) | 1997-10-01 |
CN1190367A (en) | 1998-08-12 |
JPH10512506A (en) | 1998-12-02 |
BR9510093A (en) | 1998-07-14 |
RU2159186C2 (en) | 2000-11-20 |
CA2207718A1 (en) | 1996-06-20 |
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