WO1993001052A1 - Improved extrudable and primerless ahdesives and products therefrom - Google Patents

Improved extrudable and primerless ahdesives and products therefrom Download PDF

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Publication number
WO1993001052A1
WO1993001052A1 PCT/US1991/004495 US9104495W WO9301052A1 WO 1993001052 A1 WO1993001052 A1 WO 1993001052A1 US 9104495 W US9104495 W US 9104495W WO 9301052 A1 WO9301052 A1 WO 9301052A1
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Prior art keywords
copolymer
composition
comonomer
ethylene
percent
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PCT/US1991/004495
Other languages
French (fr)
Inventor
I-Hwa Lee
Original Assignee
E.I. Du Pont De Nemours And Company
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Application filed by E.I. Du Pont De Nemours And Company filed Critical E.I. Du Pont De Nemours And Company
Priority to AU81846/91A priority Critical patent/AU661823B2/en
Priority to KR1019930704099A priority patent/KR0155962B1/en
Publication of WO1993001052A1 publication Critical patent/WO1993001052A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B7/00Layered 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
    • B32B7/04Interconnection of layers
    • B32B7/12Interconnection of layers using interposed adhesives or interposed materials with bonding properties
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J123/00Adhesives based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Adhesives based on derivatives of such polymers
    • C09J123/26Adhesives based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Adhesives based on derivatives of such polymers modified by chemical after-treatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B15/00Layered products comprising a layer of metal
    • B32B15/04Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B15/08Layered products comprising a layer of metal comprising metal 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
    • B32B15/09Layered products comprising a layer of metal comprising metal 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 comprising polyesters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/06Layered 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
    • B32B27/08Layered 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/30Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
    • B32B27/306Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers comprising vinyl acetate or vinyl alcohol (co)polymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/36Layered products comprising a layer of synthetic resin comprising polyesters
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J151/00Adhesives based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Adhesives based on derivatives of such polymers
    • C09J151/06Adhesives based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Adhesives based on derivatives of such polymers grafted on to homopolymers or copolymers of aliphatic hydrocarbons containing only one carbon-to-carbon double bond
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2329/00Polyvinylalcohols, polyvinylethers, polyvinylaldehydes, polyvinylketones or polyvinylketals
    • B32B2329/04Polyvinylalcohol
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2367/00Polyesters, e.g. PET, i.e. polyethylene terephthalate
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2666/00Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
    • C08L2666/02Organic macromolecular compounds, natural resins, waxes or and bituminous materials
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/31504Composite [nonstructural laminate]
    • Y10T428/31678Of metal
    • Y10T428/31692Next to addition polymer from unsaturated monomers
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/31504Composite [nonstructural laminate]
    • Y10T428/31855Of addition polymer from unsaturated monomers
    • Y10T428/31909Next to second addition polymer from unsaturated monomers
    • Y10T428/31913Monoolefin polymer
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/31504Composite [nonstructural laminate]
    • Y10T428/31855Of addition polymer from unsaturated monomers
    • Y10T428/31909Next to second addition polymer from unsaturated monomers
    • Y10T428/31928Ester, halide or nitrile of addition polymer
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/31504Composite [nonstructural laminate]
    • Y10T428/31855Of addition polymer from unsaturated monomers
    • Y10T428/31938Polymer of monoethylenically unsaturated hydrocarbon

Definitions

  • This invention relates to an extrudable adhesive composition of ethylene copolymer and tac ifying resin, useful for bonding structural polymers to barrier polymers.
  • Japanese Application 53 18653 discloses an adhesive resin for low temperature heat sealing purposes comprising 3 to 100 parts by weight of a hydrogenated petroleum resin, and 100 parts by weight of an ethylene carboxylate-vinyl acetate copolymer obtained by copolymerizing an unsaturated carboxylic acid and/or anhydride with at least one vinylidene monomer in the presence of an ethylene-vinyl acetate copolymer.
  • Japanese application 60 51768 discloses a hot melt adhesive composition of 100 parts by weight of polymer component, 25 to 200 parts by weight of tackifier resin, and 75 parts by weight or less of wax.
  • the polymer component comprises 25 to 75 weight % low crystallinity or amorphous ethylene alpha-olefin copolymer (20 to 50 mole % ethylene, 50 to 80 mole % alpha-olefin) and 25 to 75 weight % ethylene vinyl ester copolymer. Either polymer, or both, are modified with unsaturated carboxylic acid or its acid anhydride.
  • the tackifier resin is a terpene resin or petroleum resin.
  • the wax is a paraffin, microcrystalline polyethylene, etc.
  • the composition has a viscosity of 50 Pa.sec or less at 180 * c.
  • Japanese Application 01 27923 discloses a laminate in which a resin layer is coextrusion laminated onto an oriented film or Al foil.
  • the adhesive is made of 50 to 99 weight percent ethylene-alpha-olefin random copolymer partially graft-modified with acid, and 1 to 50 weight percent tackifier.
  • the ethylene-alpha-olefin copolymer has a density of 0.850 to 0.900 g/cc.
  • U.S. Patent 4,670,349 discloses an adhesive resin composition comprising 100 parts of an ethylene/vinyl acetate or ethylene/alpha-olefin random copolymer, 1-50 parts of modified polyethylene containing 0.01 to 10% grafted acid or derivative, and 1-125 parts hydrogenated aromatic petroleum resin.
  • the resin composition is useful as an adhesive for polystyrene and ethylene vinyl alcohol copolymer.
  • U.S. Patent 4,337,297 discloses blends of a low density ethylene polymer and a copolymer of 70-90 % ethylene with the balance acrylic or methacrylic acid or vinyl acetate, the two ethylene polymers comprising together 100 parts; an ionomer resin having an acid content of 1-10%, 2-100 parts; and optionally a tackifying resin, 0-150 parts.
  • the blend is a useful adhesive for PET film.
  • U.S. Patent 4,367,113, Kari et al. discloses a similar blend except the low density polymer is replaced by an ethylene-alpha olefin copolymer or isotactic propylene polymer.
  • U.S. Patent 4,358,557 discloses a hot-melt adhesive comprising ethylene vinyl acetate copolymer, a tackifier resin selected from hydrocarbon resin, polyterpene resin or rosin ester, a paraffin wax and an aromatic hydrocarbon resin.
  • U.S. Patent 4,861,676 discloses a blend of ethylene copolymer, ethylene copolymer modified by grafting with a comonomer containing pendant acid or acid derivative functionality, styrene polymer, and alicyclic resin modifier or stabilized rosin ester.
  • the composition provides a useful adhesive, particularly for bonding polystyrene to barrier polymers.
  • U.S. Patent 4,861,677 discloses a blend of ethylene vinyl acetate copolymer, ethylene vinyl acetate copolymer modified by grafting with a comonomer containing pendant acid or acid derivative functionality, and impact-modified polystyrene.
  • the composition provides a useful adhesive, particularly for bonding polystyrene to gas barrier polymers.
  • the present invention provides an extrudable bonding resin composition consisting essentially of: (a) about 65 to about 99 percent by weight of an ethylene copolymer portion consisting essentially of (i) about 1 to 100 percent by weight of a copolymer of about 50 to about 80 weight percent ethylene and 20 to about 50 weight percent of at least one comonomer copolymerized therewith selected from the group consisting of unsaturated mono- or dicarboxylic acids of 2-20 carbon atoms, esters or salts of said unsaturated mono- or dicarboxylic acids, vinyl esters of saturated carboxylic acids where the acid group has 1-18 carbon atoms, and carbon monoxide, the carbon monoxide being present in an amount of 0 to about 30 weight percent; having grafted thereon side chains at least one comonomer unit in length, the comonomer units in said side chains being selected from the group consisting of ethylenically unsaturated mono-, di-, or polycarbox
  • the invention further provides a multiple layer structure comprising at least one structural layer, at least one barrier layer, and at least one bonding layer of the above extrudable bonding resin composition.
  • the extrudable bonding resin of the present invention comprises a blend of about 65 to about 99 percent by weight, preferably about 80 to about 95 percent by weight, of an ethylene copolymer component, and about 1 to about 35 weight percent of a tackifying resin.
  • the ethylene copolymer component comprises an ethylene copolymer grafted with pendant acid or certain acid derivative functionality. This grafted copolymer may be blended, if desired, with additional ungrafted ethylene copolymer. Such blending may be desirable in order to minimize the amount of the relatively more expensive grafted material, while maintaining the excellent adhesive properties of the composition.
  • the grafted ethylene copolymer is present in amounts of about 1 to about 100, and preferably about 5 to about 50 percent by weight of the ethylene copolymer portion of the composition.
  • This component is a copolymer containing about 20 to about 50, and preferably about 25 to about 30 weight percent copolymerized comonomer selected from the group consisting of unsaturated mono- or dicarboxylic acids of 2-20 carbon atoms, esters or salts of said unsaturated mono- or dicarboxylic acids, vinyl esters of saturated carboxylic acids where the acid group has 1-18 carbon atoms, and carbon monoxide, the carbon monoxide being present in an amount of 0 to about 30 weight percent.
  • Vinyl acetate is a preferred comonomer, but methyl acrylate, n-butyl acrylate, and the like, optionally with carbon monoxide present as a third monomer, are also quite suitable.
  • the balance of the copolymer is substantially copolymerized ethylene.
  • Such copolymers are prepared by the well-known addition polymerization processes. Onto this copolymer are grafted additional comonomer units of carboxylic acid or certain carboxylic acid derivative functionality to form short sidechains.
  • melt index of the resulting graft copolymer should be about 0.5 to about 40. Outside of these ranges, processing becomes more difficult, and flow instabilities may result.
  • the grafting monomer is selected from the group consisting of ethylenically unsaturated mono-, di-, or polycarboxylic acids, ethylenically unsaturated carboxylic acid anhydrides, and metal salts and half-esters of such acids and anhydrides.
  • the acids and anhydrides include acrylic acid, ethacrylic acid, maleic acid, fumaric acid, itaconic acid, crotonic acid, itaconic anhydride, maleic anhydride, and dimethyl maleic anhydride, and salts and half-esters thereof.
  • acids and anhydrides that are particularly useful are maleic anhydride and maleic acid.
  • the method for grafting of the comonomer onto the ethylene copolymer can be any of the processes which are well known in the art.
  • grafting can be carried out in the melt without a solvent, as disclosed in European Patent Application 0 266 994, incorporated herein by reference, or in solution or dispersion.
  • Melt grafting can be done using a heated extruder, a BrabenderTM or BanburyTM mixer or other internal mixers or kneading machines, roll mills, and the like.
  • the grafting may be carried out in the presence of a radical initiator such as a suitable organic peroxide, organic perester, or organic hydroperoxide.
  • the graft copolymers are recovered by any method which separates or utilizes the graft polymer that is formed.
  • the graft copolymer can be recovered in the form of precipitated fluff, pellets, powders, and the like.
  • the amount of monomer grafted onto the ethylene copolymer is not particularly limiting, and may be as low as about 0.03 weight percent or as much as about 5 percent or even 10 percent, based on the weight of the grafted ethylene copolymer.
  • the total amount of graft polymer in the total adhesive composition is important, and should be between about 0.03 and about 10 weight percent of the total composition, in order to obtain superior adhesive and bonding properties.
  • the ungrafted ethylene copolymer component comprises at least one comonomer similar to that described above, but without the grafted comonomer.
  • the comonomer of the ungrafted copolymer should be of a type and amount sufficiently similar to that of the grafted copolymer that the grafted and ungrafted copolymers have a suitable degree of compatibility.
  • Such copolymers are normally compatible if they contain the same or closely chemically related monomers (except for the graft comonomer) and the amounts of such monomers in the two copolymers are similar.
  • the grafted copolymer and each of the ungrafted copolymers should contain at least one said copolymerized comonomer in common and the amount of each such common comonomer in the grafted copolymer and the ungrafted copolymer should be within about 10%, and preferably within about 5%, of each other.
  • the grafted copolymer is based on an ethylene polymer containing 30 weight % n-butyl acrylate
  • the ungrafted copolymer should contain between about 20 and about 40 weight percent n-butyl acrylate.
  • each copolymer should contain less than about 10% by weight of such comonomers that are not common to the other copolymer.
  • closely similar comonomers such as n-butyl acrylate and i-butyl acrylate could be interchanged while retaining compatibility.
  • the graft copolymer be the same as the ungrafted copolymer, except for the presence of the grafted monomers.
  • the melt index of the ungrafted copolymer should be about 0.05 to about 40.
  • the ungrafted copolymer component can be a single polymer or it can be more than one polymer, provided that the comonomer content of each such polymer is as described above, i.e., the polymers are mutually compatible. It has been sometimes found to be desirable that the ungrafted copolymer component be a mixture of two polymers having identical comonomer contents but having differing melt indices. For example, one copolymer can have a melt index of about 6 and a second can have a melt index of 25 or higher. The mixture of these polymers should have an overall melt index within the range of about 0.05 to about 40, as indicated. Use of such a mixture of copolymers provides ease in processability in, for example extrusion coating.
  • the second major component of the present invention is a tackifying resin, which is present at about 1 to about 35 weight percent, preferably about 5 to about 20 weight percent of the composition.
  • Suitable tackifying resins may be selected from the categories of:
  • tackifying resins will generally have a ring-and-ball softening temperature (ASTM E-2858T) of 0 to 150"C, preferably about 75 to about 140*C.
  • the tackifying resins employed in the present invention are well known products available from commercial sources. Rosin tackifiers are described in the Kirk Othmer Encyclopedia of Chemical Technology. Interscience Publishers, Second Edition, Volume 17, pages 475-509. They include naturally occurring rosins and chemically modified rosin derivatives obtained by hydrogenation, dehydrogenation, isomerization, and the like.
  • Rosin derivatives includes rosin esters and rosin acids. Rosin acids are typically derived from tall oil and can be mixtures of so called abietic types and primary types. Rosin esters are formed by esterifying rosin acid with a di-, tri-, or tetra-hydroxy alphatic alcohol such as ethylene glycol, propylene glycol, glycerine, or pentaerythritol.
  • the terpene resins are generally prepared by the polymerization of terpene hydrocarbons in the presence of Friedel-Crafts catalysts at moderately low temperatures. Petroleum resins, under which are classed aliphatic, alicyclic, and aromatic hydrocarbon resins, are described in the Kirk Oth er Encyclopedia of Chemical Technology.
  • Suitable aromatic resins can be prepared from polymerization of alpha methyl styrene, vinyl toluene, and/or indene monomers.
  • the adhesive resin may contain small amounts of other materials commonly used and known in the art, such as antioxidants, stabilizers, slip additives, and fillers.
  • the adhesive resin composition is prepared by blending the above described components by any suitable means, such as melt blending, extruding, etc. Further details are provided in the Examples which follow.
  • the composition of the present invention provides excellent adhesion to polyester and copolyester resins, vinyl chloride polymers, polycarbonates, polyethylenes, ethylene copolymers, iono ers, polystyrene, ethylene vinyl alcohol copolymer, polyamides, and the like. It also shows good adhesion to substrates such as aluminum foil.
  • the adhesive is particularly useful for extrusion or coextrusion laminating structural and barrier polymers on to substrates such as polyester film, including multiple layer structures comprising at least two structural layers and at least one barrier layer.
  • the structural layers may be of the same material or can be of different materials, e.g. one layer polyester and a second layer ionomer or acid copolymer.
  • the adhesive can be used without having to resort to use of a solvent-based primer to prepare the polymer film surface.
  • the resulting composite structures are useful in packaging and other applications. Examples
  • Adhesive blends for the Examples shown in Table 1 were prepared by dry blending the ingredients in a polyethylene bag and subsequently melt blending at 210 to 230*C in a 28 or 53 mm Werner & PfleidererTM twin screw extruder with a vacuum port. Each of the blends, listed in the Table, also contained about 0.10 weight percent IrganoxTM 1010 hindered polyphenol stabilizer (not separately reported in the Table) . For the extruded pellets, 0.3 weight percent KemamideTM 20 was also added.
  • the adhesive properties of the blends were evaluated by measuring the peel strength of laminates prepared using a sheet of the adhesive between two layers of PET film.
  • the layers of PET film were 12 micrometers (0.48 mils) thick; heat seal conditions were 210 ⁇ C, 0.8 seconds dwell time and 324 kPa (47 psig) applied pressure. Peel strength was measured by ASTM D 1876-72, modified in that the test was run at 305 mm/min, rather than 254 mm/min, and 3 to 6 duplicates of each sample were measured, rather than 10. The numbers are given as grams per 25 mm.
  • Comparative Examples Cl through C8 show poor peel strength because the acid polymer, which contains o% vinyl acetate comonomer, is used with a base resin containing 28% vinyl acetate. This is greater than the 10% difference in comonomer content between the ethylene polymer and its acid-modified ethylene polymer permitted in the present invention. In contrast, Examples 1 through 4 show good results because the difference in comonomer content between the acid polymer and the base resin is less than 10%.
  • P90 is Arkon P90, 100% hydrogenated Cg hydrocarbon resin, from Arakawa Chemical, having a Ring and Ball softening point ("R&B") of 90"C.
  • P115 is a similar material, R&B 115-C.
  • Comparative Examples C9 and CIO are to be compared with Example 5.
  • Comparative Example C9 a low peel number is observed because no acid polymer is employed.
  • Comparative Example CIO the comonomer difference between the acid polymer and base resin polymer is greater than 10%.
  • Comparative Example Cll which contains no tackifier resin, compares unfavorably to Example 16 which is identical in composition with the exception of the tackifier. Examples 15, 16, and 17 show that blends of otherwise identical or compatible copolymers of different melt indices can be used in place of a single copolymer.
  • Comparative Examples C12 and C15 show poor results because the acrylate comonomer at 10% and vinyl ester comonomer at 9% respectively fall below the range of the present invention, i.e., 15 to 40 weight percent.
  • Comparative Examples C13 and C14 give low peel numbers compared to Example 18 because the difference in comonomer content between acid-containing polymer and the base polymers is greater than 10%.
  • E/28VA' in the second column, is identical to the first E/28VA except that its melt index is 25 dg/min.
  • P125 is ArkonTM P125 100% hydrogenated Cg hydrocarbon resin, R&B 125° C.
  • P140 is a comparable material, R&B 140- C.
  • M115 is ArkonTM M115 85% hydrogenated Cg hydrocarbon resin, R&B 115°C.
  • M135 is a comparable material, R&B 135° C.
  • F-105 is FloralTM 105 65% hydrogenated rosin ester from Hercules, R&B 104° R3102 is RegalrezTM 3102, 30% hydrogenated hydrocarbon resin from Hercules
  • R6108, a comparable resin, is 60% hydrogenated, R&B 108° C.
  • R1126 is 100% hydrogenated, R&B 126° C.
  • the multiple layer structures were made by coextrusion coating a layer of ionomer (ethylene methacrylic acid copolymer containing 15% methacrylic acid moieties, melt index 10 dg/min, 22% neutralized with zinc ions) , 23 micrometers thick, and a layer of adhesive onto corona-treated PET film, 12 micrometers thick.
  • the adhesive blends were melted in a 63 mm extruder with barrel temperatures from 154 ⁇ C at the rear to 232"C at the front.
  • the ionomer resin was melted in a 114 mm extruder with barrel temperatures from 177*C in the rear to 232*C at the front. Both melt streams were fed into a 107 cm (42 inch) die set at 232 ' C.
  • the air gap was set at 16.5 centimeters. Line speed was 122 meters per minute.
  • Comparative Examples C17, C18, C22, C24 and C25 give poor results because the difference in vinyl ester comonomer content between the acid-containing polymer and the base polymer is greater than 10%. Comparative Example C19 compares unfavorably with Example 28 because it contains no tackifier. In Comparative Example C20, the acrylate comonomer content of the ethylene polymer is below 20 weight percent. Comparative Examples C21, C23 and C26 contain no acid polymers.
  • Example 5 the multiple layer structures of Examples 31 and 32 were made by coextrusion coating a layer of ionomer (as described for the Examples of Table 4) , adhesive, a layer of ethylene vinyl alcohol copolymer containing 44 ol % ethylene, melt index 16, and adhesive onto PET film as described for the Examples of Table 4.
  • the adhesive blends were melted in a 63 mm extruder with barrel temperatures from 154*C at the rear to 232*C at the front.
  • the ionomer resin was melted in a 114 mm extruder with barrel temperatures from 177*C in the rear to 232"C at the front.
  • the ethylene vinyl alcohol resin was melted in a 62.5 mm extruder with barrel temperatures from 177"C in the rear to 232*C at the front.
  • the melt streams were fed into a feedblock in which the adhesive stream was split into two.
  • the 1067 mm die was at 232*C.
  • the air gap was set at 16.5 centimeters. Line speed was 122 meters per minute. Good adhesive strength is achieved in the structure.
  • the multiple layer structures of Examples 33-39 were made with several different substrates.
  • the adhesive blends were melted in a 87.5 mm extruder with barrel temperatures from 180*C in the rear to 240 ⁇ C at the front.
  • the ionomer and acid copolymer resins were melted in a 62.5 mm extruder with a similar temperature profile.
  • the melt streams were were fed into a die with a slot width of 800 mm.
  • the die was set at 240*C.
  • the air gap was at 15 centimeters. Good bond strengths are obtained with different substrates.
  • the multiple layer structures of Examples 40-49 were prepared by coextrusion of an adhesive layer between a copolyester layer and an ethylene vinyl alcohol copolymer containing 30 mol% ethylene moieties.
  • the copolyester was a high melt viscosity copolyester of ethylene glycol copolymerized with about 86% terephthalic and about 14% isophthalic acid, further containing 0.4% comonomer moieties derived from trimellitic acid.
  • the adhesive blends were melted at 160*C in a 25 mm extruder at 4-6 rpm.
  • the copolyester was fed through a 37.5 mm extruder at 30-45 rpm at 240*C.
  • the extrudate was cast onto chill rolls maintained at 60"C.
  • the takeup speed of the sheet was 1.5 m/min. Good bonding is achieved to copolyester and ethylene vinyl alcohol copolymer with these compositions.

Abstract

An extrudable bonding resin composition of (a) 65 to 99 percent of an ethylene copolymer portion of a copolymer of ethylene and 20 to 50 percent comonomer of acids, esters, and the like, and grafted sidechains of comonomer units selected from carboxylic acid, anhydride, salt, or half ester functionality, and optionally a compatible non-grafted ethylene copolymer, and (b) 1 to 35 percent by weight of a tackifying resin exhibits good adhesion properties without the need for a primer.

Description

TITLE IMPROVED EXTRUDABLE AND PRIMERLESS ADHESIVES AND PRODUCTS THEREFROM BACKGROUND OF THE INVENTION This invention relates to an extrudable adhesive composition of ethylene copolymer and tac ifying resin, useful for bonding structural polymers to barrier polymers.
Many attempts have been made to provide adhesive compositions which are particularly suitable for joining together layers of polymers, especially for joining structural polymers to polymers such as barrier resins. For example, Japanese Application 53 18653 discloses an adhesive resin for low temperature heat sealing purposes comprising 3 to 100 parts by weight of a hydrogenated petroleum resin, and 100 parts by weight of an ethylene carboxylate-vinyl acetate copolymer obtained by copolymerizing an unsaturated carboxylic acid and/or anhydride with at least one vinylidene monomer in the presence of an ethylene-vinyl acetate copolymer.
Japanese application 60 51768 discloses a hot melt adhesive composition of 100 parts by weight of polymer component, 25 to 200 parts by weight of tackifier resin, and 75 parts by weight or less of wax. The polymer component comprises 25 to 75 weight % low crystallinity or amorphous ethylene alpha-olefin copolymer (20 to 50 mole % ethylene, 50 to 80 mole % alpha-olefin) and 25 to 75 weight % ethylene vinyl ester copolymer. Either polymer, or both, are modified with unsaturated carboxylic acid or its acid anhydride. The tackifier resin is a terpene resin or petroleum resin. The wax is a paraffin, microcrystalline polyethylene, etc. The composition has a viscosity of 50 Pa.sec or less at 180*c. Japanese Application 01 27923 discloses a laminate in which a resin layer is coextrusion laminated onto an oriented film or Al foil. The adhesive is made of 50 to 99 weight percent ethylene-alpha-olefin random copolymer partially graft-modified with acid, and 1 to 50 weight percent tackifier. The ethylene-alpha-olefin copolymer has a density of 0.850 to 0.900 g/cc.
U.S. Patent 4,670,349 discloses an adhesive resin composition comprising 100 parts of an ethylene/vinyl acetate or ethylene/alpha-olefin random copolymer, 1-50 parts of modified polyethylene containing 0.01 to 10% grafted acid or derivative, and 1-125 parts hydrogenated aromatic petroleum resin. The resin composition is useful as an adhesive for polystyrene and ethylene vinyl alcohol copolymer.
U.S. Patent 4,337,297 discloses blends of a low density ethylene polymer and a copolymer of 70-90 % ethylene with the balance acrylic or methacrylic acid or vinyl acetate, the two ethylene polymers comprising together 100 parts; an ionomer resin having an acid content of 1-10%, 2-100 parts; and optionally a tackifying resin, 0-150 parts. The blend is a useful adhesive for PET film. U.S. Patent 4,367,113, Kari et al. discloses a similar blend except the low density polymer is replaced by an ethylene-alpha olefin copolymer or isotactic propylene polymer.
U.S. Patent 4,358,557 discloses a hot-melt adhesive comprising ethylene vinyl acetate copolymer, a tackifier resin selected from hydrocarbon resin, polyterpene resin or rosin ester, a paraffin wax and an aromatic hydrocarbon resin.
U.S. Patent 4,861,676 discloses a blend of ethylene copolymer, ethylene copolymer modified by grafting with a comonomer containing pendant acid or acid derivative functionality, styrene polymer, and alicyclic resin modifier or stabilized rosin ester. The composition provides a useful adhesive, particularly for bonding polystyrene to barrier polymers.
U.S. Patent 4,861,677 discloses a blend of ethylene vinyl acetate copolymer, ethylene vinyl acetate copolymer modified by grafting with a comonomer containing pendant acid or acid derivative functionality, and impact-modified polystyrene. The composition provides a useful adhesive, particularly for bonding polystyrene to gas barrier polymers.
SUMMARY OF THE INVENTION The present invention provides an extrudable bonding resin composition consisting essentially of: (a) about 65 to about 99 percent by weight of an ethylene copolymer portion consisting essentially of (i) about 1 to 100 percent by weight of a copolymer of about 50 to about 80 weight percent ethylene and 20 to about 50 weight percent of at least one comonomer copolymerized therewith selected from the group consisting of unsaturated mono- or dicarboxylic acids of 2-20 carbon atoms, esters or salts of said unsaturated mono- or dicarboxylic acids, vinyl esters of saturated carboxylic acids where the acid group has 1-18 carbon atoms, and carbon monoxide, the carbon monoxide being present in an amount of 0 to about 30 weight percent; having grafted thereon side chains at least one comonomer unit in length, the comonomer units in said side chains being selected from the group consisting of ethylenically unsaturated mono-, di-, or polycarboxylic acids, ethylenically unsaturated carboxylic acid anhydrides, metal salts and half-esters of such acids and anhydrides, and mixtures thereof, wherein the amount of said grafted comonomer units comprises about 0.03 to about 10 percent by weight of the total bonding resin composition, and
(ii) 0 to about 99 percent by weight of at least one copolymer of about 50 to about 80 weight percent ethylene and 20 to about 50 weight percent of at least one comonomer copolymerized therewith selected from the group consisting of unsaturated mono- or dicarboxylic acids of 2-20 carbon atoms, esters or salts of said unsaturated mono- or dicarboxylic acids, vinyl esters of saturated carboxylic acids where the acid group has 1-18 carbon atoms, and carbon monoxide, the carbon monoxide being present in an amount of 0 to about 30 weight percent, wherein the copolymer of (i) and each copolymer of (ii) contain at least one said copolymerized comonomer in common, the amount of each such common comonomer in each copolymer of (ii) being within about 10% of the amount of the corresponding comonomer in copolymer (i) , and the total amount of said copolymerized comonomers other than such common comonomers in any such copolymer being less than about ιo%; and
(b) about 1 to about 35 percent by weight of a tackifying resin.
The invention further provides a multiple layer structure comprising at least one structural layer, at least one barrier layer, and at least one bonding layer of the above extrudable bonding resin composition.
DETAILED DESCRIPTION OF THE INVENTION The extrudable bonding resin of the present invention comprises a blend of about 65 to about 99 percent by weight, preferably about 80 to about 95 percent by weight, of an ethylene copolymer component, and about 1 to about 35 weight percent of a tackifying resin. The ethylene copolymer component comprises an ethylene copolymer grafted with pendant acid or certain acid derivative functionality. This grafted copolymer may be blended, if desired, with additional ungrafted ethylene copolymer. Such blending may be desirable in order to minimize the amount of the relatively more expensive grafted material, while maintaining the excellent adhesive properties of the composition.
The grafted ethylene copolymer is present in amounts of about 1 to about 100, and preferably about 5 to about 50 percent by weight of the ethylene copolymer portion of the composition. This component is a copolymer containing about 20 to about 50, and preferably about 25 to about 30 weight percent copolymerized comonomer selected from the group consisting of unsaturated mono- or dicarboxylic acids of 2-20 carbon atoms, esters or salts of said unsaturated mono- or dicarboxylic acids, vinyl esters of saturated carboxylic acids where the acid group has 1-18 carbon atoms, and carbon monoxide, the carbon monoxide being present in an amount of 0 to about 30 weight percent. (The amount of carbon monoxide is limited only because it is believed that preparation of polymers containing more than about 30 weight percent carbon monoxide is not feasible due to problems of reactor fouling.) Vinyl acetate is a preferred comonomer, but methyl acrylate, n-butyl acrylate, and the like, optionally with carbon monoxide present as a third monomer, are also quite suitable. The balance of the copolymer is substantially copolymerized ethylene. Such copolymers are prepared by the well-known addition polymerization processes. Onto this copolymer are grafted additional comonomer units of carboxylic acid or certain carboxylic acid derivative functionality to form short sidechains. (It is believed that when maleic anhydride is the graft comonomer, the sidechains are only one or at most two monomer units long.) The melt index of the resulting graft copolymer, as measured by ASTM D1238 Condition *E", should be about 0.5 to about 40. Outside of these ranges, processing becomes more difficult, and flow instabilities may result.
The grafting monomer is selected from the group consisting of ethylenically unsaturated mono-, di-, or polycarboxylic acids, ethylenically unsaturated carboxylic acid anhydrides, and metal salts and half-esters of such acids and anhydrides. Examples of the acids and anhydrides include acrylic acid, ethacrylic acid, maleic acid, fumaric acid, itaconic acid, crotonic acid, itaconic anhydride, maleic anhydride, and dimethyl maleic anhydride, and salts and half-esters thereof. Among the acids and anhydrides that are particularly useful are maleic anhydride and maleic acid.
The method for grafting of the comonomer onto the ethylene copolymer can be any of the processes which are well known in the art. For example, grafting can be carried out in the melt without a solvent, as disclosed in European Patent Application 0 266 994, incorporated herein by reference, or in solution or dispersion. Melt grafting can be done using a heated extruder, a Brabender™ or Banbury™ mixer or other internal mixers or kneading machines, roll mills, and the like. The grafting may be carried out in the presence of a radical initiator such as a suitable organic peroxide, organic perester, or organic hydroperoxide. The graft copolymers are recovered by any method which separates or utilizes the graft polymer that is formed. Thus the graft copolymer can be recovered in the form of precipitated fluff, pellets, powders, and the like.
The amount of monomer grafted onto the ethylene copolymer is not particularly limiting, and may be as low as about 0.03 weight percent or as much as about 5 percent or even 10 percent, based on the weight of the grafted ethylene copolymer. The total amount of graft polymer in the total adhesive composition, however, is important, and should be between about 0.03 and about 10 weight percent of the total composition, in order to obtain superior adhesive and bonding properties.
The ungrafted ethylene copolymer component comprises at least one comonomer similar to that described above, but without the grafted comonomer. in order to achieve good peel strength in laminates prepared from the present adhesive, the comonomer of the ungrafted copolymer should be of a type and amount sufficiently similar to that of the grafted copolymer that the grafted and ungrafted copolymers have a suitable degree of compatibility. Such copolymers are normally compatible if they contain the same or closely chemically related monomers (except for the graft comonomer) and the amounts of such monomers in the two copolymers are similar. Specifically, the grafted copolymer and each of the ungrafted copolymers (if there is more than one) should contain at least one said copolymerized comonomer in common and the amount of each such common comonomer in the grafted copolymer and the ungrafted copolymer should be within about 10%, and preferably within about 5%, of each other. Thus if the grafted copolymer is based on an ethylene polymer containing 30 weight % n-butyl acrylate, the ungrafted copolymer should contain between about 20 and about 40 weight percent n-butyl acrylate. Small amounts of additional comonomers may also be present in one or both copolymers, but in order to retain compatibility each copolymer should contain less than about 10% by weight of such comonomers that are not common to the other copolymer. Alternatively, closely similar comonomers, such as n-butyl acrylate and i-butyl acrylate could be interchanged while retaining compatibility. It is preferred that the graft copolymer be the same as the ungrafted copolymer, except for the presence of the grafted monomers. The melt index of the ungrafted copolymer should be about 0.05 to about 40.
The ungrafted copolymer component can be a single polymer or it can be more than one polymer, provided that the comonomer content of each such polymer is as described above, i.e., the polymers are mutually compatible. It has been sometimes found to be desirable that the ungrafted copolymer component be a mixture of two polymers having identical comonomer contents but having differing melt indices. For example, one copolymer can have a melt index of about 6 and a second can have a melt index of 25 or higher. The mixture of these polymers should have an overall melt index within the range of about 0.05 to about 40, as indicated. Use of such a mixture of copolymers provides ease in processability in, for example extrusion coating.
It is similarly to be understood that the use of more than one graft copolymer will fall within the scope of the present invention, provided that the general principles of polymeric compatibility set forth herein are maintained.
The second major component of the present invention is a tackifying resin, which is present at about 1 to about 35 weight percent, preferably about 5 to about 20 weight percent of the composition. Suitable tackifying resins may be selected from the categories of:
(i) alicyclic or aliphatic hydrocarbon resins;
(ii) aromatic hydrocarbon resins; (iii) rosin and rosin derivatives; and (iv) terpene resins, or mixtures thereof. These tackifying resins will generally have a ring-and-ball softening temperature (ASTM E-2858T) of 0 to 150"C, preferably about 75 to about 140*C. The tackifying resins employed in the present invention are well known products available from commercial sources. Rosin tackifiers are described in the Kirk Othmer Encyclopedia of Chemical Technology. Interscience Publishers, Second Edition, Volume 17, pages 475-509. They include naturally occurring rosins and chemically modified rosin derivatives obtained by hydrogenation, dehydrogenation, isomerization, and the like. Rosin derivatives includes rosin esters and rosin acids. Rosin acids are typically derived from tall oil and can be mixtures of so called abietic types and primary types. Rosin esters are formed by esterifying rosin acid with a di-, tri-, or tetra-hydroxy alphatic alcohol such as ethylene glycol, propylene glycol, glycerine, or pentaerythritol. The terpene resins are generally prepared by the polymerization of terpene hydrocarbons in the presence of Friedel-Crafts catalysts at moderately low temperatures. Petroleum resins, under which are classed aliphatic, alicyclic, and aromatic hydrocarbon resins, are described in the Kirk Oth er Encyclopedia of Chemical Technology. Interscience Publishers, Third Edition, Volume 12, page 852. They are generally prepared by polymerization of 4-10 carbon atom hydrocarbons by selected Friedel Crafts catalysts. Higher or lower hydrocarbons may also be present. The product may be further partially or fully hydrogenated. Suitable aromatic resins can be prepared from polymerization of alpha methyl styrene, vinyl toluene, and/or indene monomers.
In addition to the above mentioned components, the adhesive resin may contain small amounts of other materials commonly used and known in the art, such as antioxidants, stabilizers, slip additives, and fillers. The adhesive resin composition is prepared by blending the above described components by any suitable means, such as melt blending, extruding, etc. Further details are provided in the Examples which follow.
The composition of the present invention provides excellent adhesion to polyester and copolyester resins, vinyl chloride polymers, polycarbonates, polyethylenes, ethylene copolymers, iono ers, polystyrene, ethylene vinyl alcohol copolymer, polyamides, and the like. It also shows good adhesion to substrates such as aluminum foil. The adhesive is particularly useful for extrusion or coextrusion laminating structural and barrier polymers on to substrates such as polyester film, including multiple layer structures comprising at least two structural layers and at least one barrier layer. The structural layers may be of the same material or can be of different materials, e.g. one layer polyester and a second layer ionomer or acid copolymer. The adhesive can be used without having to resort to use of a solvent-based primer to prepare the polymer film surface. The resulting composite structures are useful in packaging and other applications. Examples
Adhesive blends for the Examples shown in Table 1 were prepared by dry blending the ingredients in a polyethylene bag and subsequently melt blending at 210 to 230*C in a 28 or 53 mm Werner & Pfleiderer™ twin screw extruder with a vacuum port. Each of the blends, listed in the Table, also contained about 0.10 weight percent Irganox™ 1010 hindered polyphenol stabilizer (not separately reported in the Table) . For the extruded pellets, 0.3 weight percent Kemamide™ 20 was also added.
The adhesive properties of the blends were evaluated by measuring the peel strength of laminates prepared using a sheet of the adhesive between two layers of PET film. The layers of PET film were 12 micrometers (0.48 mils) thick; heat seal conditions were 210βC, 0.8 seconds dwell time and 324 kPa (47 psig) applied pressure. Peel strength was measured by ASTM D 1876-72, modified in that the test was run at 305 mm/min, rather than 254 mm/min, and 3 to 6 duplicates of each sample were measured, rather than 10. The numbers are given as grams per 25 mm.
Comparative Examples Cl through C8 show poor peel strength because the acid polymer, which contains o% vinyl acetate comonomer, is used with a base resin containing 28% vinyl acetate. This is greater than the 10% difference in comonomer content between the ethylene polymer and its acid-modified ethylene polymer permitted in the present invention. In contrast, Examples 1 through 4 show good results because the difference in comonomer content between the acid polymer and the base resin is less than 10%.
TABLE I
Figure imgf000015_0002
weight percent isobutyl acrylate and 10 weight percent methacrylic acid, melt index 10 dg/min, or a copolymer of ethylene with 28 weight percent vinyl acetate, grafted with 1.5 weight percent maleic anhydride, melt index 2.0 dg/min. c. P90 is Arkon P90, 100% hydrogenated Cg hydrocarbon resin, from Arakawa Chemical, having a Ring and Ball softening point ("R&B") of 90"C. P115 is a similar material, R&B 115-C.
Figure imgf000015_0001
The laminates in Table 2 were made in the same manner as in Table 1. Comparative Examples C9 and CIO are to be compared with Example 5. In Comparative Example C9, a low peel number is observed because no acid polymer is employed. In Comparative Example CIO, the comonomer difference between the acid polymer and base resin polymer is greater than 10%. Comparative Example Cll, which contains no tackifier resin, compares unfavorably to Example 16 which is identical in composition with the exception of the tackifier. Examples 15, 16, and 17 show that blends of otherwise identical or compatible copolymers of different melt indices can be used in place of a single copolymer.
The laminates in Table 3 were prepared in the same manner as described for the Examples in Table l. Comparative Examples C12 and C15 show poor results because the acrylate comonomer at 10% and vinyl ester comonomer at 9% respectively fall below the range of the present invention, i.e., 15 to 40 weight percent. Comparative Examples C13 and C14 give low peel numbers compared to Example 18 because the difference in comonomer content between acid-containing polymer and the base polymers is greater than 10%.
SUBSTITUTESHEET
Figure imgf000017_0001
Add t onal materials not dent f ed n Table I: E/28VA', in the second column, is identical to the first E/28VA except that its melt index is 25 dg/min. P125 is Arkon™ P125 100% hydrogenated Cg hydrocarbon resin, R&B 125° C. P140 is a comparable material, R&B 140- C.
M115 is Arkon™ M115 85% hydrogenated Cg hydrocarbon resin, R&B 115°C. M135 is a comparable material, R&B 135° C.
F-105 is Floral™ 105 65% hydrogenated rosin ester from Hercules, R&B 104° R3102 is Regalrez™ 3102, 30% hydrogenated hydrocarbon resin from Hercules
R&B 102βC. R6108, a comparable resin, is 60% hydrogenated, R&B 108° C.
R1126 is 100% hydrogenated, R&B 126° C.
Figure imgf000018_0001
E/9VA - ethylene/9% vinyl acetate copolymer, melt index 7
E/9VA-g-1.5MAn - ethylene/9% vinyl acetate copolymer, melt index 1.2, grafted with 1.5 weight percent maleic anhydride E/28VA' ' - ethylene/28% vinyl acetate copolymer, melt index 43 E/20MA - ethylene/20% methyl acrylate copolymer, melt index 2 E/20MA-g-1.5MAn - ethylene/20% methyl acrylate copolymer, melt index 3.6, grafted with 1.5 weight percent maleic anhydride E/21MA/4EHM - ethylene/21% methyl acrylate/4% ethyl hydrogen maleate terpoly er E/30nBA/10CO - ethylene/30% n-butyl acrylate/10% CO terpolymer, melt index 5 E/nBA/CO-g-MAn - ethylene/30% n-butyl acrylate/10% CO terpolymer, melt index 4.7, grafted with 0.3 weight percent maleic anhydride
In Table 4, the multiple layer structures were made by coextrusion coating a layer of ionomer (ethylene methacrylic acid copolymer containing 15% methacrylic acid moieties, melt index 10 dg/min, 22% neutralized with zinc ions) , 23 micrometers thick, and a layer of adhesive onto corona-treated PET film, 12 micrometers thick. The adhesive blends were melted in a 63 mm extruder with barrel temperatures from 154βC at the rear to 232"C at the front. The ionomer resin was melted in a 114 mm extruder with barrel temperatures from 177*C in the rear to 232*C at the front. Both melt streams were fed into a 107 cm (42 inch) die set at 232 ' C. The air gap was set at 16.5 centimeters. Line speed was 122 meters per minute.
Comparative Examples C17, C18, C22, C24 and C25 give poor results because the difference in vinyl ester comonomer content between the acid-containing polymer and the base polymer is greater than 10%. Comparative Example C19 compares unfavorably with Example 28 because it contains no tackifier. In Comparative Example C20, the acrylate comonomer content of the ethylene polymer is below 20 weight percent. Comparative Examples C21, C23 and C26 contain no acid polymers.
TABLE IV
High . i. Adhesive
E Copol.D Copol c Acid Copol Tackifier Thickness
Ex. _____* i_ Type % Type % urn
C17 46 46 E/15MAAa 8 (none) 18
C18 80 0 E/lOiBA/lOMAA 20 II 10.2
C19 90 0 E/28VA-g-1.5MAn 10 " 8
C20 0 0 E/lOiBA/lOMAA 100 " 9
C21 95 0 (none) 0 F-105 5 23
C22 75 0 E/lOiBA/lOMAA 20 P115 5 28
24 55 0 E/28VA-g-1.5MAn 40 R6108 5 20
25 60 15 " 20 " 5 20
26 40 15 " 30 P125 5 23
C23 80 15 (none) 0 R3102 5 18
C24 60 15 E/lOiBA/lOMAA 10 P90 15 15
C25 50 15 " 20 F-105 15 15
27 30 15 E/28VA-g-1.5MAn 40 P115 15 10
C26 85 0 (none) 0 R6108 15 18
C27 65 0 E/lOiBA/lOMAA 20 P90 15 10
28 55 0 E/28VA-g-1.5MAn 20 R3102 15 8
29 45 0 " 40 P125 15 10
30 45 0 » 40 " 15 8 a. Ethylene/15 wt.% methacrylic acid copolymer, melt i b. In each case the polymer was E/28VA, melt index 6. c. In each case the polymer was E/28VA, melt index 25. d. "Green" refers to peel testing conducted as soon as
"1 wk" and "4 wk" refer to peel testing conducted respectively after sample manufacture.
In Table 5, the multiple layer structures of Examples 31 and 32 were made by coextrusion coating a layer of ionomer (as described for the Examples of Table 4) , adhesive, a layer of ethylene vinyl alcohol copolymer containing 44 ol % ethylene, melt index 16, and adhesive onto PET film as described for the Examples of Table 4. The adhesive blends were melted in a 63 mm extruder with barrel temperatures from 154*C at the rear to 232*C at the front. The ionomer resin was melted in a 114 mm extruder with barrel temperatures from 177*C in the rear to 232"C at the front. The ethylene vinyl alcohol resin was melted in a 62.5 mm extruder with barrel temperatures from 177"C in the rear to 232*C at the front. The melt streams were fed into a feedblock in which the adhesive stream was split into two. The 1067 mm die was at 232*C. The air gap was set at 16.5 centimeters. Line speed was 122 meters per minute. Good adhesive strength is achieved in the structure.
The multiple layer structures of Examples 33-39 were made with several different substrates. The adhesive blends were melted in a 87.5 mm extruder with barrel temperatures from 180*C in the rear to 240βC at the front. The ionomer and acid copolymer resins were melted in a 62.5 mm extruder with a similar temperature profile. The melt streams were were fed into a die with a slot width of 800 mm. The die was set at 240*C. The air gap was at 15 centimeters. Good bond strengths are obtained with different substrates.
The multiple layer structures of Examples 40-49 were prepared by coextrusion of an adhesive layer between a copolyester layer and an ethylene vinyl alcohol copolymer containing 30 mol% ethylene moieties. The copolyester was a high melt viscosity copolyester of ethylene glycol copolymerized with about 86% terephthalic and about 14% isophthalic acid, further containing 0.4% comonomer moieties derived from trimellitic acid. The adhesive blends were melted at 160*C in a 25 mm extruder at 4-6 rpm. The copolyester was fed through a 37.5 mm extruder at 30-45 rpm at 240*C. The extrudate was cast onto chill rolls maintained at 60"C. The takeup speed of the sheet was 1.5 m/min. Good bonding is achieved to copolyester and ethylene vinyl alcohol copolymer with these compositions.
Figure imgf000023_0001
TABLE V
Ethylene High m.i. Adhesive % MAn Copol.a Copol.b c Tackifier Thickness in Peel Str.,g/25ram
Ex. % % Type % υm blend green 1 wk 6 wk Stucturee
31 65 0 R3102 15 7.6 0.3 583 674 PET/A/EV0H1/A/I0N 32 65 0 R6108 15 5.1 0.3 574 686 II 33 50 15 R3102 15 5 0.3 367 383 PET/A/I0N0MER2 34 50 15 II 15 10 0.3 567 633 II 35 50 15 15 5 0.3 450 483 36 50 15 15 10 0.3 717 783 37 50 15 R6108 15 25 0.3 d d PET/A/PET 38 50 15 R3102 15 5 0.3 d d PET/A/AC/Al foil 39 50 15 •I 15 10 0.3 d d II 40 50 15 P125 15 50 0.3 3230 P0LYESTER/A/EV0H2 41 45 0 II 15 65 0.6 3450 42 40 15 II 5 65 0.6 4722 43 50 15 R3102 15 70 0.3 4859 44 65 0 II 15 55 0.3 4812 45 30 15 II 15 55 0.6 4722 46 50 15 R3108 15 60 0.3 4812 47 60 15 II 5 60 0.3 1816 48 65 0 II 15 50 0.3 4903 49 55 0
Figure imgf000023_0002
II 15 55 0.6 5085 a E/28VA, mi 6 b~. E/28VA, mi 25 c. E/28VA-g-1.5MAnh, mi 2. d. Could not sepa e Multilayer structures as indicated, where A = adhesive layer (from this Table) ; PET = polyethylene terephthalate film, 12 micrometers, corona treated
I0N0MER1 = ethylene/15% methacrylic acid copolymer, 22% zinc neutralized, 25 micromet IONOMER2 = ethylene/8.7% methacrylic acid copolymer, 18% zinc neutralized, MI = 16, 2 AC = ethylene/9% acrylic acid copolymer, melt index 10, 25 micrometers Al foil = aluminum foil, 20 micrometers thick.
EV0H1 = ethylene vinyl alcohol copolymer, 44 mol % ethylene, MI = 16 8 micrometers EV0H2 = ethylene vinyl alcohol copolymer, 30 mol % ethylene, MI = 3, 80-120 micromete POLYESTER = copolymer of iso-, terephthalic, and trimellitic acids, 185-405 micromete

Claims

WHAT IS CLAIMED IS: 1. An extrudable bonding resin composition consisting essentially of:
(a) about 65 to about 99 percent by weight of an ethylene copolymer portion consisting essentially of
(i) about 1 to 100 percent by weight of a copolymer of about 50 to about 80 weight percent ethylene and 20 to about 50 weight percent of at least one comonomer copolymerized therewith selected from the group consisting of unsaturated mono- or dicarboxylic acids of 2-20 carbon atoms, esters or salts of said unsaturated mono- or dicarboxylic acids, vinyl esters of saturated carboxylic acids where the acid group has 1-18 carbon atoms, and carbon monoxide, the carbon monoxide being present in an amount of 0 to about 30 weight percent; having grafted thereon side chains at least one comonomer unit in length, the comonomer units in said side chains being selected from the group consisting of ethylenically unsaturated mono-, di-, or polycarboxylic acids, ethylenically unsaturated carboxylic acid anhydrides, metal salts and half-esters of such acids and anhydrides, and mixtures thereof, wherein the amount of said grafted comonomer units comprises about 0.03 to about 10 percent by weight of the total bonding resin composition, and
(ii) 0 to about 99 percent by weight of at least one copolymer of about 50 to about 80 weight percent ethylene and 20 to about 50 weight percent of at least one comonomer copolymerized therewith selected from the group consisting of unsaturated mono- or dicarboxylic acids of 2-20 carbon atoms, esters or salts of said unsaturated mono- or dicarboxylic acids, vinyl esters of saturated carboxylic acids where the acid group has 1-18 carbon atoms, and carbon monoxide, the carbon monoxide being present in an amount of 0 to about 30 weight percent, wherein the copolymer of (i) and each copolymer of (ii) contain at least one said copolymerized comonomer in common, the amount of each such common comonomer in each copolymer of (ii) being within about 10% of the amount of the corresponding comonomer in copolymer (i) , and the total amount of said copolymerized comonomers other than such common comonomers in any such copolymer being less than about 10%; and
(b) about 1 to about 35 percent by weight of a tackifying resin.
2. The composition of claim 1 wherein the ethylene copolymer portion consists essentially of about 5 to about 50 weight percent graft copolymer of (i) and about 50 to about 95 weight percent of at least one copolymer of (ii) .
3. The composition of claim 1 wherein the copolymer of (i) and each copolymer of (ii) contain the same copolymerized comonomers.
4. The composition of claim 3 wherein each comonomer in each copolymer of (ii) is within about 5 % of the amount of the corresponding comonomer in copolymer (i) .
5. The composition of claim 1 wherein the amount of ethylene copolymer portion is about 80 to about 95 weight percent and amount of the tackifying resin is about 5 to about 20 weight percent.
6. The composition of claim 1 wherein the amount of each copolymerized comonomer in each of the copolymers of (i) and copolymer of (ii) is about 25 to about 30 percent by weight.
7. The composition of claim 1 wherein the copolymer of (i) exclusive of the grafted comonomer units and each copolymer of (ii) are selected from the group consisting of ethylene vinyl acetate copolymer, ethylene methyl acrylate copolymer, ethylene n-butyl acrylate copolymer, and ethylene n-butyl acrylate carbon monoxide copolymer.
8. The composition of claim 7 wherein the copolymer of (i) exclusive of the grafted comonomer units and each copolymer of (ii) are ethylene vinyl acetate copolymer.
9. The composition of claim 1 wherein the at least one copolymer of (ii) is a single copolymer.
10. The composition of claim 1 wherein the at least one copolymer of (ii) comprises two copolymers which differ in melt index.
11. The composition of claim 1 wherein the grafted comonomer units are grafted onto polymer (i) in an amount of about 0.05 to about 5 weight percent of polymer (i) .
12. The composition of claim 11 wherein the grafted comonomer units are ethylenically unsaturated mono, di, or polycarboxylic acids, anhydrides, or salts.
13. The composition of claim 12 wherein the grafted comonomer units are acrylic acid, methacrylic acid, maleic acid, fumaric acid, itaconic acid, crotonic acid, itaconic anhydride, maleic anhydride, dimethyl maleic anhydride monosodium maleate, disodium maleate, diethyl fumarate, maleic anhydride or maleic acid.
14. The composition of claim 12 wherein the grafted comonomer units are anhydride units.
15. The composition of claim 14 wherein the anhydride is maleic anhydride.
16. The composition of claim 1 wherein the tackifying resin has a ring and ball softening point of about 0 to about 150*C and is at least one of the resins selected from the group consisting of: (i) alicyclic or aliphatic hydrocarbon resins;
(ii) aromatic hydrocarbon resins;
(iii) rosin and rosin derivatives; and
(iv) terpene resins.
17. The composition of claim 16 wherein the tackifying resin has a ring and ball softening point of about 75 to about 140"C.
18. The composition of claim 16 wherein the tackifying resin is a partially or fully hydrogenated hydrocarbon resin having a ring and ball softening temperature of about 100 to about 140"C.
19. The composition of claim 18 wherein the tackifying resin is an alicyclic resin prepared from monomers selected from the group consisting of alpha methyl styrene, vinyl toluene, and indene.
20. The composition of claim 16 wherein the tackifying resin is a partially hydrogentated alicyclic, aliphatic, or aromatic hydrocarbon resin.
21. A multiple layer structure comprising at least one structural layer, at least one barrier layer, and at least one bonding layer of an extrudable bonding resin composition consisting essentially of
(a) about 65 to about 99 percent by weight of an ethylene copolymer portion consisting essentially of
(i) about 1 to 100 percent by weight of a copolymer of about 50 to about 80 weight percent ethylene and about 20 to about 50 weight percent of at least one comonomer copolymerized therewith selected from the group consisting of unsaturated mono- or dicarboxylic acids of 2-20 carbon atoms, esters or salts of said unsaturated mono- or dicarboxylic acids, vinyl esters of saturated carboxylic acids where the acid group has 1-18 carbon atoms, and carbon monoxide, the carbon monoxide being present in an amount of 0 to about 30 weight percent; and grafted comonomer units of pendant ethylenically unsaturated mono-, di-, or polycarboxylic acids, ethylenically unsaturated carboxylic acid anhydrides, or metal salts or half-esters of such acids or anhydrides, wherein the amount of said grafted comonomer units comprises about 0.03 to about 10 percent by weight of the total bonding resin composition, and
(ii) 0 to about 99 percent by weight of at least one copolymer of about 50 to about 80 weight percent ethylene and about 20 to about 50 weight percent of at least one comonomer copolymerized therewith selected from the group consisting of unsaturated mono- or dicarboxylic acids of 2-20 carbon atoms, esters or salts of said unsaturated mono- or dicarboxylic acids, vinyl esters of saturated carboxylic acids where the acid group has 1-18 carbon atoms, and carbon monoxide, the carbon monoxide being present in an amount of 0 to about 30 weight percent, wherein the copolymer of (i) and each copolymer of (ii) contain at least one said copolymerized comonomer in common, the amount of each such common comonomer in each copolymer of (ii) being within about 10% of the amount of the corresponding comonomer in copolymer (i) , and the total amount of said copolymerized comonomers other than such common comonomers in any such copolymer being less than about 10%; and
(b) about 1 to about 35 percent by weight of a tackifying resin.
22. The multiple layer structure of claim 21 wherein the structural layer is polyester and the barrier layer is ethylene vinyl alcohol copolymer.
23. The multiple layer structure of claim 21 wherein the structural layer is is polyester and the barrier layer is aluminum.
24. The multiple layer structure of claim 21 comprising at least two structural layers.
25. The multiple layer structure of claim 24 wherein one structural layer is prepared from ionomer resin and one structural layer is prepared from polyester.
26. The multiple layer structure of claim 24 wherein one structural layer is prepared from acid copolymer and one structural layer is prepared from polyester.
PCT/US1991/004495 1990-06-25 1991-07-01 Improved extrudable and primerless ahdesives and products therefrom WO1993001052A1 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4342605A1 (en) * 1993-12-14 1995-06-22 Buna Gmbh Functionalized olefin homo- and copolymers
US6996740B2 (en) 2001-05-28 2006-02-07 Samsung Electronics Co., Ltd. Method of optimizing design parameters of data storage system and method of applying optimized design parameters
DE102007043972A1 (en) 2007-09-11 2009-05-20 Kometra Kunststoff-Modifikatoren Und -Additiv Gmbh Process for the preparation of carboxylated ethylene polymer blends

Families Citing this family (41)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3192731B2 (en) * 1992-03-04 2001-07-30 三井・デュポンポリケミカル株式会社 Resin composition and adhesive using the same
ES2111740T3 (en) * 1992-03-13 1998-03-16 Allied Signal Inc THERMO-FUSE ADHESIVE COMPOSITIONS INCLUDING LOW MOLECULAR WEIGHT ETHYLENE COPOLYMERS.
US5382615A (en) * 1993-10-01 1995-01-17 Eastman Chemical Company Modified polyethylene based hot-melt adhesives for use in packaging
DE4344438C2 (en) * 1993-12-24 1997-07-03 Renker Gmbh Barrier layer
CH686309A5 (en) * 1994-03-24 1996-02-29 Alusuisse Lonza Services Ag Polymer-containing mixture.
JPH11503766A (en) * 1994-03-31 1999-03-30 イー・アイ・デュポン・ドゥ・ヌムール・アンド・カンパニー Extrudable adhesive compositions and related methods
US5461110A (en) * 1994-05-04 1995-10-24 Du Pont Canada Inc. Cross-linkable adhesive polymers
US6127032A (en) * 1997-12-24 2000-10-03 The Dow Chemical Company Adhesive film for glass substrates
EP1198346B1 (en) 1999-07-23 2005-09-14 E.I. Du Pont De Nemours And Company Ethylene acid copolymer with enhanced adhesion
US6302321B1 (en) 1999-10-11 2001-10-16 Sonoco Development, Inc. Sealant layer for container lid
US7323239B2 (en) * 2001-10-22 2008-01-29 Exxonmobil Chemical Patents Inc. Protective films
ATE434645T1 (en) * 2002-03-28 2009-07-15 Arizona Chem RESINATES FROM MONOMER FATTY ACIDS
KR101186271B1 (en) 2002-06-26 2012-09-27 애버리 데니슨 코포레이션 Oriented films comprising polypropylene/olefin elastomer blends
ATE391151T1 (en) * 2002-10-09 2008-04-15 Exxonmobil Chem Patents Inc HEAT SEALABLE RESIN COMPOSITIONS AND USE THEREOF
DE10251333A1 (en) 2002-11-05 2004-05-19 Ticona Gmbh Composite including polyacetal and polyolefin shaped parts useful for preparation of structural parts contacting fuels, especially fuel-feed units, valves, tanks, or tank filler caps, gear wheels, guide rollers, drive parts
US7503820B2 (en) * 2004-10-05 2009-03-17 Wah Kan Cheung Multi-layered sports board
US7935401B2 (en) * 2005-10-27 2011-05-03 Cryovac, Inc. Shrink sleeve label
US20070172614A1 (en) * 2005-12-30 2007-07-26 I-Hwa Lee Heat shrinkable multilayer film and tube with improved adhesion after orientation
US7767760B2 (en) * 2005-12-30 2010-08-03 E.I. Du Pont De Nemours And Company Hot melt adhesive composition
WO2007146986A1 (en) 2006-06-14 2007-12-21 Avery Dennison Corporation Conformable and die-cuttable machine direction oriented labelstocks and labels, and process for preparing
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US8114491B2 (en) * 2007-02-15 2012-02-14 Cryovac, Inc. Shrink sleeve label
EP2206760B1 (en) * 2007-10-31 2012-12-19 Du Pont-Mitsui Polychemicals Co., Ltd. Pressure-sensitive adhesive film or sheet
JP4726989B2 (en) * 2008-02-20 2011-07-20 ユニチカ株式会社 Resin composition, laminate using the same, and molded article using the laminate
WO2012149391A1 (en) 2011-04-28 2012-11-01 Adherent Laboratories, Inc. Polyolefin based hot melt adhesive composition
ES2585129T3 (en) * 2011-11-22 2019-11-21 Danapak Flexibles As A sheet, a manufacturing process and use of a sheet as a lid for packaging
US9676532B2 (en) 2012-08-15 2017-06-13 Avery Dennison Corporation Packaging reclosure label for high alcohol content products
US8865824B2 (en) 2012-09-19 2014-10-21 IFS Industries Inc. Hot melt adhesive
US9241843B2 (en) 2012-09-19 2016-01-26 The Procter & Gamble Company Article with tackifier-free adhesive
US10639210B2 (en) 2013-12-19 2020-05-05 The Procter & Gamble Company Article with tackifier-free adhesive
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US20180264787A1 (en) 2014-10-03 2018-09-20 E I Du Pont De Nemours And Company Multilayer food casing or food film
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WO2019126129A1 (en) 2017-12-22 2019-06-27 E. I. Du Pont De Nemours And Company Thermoplastic adhesive composition
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EP3591019A1 (en) 2018-07-02 2020-01-08 E. I. du Pont de Nemours and Company Universal thermoplastic adhesives for multilayer films
EP3590705A1 (en) 2018-07-02 2020-01-08 E. I. du Pont de Nemours and Company Multilayer films incorporating universal thermoplastic adhesives
KR102291059B1 (en) * 2019-03-18 2021-08-20 효성화학 주식회사 Tube comprising polyketone and polyolefin
WO2020190018A1 (en) * 2019-03-18 2020-09-24 효성화학 주식회사 Multi-layered tube comprising polyketone and polyolefin

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS603098A (en) * 1983-06-20 1985-01-09 株式会社日立製作所 Voltage-current conversion circuit

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS603098B2 (en) * 1976-08-04 1985-01-25 東ソー株式会社 Resin composition with excellent low-temperature heat sealability
US4337298A (en) * 1980-11-19 1982-06-29 Gulf Oil Corporation Polymer compositions and laminates produced by bonding or coextrusion
US4367113A (en) * 1981-06-29 1983-01-04 Gulf Oil Corporation Multicomponent polymer compositions
ATE16476T1 (en) * 1982-02-12 1985-11-15 Hoffmann La Roche PANTHENOL DERIVATIVES.
US4358557A (en) * 1982-03-08 1982-11-09 Eastman Kodak Company Four component hot-melt adhesives
DE3306202A1 (en) * 1983-02-23 1984-08-23 Bayer Ag, 5090 Leverkusen USE OF GRAFTED ETHYLENE VINYL ACETATE COPOLYMERS FOR THE PRODUCTION OF MELT ADHESIVES
JPS60247557A (en) * 1984-05-09 1985-12-07 株式会社クラレ Laminate and manufacture thereof
US4861677A (en) * 1988-06-03 1989-08-29 E. I. Du Pont De Nemours And Company Coextrudable adhesive for polystyrene, and products therefrom
US4861676A (en) * 1988-08-29 1989-08-29 E. I. Du Pont De Nemours And Company Improved coextrudable adhesive and products therefrom

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS603098A (en) * 1983-06-20 1985-01-09 株式会社日立製作所 Voltage-current conversion circuit

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
ANONYMOUS RESEARCH DISCLOSURE, May 1990, page 436. *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4342605A1 (en) * 1993-12-14 1995-06-22 Buna Gmbh Functionalized olefin homo- and copolymers
US6996740B2 (en) 2001-05-28 2006-02-07 Samsung Electronics Co., Ltd. Method of optimizing design parameters of data storage system and method of applying optimized design parameters
DE102007043972A1 (en) 2007-09-11 2009-05-20 Kometra Kunststoff-Modifikatoren Und -Additiv Gmbh Process for the preparation of carboxylated ethylene polymer blends
US8742016B2 (en) 2007-09-11 2014-06-03 Dow Global Technologies Llc Method for producing carboxylated ethylene polymer blends

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AU661823B2 (en) 1995-08-10
CA2045273C (en) 2002-07-09
ZA914880B (en) 1993-02-24
KR0155962B1 (en) 1998-11-16
EP0463841A1 (en) 1992-01-02
US5217812A (en) 1993-06-08
MX171093B (en) 1993-09-29
CA2045273A1 (en) 1991-12-26
AU8184691A (en) 1993-02-11
ATE121439T1 (en) 1995-05-15
KR940701338A (en) 1994-05-28
DE69108992T2 (en) 1995-11-16
NZ238657A (en) 1994-08-26
DE69108992D1 (en) 1995-05-24

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