CA2169067C - Gaskets made from homogeneous linear olefin polymers - Google Patents
Gaskets made from homogeneous linear olefin polymers Download PDFInfo
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- CA2169067C CA2169067C CA002169067A CA2169067A CA2169067C CA 2169067 C CA2169067 C CA 2169067C CA 002169067 A CA002169067 A CA 002169067A CA 2169067 A CA2169067 A CA 2169067A CA 2169067 C CA2169067 C CA 2169067C
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- Prior art keywords
- gasket
- homogeneous linear
- ethylene polymer
- linear ethylene
- ethylene
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- Expired - Lifetime
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- 229920000098 polyolefin Polymers 0.000 title description 17
- 229920000573 polyethylene Polymers 0.000 claims abstract description 45
- 235000013361 beverage Nutrition 0.000 claims abstract description 4
- 239000005977 Ethylene Substances 0.000 claims description 30
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 27
- -1 polyethylene terephthalate Polymers 0.000 claims description 20
- 239000000654 additive Substances 0.000 claims description 12
- 229920001577 copolymer Polymers 0.000 claims description 10
- 238000009826 distribution Methods 0.000 claims description 10
- 238000002844 melting Methods 0.000 claims description 9
- 230000008018 melting Effects 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 9
- 239000000155 melt Substances 0.000 claims description 8
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 claims description 6
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 claims description 6
- 239000004743 Polypropylene Substances 0.000 claims description 6
- 229920001155 polypropylene Polymers 0.000 claims description 6
- 229920001169 thermoplastic Polymers 0.000 claims description 6
- 229920001903 high density polyethylene Polymers 0.000 claims description 4
- 239000004700 high-density polyethylene Substances 0.000 claims description 4
- 229920001519 homopolymer Polymers 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 239000000758 substrate Substances 0.000 claims description 4
- 239000011521 glass Substances 0.000 claims description 3
- 229920000092 linear low density polyethylene Polymers 0.000 claims description 3
- 239000004707 linear low-density polyethylene Substances 0.000 claims description 3
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims description 3
- 239000004716 Ethylene/acrylic acid copolymer Substances 0.000 claims description 2
- 239000003963 antioxidant agent Substances 0.000 claims description 2
- 239000003054 catalyst Substances 0.000 claims description 2
- 238000000113 differential scanning calorimetry Methods 0.000 claims description 2
- 229920001684 low density polyethylene Polymers 0.000 claims description 2
- 239000004702 low-density polyethylene Substances 0.000 claims description 2
- 239000000049 pigment Substances 0.000 claims description 2
- 239000005020 polyethylene terephthalate Substances 0.000 claims description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 claims description 2
- 230000000996 additive effect Effects 0.000 claims 1
- 230000000717 retained effect Effects 0.000 claims 1
- 238000007789 sealing Methods 0.000 abstract description 4
- 229920000642 polymer Polymers 0.000 description 32
- 239000004698 Polyethylene Substances 0.000 description 11
- 239000000178 monomer Substances 0.000 description 11
- 239000000463 material Substances 0.000 description 9
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 6
- 239000003921 oil Substances 0.000 description 5
- 229920003023 plastic Polymers 0.000 description 5
- 239000004033 plastic Substances 0.000 description 5
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 4
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 description 4
- QQONPFPTGQHPMA-UHFFFAOYSA-N Propene Chemical compound CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 4
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 4
- HGCIXCUEYOPUTN-UHFFFAOYSA-N cyclohexene Chemical compound C1CCC=CC1 HGCIXCUEYOPUTN-UHFFFAOYSA-N 0.000 description 4
- LPIQUOYDBNQMRZ-UHFFFAOYSA-N cyclopentene Chemical compound C1CC=CC1 LPIQUOYDBNQMRZ-UHFFFAOYSA-N 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000004416 thermosoftening plastic Substances 0.000 description 4
- PBKONEOXTCPAFI-UHFFFAOYSA-N 1,2,4-trichlorobenzene Chemical group ClC1=CC=C(Cl)C(Cl)=C1 PBKONEOXTCPAFI-UHFFFAOYSA-N 0.000 description 3
- 150000001993 dienes Chemical class 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- 238000005227 gel permeation chromatography Methods 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- PRBHEGAFLDMLAL-GQCTYLIASA-N (4e)-hexa-1,4-diene Chemical class C\C=C\CC=C PRBHEGAFLDMLAL-GQCTYLIASA-N 0.000 description 2
- OOVQLEHBRDIXDZ-UHFFFAOYSA-N 7-ethenylbicyclo[4.2.0]octa-1,3,5-triene Chemical class C1=CC=C2C(C=C)CC2=C1 OOVQLEHBRDIXDZ-UHFFFAOYSA-N 0.000 description 2
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- OWYWGLHRNBIFJP-UHFFFAOYSA-N Ipazine Chemical compound CCN(CC)C1=NC(Cl)=NC(NC(C)C)=N1 OWYWGLHRNBIFJP-UHFFFAOYSA-N 0.000 description 2
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical group CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 2
- 229920002367 Polyisobutene Polymers 0.000 description 2
- 239000004793 Polystyrene Substances 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- URYYVOIYTNXXBN-UPHRSURJSA-N cyclooctene Chemical compound C1CCC\C=C/CC1 URYYVOIYTNXXBN-UPHRSURJSA-N 0.000 description 2
- 239000004913 cyclooctene Substances 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 238000010828 elution Methods 0.000 description 2
- 239000012632 extractable Substances 0.000 description 2
- 238000013023 gasketing Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- RGSFGYAAUTVSQA-UHFFFAOYSA-N pentamethylene Natural products C1CCCC1 RGSFGYAAUTVSQA-UHFFFAOYSA-N 0.000 description 2
- 150000004291 polyenes Chemical class 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 229920002223 polystyrene Polymers 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 150000003440 styrenes Chemical class 0.000 description 2
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical class FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 1
- UAUDZVJPLUQNMU-UHFFFAOYSA-N Erucasaeureamid Natural products CCCCCCCCC=CCCCCCCCCCCCC(N)=O UAUDZVJPLUQNMU-UHFFFAOYSA-N 0.000 description 1
- 239000002998 adhesive polymer Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 235000013334 alcoholic beverage Nutrition 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- UBAZGMLMVVQSCD-UHFFFAOYSA-N carbon dioxide;molecular oxygen Chemical compound O=O.O=C=O UBAZGMLMVVQSCD-UHFFFAOYSA-N 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 235000013409 condiments Nutrition 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000007799 cork Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- GYZLOYUZLJXAJU-UHFFFAOYSA-N diglycidyl ether Chemical compound C1OC1COCC1CO1 GYZLOYUZLJXAJU-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 229920001198 elastomeric copolymer Polymers 0.000 description 1
- UAUDZVJPLUQNMU-KTKRTIGZSA-N erucamide Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCC(N)=O UAUDZVJPLUQNMU-KTKRTIGZSA-N 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000005357 flat glass Substances 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 1
- 239000012943 hotmelt Substances 0.000 description 1
- 229920004889 linear high-density polyethylene Polymers 0.000 description 1
- 238000002074 melt spinning Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000009928 pasteurization Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- AQSJGOWTSHOLKH-UHFFFAOYSA-N phosphite(3-) Chemical class [O-]P([O-])[O-] AQSJGOWTSHOLKH-UHFFFAOYSA-N 0.000 description 1
- 235000013824 polyphenols Nutrition 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 229910001868 water Inorganic materials 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 238000004078 waterproofing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K3/00—Materials not provided for elsewhere
- C09K3/10—Materials in mouldable or extrudable form for sealing or packing joints or covers
-
- 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
- B65D53/00—Sealing or packing elements; Sealings formed by liquid or plastics material
- B65D53/06—Sealings formed by liquid or plastic material
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/08—Copolymers of ethene
- C08L23/0807—Copolymers of ethene with unsaturated hydrocarbons only containing four or more carbon atoms
- C08L23/0815—Copolymers of ethene with unsaturated hydrocarbons only containing four or more carbon atoms with aliphatic 1-olefins containing one carbon-to-carbon double bond
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/04—Homopolymers or copolymers of ethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/08—Copolymers of ethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/08—Copolymers of ethene
- C08L23/0846—Copolymers of ethene with unsaturated hydrocarbons containing atoms other than carbon or hydrogen
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/08—Copolymers of ethene
- C08L23/0846—Copolymers of ethene with unsaturated hydrocarbons containing atoms other than carbon or hydrogen
- C08L23/0869—Copolymers of ethene with unsaturated hydrocarbons containing atoms other than carbon or hydrogen with unsaturated acids, e.g. [meth]acrylic acid; with unsaturated esters, e.g. [meth]acrylic acid esters
- C08L23/0876—Salts thereof, i.e. ionomers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2314/00—Polymer mixtures characterised by way of preparation
- C08L2314/06—Metallocene or single site catalysts
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2200/00—Chemical nature of materials in mouldable or extrudable form for sealing or packing joints or covers
- C09K2200/04—Non-macromolecular organic compounds
- C09K2200/0458—Nitrogen-containing compounds
- C09K2200/047—Amides, imides, imines, N-oxides
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2200/00—Chemical nature of materials in mouldable or extrudable form for sealing or packing joints or covers
- C09K2200/06—Macromolecular organic compounds, e.g. prepolymers
- C09K2200/0615—Macromolecular organic compounds, e.g. prepolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C09K2200/0617—Polyalkenes
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2200/00—Chemical nature of materials in mouldable or extrudable form for sealing or packing joints or covers
- C09K2200/06—Macromolecular organic compounds, e.g. prepolymers
- C09K2200/0615—Macromolecular organic compounds, e.g. prepolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C09K2200/0617—Polyalkenes
- C09K2200/062—Polyethylene
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2200/00—Chemical nature of materials in mouldable or extrudable form for sealing or packing joints or covers
- C09K2200/06—Macromolecular organic compounds, e.g. prepolymers
- C09K2200/0615—Macromolecular organic compounds, e.g. prepolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C09K2200/0625—Polyacrylic esters or derivatives thereof
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Medicinal Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Polymers & Plastics (AREA)
- Mechanical Engineering (AREA)
- Sealing Material Composition (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Gaskets comprising at least one homogeneous linear ethylene polymer are disclosed. The gaskets are particularly useful for sealing beverage containers and do not contribute to taste and/or odor of the packag ed product, which is especially useful in food-stuff applications.
Description
GASKETS MADE FROM HOMOGENEOUS
LINEAR OLEFIN POLYMERS
This invention relates to gaskets made from homogeneous linear olefin polymers. The gaskets are capable of compression sealing various containers, without contaminating the contents. Liquid containers particularly benefit from the use of the novel gasketing materials disclosed herein.
Gaskets have been made from a variety of structural materials, including polymers such as ethylene/vinyl acetate (EVA) and polyvinyl chloride (PVC). For example, USP 4,984,703 (Burzynski) discloses plastic closures which have a sealing liner comprising a blend of ethylene/vinyl acetate and a thermoplastic elastomeric composition.
Depending on the use environment, gaskets can have varying degrees of properties. For example, in corrosive service conditions, the gasket must be impervious to the material in question, but still resilient enough to form a seal. Gaskets used in the food and beverage area have similar requirements, but cannot contaminate the foodstuff. Furthermore, depending upon the type of food and/or liquid contents, the filling temperature might be lower or higher than room temperature, thus placing greater demands on the gasket.
Various attempts to solve these challenges usually involve the use of oil additives or elastomer additives.
For example, USP 5,137,164 (Bayer) discloses a method of lining a plastic closure to with a thermoplastic. The thermoplastic is a non-cross linked curable, vinyl chloride copolymer composition which has been plasticized with an epoxidized oil, an organic diglycidyl ether and a curing agent for the ether.
USP 4,807,772 (Schloss) and USP 4,846,362 (Schloss) disclose polypropylene and polyethylene closures, respectively, each having removable liners made from a blend of polyethylene and a thermoplastic, elastomeric copolymer (such as a block copolymer of styrene and butadiene). The blends are said to generally include 20-50 weight percent oil.
Polyethylene also has been disclosed as useful for forming gasket liners, but has not been commercially successful to date, because the polymer is too "hard" and because by adding oil to reduce the hardness, the extractables increase, thus negating regulatory requirements for food contact. In addition, linear low polyethylene does not adhere well to polypropylene (which is often used as a closure material, as described in USP 4,807,772) resulting in a loose polyethylene gasket.
While there have been many different solutions to the problems of gasketing materials, especially those involving cap liners, most of these incorporated additives.
We have now discovered homogeneous linear ethylene polymers useful in making gasket materials, without expensive additives and, in the case of foodstuff, without adversely contributing to the taste and/or odor of the product.
According to a broad aspect of the present invention, there is provided a gasket comprising at least one homogeneous linear ethylene polymer having an absence of long chain branching, wherein the at least one homogeneous linear ethylene polymer is selected from a group consisting of a homopolymer of ethylene, an interpolymer of ethylene with at least one C3-C2o a-olefin and a copolymer of ethylene with a C3-C2o a-olefin, and the homogeneous linear ethylene polymer has a composition distribution breadth index greater than 50 percent.
Gaskets comprising at least one homogeneous linear olefin polymer have now been discovered to have these often conflicting attributes. The homogeneous linear olefin polymers have an unusual combination of properties, making them especially useful for gasket materials. Preferably, the homogeneous linear olefin polymer is an ethylene polymer.
Gaskets comprising homogeneous linear ethylene polymers are especially preferred. A complete olefinic system (such as a gasket comprising the homogeneous linear ethylene polymer and a cap comprising a polypropylene polymer) can also be recycled together. Potential uses of the recycled polymers include melt spinning biconstituent fiber, as described in USP 5,133,917 (Jezic et al.).
The term "linear olefin polymers" used herein means that the olefin polymer does not have long chain branching. That is, the linear olefin polymer has an absence of long chain branching, as for example the traditional linear low density polyethylene polymers or linear high density polyethylene polymers made using Ziegler polymerization processes (for example, USP 4,076,698 (Anderson et al.)), sometimes called heterogeneous polymers.
The term "linear olefin polymers" does not refer to high pressure branched polyethylene, -2a-ethylene/vinyl acetate copolymers, or ethylene/vinyl alcohol copolymers which are known to those skilled in the art to have numerous long chain branches. The term "linear olefin polymers"
also refers to polymers made using uniform branching distribution polymerization processes, sometimes called homogeneous polymers.
Such uniformly branched or homogeneous polymers include those made as described in USP 3,645,992 (Elston), and those made using so-called single site catalysts in a batch reactor having relatively high olefin. concentrations (as described in U.S. Patent 5,026,798 (Canich) or in U.S. Patent 5,055,438 (Canich). The uniformly branched/homogeneous polymers are those polymers in which the comonomer is randomly distributed within a given interpolymer molecule and wherein substantially all of the interpolymer molecules have the same ethylene/comonomer ratio within that interpolymer, but these polymers too have an absence of long chain branching, as, for example, Exxon Chemical has taught in their February 1992 Tappi Journal paper.
The traditional homogeneous linear polymers have only a single melting point, as opposed to traditional Ziegler polymerized heterogeneous linear ethylene/a-olefin copolymers which have two or more melting points (determined using differential scanning calorimetry (DSC)).
The SCBDI (Short Chain Branch Distribution Index) or CDBI-(Composition Distribution Branch Index) is defined as the weight percent of the polymer molecules having a comonomer content within 50 percent of the median total molar comonomer content. The CDBI of a polymer is readily calculated from data obtained from techniques known in the art, such as, for example, temperature rising elution fractionation (abbreviated herein as "TREF") as described, for example, in Wild et al, ournal of Polymer Science, P_ olv. Phvs. Ed., Vol.
20, p. 441 (1982), or as described in U.S. Patent 4,798,081. The SCBDI or CDBI for the homogeneous linear olefin polymers of the present invention is preferably greater than about 30 percent, especially greater than about 50 percent.
LINEAR OLEFIN POLYMERS
This invention relates to gaskets made from homogeneous linear olefin polymers. The gaskets are capable of compression sealing various containers, without contaminating the contents. Liquid containers particularly benefit from the use of the novel gasketing materials disclosed herein.
Gaskets have been made from a variety of structural materials, including polymers such as ethylene/vinyl acetate (EVA) and polyvinyl chloride (PVC). For example, USP 4,984,703 (Burzynski) discloses plastic closures which have a sealing liner comprising a blend of ethylene/vinyl acetate and a thermoplastic elastomeric composition.
Depending on the use environment, gaskets can have varying degrees of properties. For example, in corrosive service conditions, the gasket must be impervious to the material in question, but still resilient enough to form a seal. Gaskets used in the food and beverage area have similar requirements, but cannot contaminate the foodstuff. Furthermore, depending upon the type of food and/or liquid contents, the filling temperature might be lower or higher than room temperature, thus placing greater demands on the gasket.
Various attempts to solve these challenges usually involve the use of oil additives or elastomer additives.
For example, USP 5,137,164 (Bayer) discloses a method of lining a plastic closure to with a thermoplastic. The thermoplastic is a non-cross linked curable, vinyl chloride copolymer composition which has been plasticized with an epoxidized oil, an organic diglycidyl ether and a curing agent for the ether.
USP 4,807,772 (Schloss) and USP 4,846,362 (Schloss) disclose polypropylene and polyethylene closures, respectively, each having removable liners made from a blend of polyethylene and a thermoplastic, elastomeric copolymer (such as a block copolymer of styrene and butadiene). The blends are said to generally include 20-50 weight percent oil.
Polyethylene also has been disclosed as useful for forming gasket liners, but has not been commercially successful to date, because the polymer is too "hard" and because by adding oil to reduce the hardness, the extractables increase, thus negating regulatory requirements for food contact. In addition, linear low polyethylene does not adhere well to polypropylene (which is often used as a closure material, as described in USP 4,807,772) resulting in a loose polyethylene gasket.
While there have been many different solutions to the problems of gasketing materials, especially those involving cap liners, most of these incorporated additives.
We have now discovered homogeneous linear ethylene polymers useful in making gasket materials, without expensive additives and, in the case of foodstuff, without adversely contributing to the taste and/or odor of the product.
According to a broad aspect of the present invention, there is provided a gasket comprising at least one homogeneous linear ethylene polymer having an absence of long chain branching, wherein the at least one homogeneous linear ethylene polymer is selected from a group consisting of a homopolymer of ethylene, an interpolymer of ethylene with at least one C3-C2o a-olefin and a copolymer of ethylene with a C3-C2o a-olefin, and the homogeneous linear ethylene polymer has a composition distribution breadth index greater than 50 percent.
Gaskets comprising at least one homogeneous linear olefin polymer have now been discovered to have these often conflicting attributes. The homogeneous linear olefin polymers have an unusual combination of properties, making them especially useful for gasket materials. Preferably, the homogeneous linear olefin polymer is an ethylene polymer.
Gaskets comprising homogeneous linear ethylene polymers are especially preferred. A complete olefinic system (such as a gasket comprising the homogeneous linear ethylene polymer and a cap comprising a polypropylene polymer) can also be recycled together. Potential uses of the recycled polymers include melt spinning biconstituent fiber, as described in USP 5,133,917 (Jezic et al.).
The term "linear olefin polymers" used herein means that the olefin polymer does not have long chain branching. That is, the linear olefin polymer has an absence of long chain branching, as for example the traditional linear low density polyethylene polymers or linear high density polyethylene polymers made using Ziegler polymerization processes (for example, USP 4,076,698 (Anderson et al.)), sometimes called heterogeneous polymers.
The term "linear olefin polymers" does not refer to high pressure branched polyethylene, -2a-ethylene/vinyl acetate copolymers, or ethylene/vinyl alcohol copolymers which are known to those skilled in the art to have numerous long chain branches. The term "linear olefin polymers"
also refers to polymers made using uniform branching distribution polymerization processes, sometimes called homogeneous polymers.
Such uniformly branched or homogeneous polymers include those made as described in USP 3,645,992 (Elston), and those made using so-called single site catalysts in a batch reactor having relatively high olefin. concentrations (as described in U.S. Patent 5,026,798 (Canich) or in U.S. Patent 5,055,438 (Canich). The uniformly branched/homogeneous polymers are those polymers in which the comonomer is randomly distributed within a given interpolymer molecule and wherein substantially all of the interpolymer molecules have the same ethylene/comonomer ratio within that interpolymer, but these polymers too have an absence of long chain branching, as, for example, Exxon Chemical has taught in their February 1992 Tappi Journal paper.
The traditional homogeneous linear polymers have only a single melting point, as opposed to traditional Ziegler polymerized heterogeneous linear ethylene/a-olefin copolymers which have two or more melting points (determined using differential scanning calorimetry (DSC)).
The SCBDI (Short Chain Branch Distribution Index) or CDBI-(Composition Distribution Branch Index) is defined as the weight percent of the polymer molecules having a comonomer content within 50 percent of the median total molar comonomer content. The CDBI of a polymer is readily calculated from data obtained from techniques known in the art, such as, for example, temperature rising elution fractionation (abbreviated herein as "TREF") as described, for example, in Wild et al, ournal of Polymer Science, P_ olv. Phvs. Ed., Vol.
20, p. 441 (1982), or as described in U.S. Patent 4,798,081. The SCBDI or CDBI for the homogeneous linear olefin polymers of the present invention is preferably greater than about 30 percent, especially greater than about 50 percent.
21fi~~6rl The density of the ethylene or ethylene/a-olefin homogeneous linear ethylene polymers in the present invention is measured in accordance with ASTM D-792 and is generally from 0.85 gramS/cubic centimeter (g/cm3) to 0.93 g/cm3, preferably from 0.9 g/cm3 to 0.92 g/cm3, and especially from 0.9 g/cm3 to 0.915 g/cm3.
Melting point (and Vicat softening point) of the homogeneous linear ethylene polymers correlates primarily with the density of the polymer since the homogeneous linear ethylene polymers lack a high density (that is, linear) fraction, with some effects attributable to the molecular weight of the polymer (indicated as melt index). Melting point variation of the homogeneous linear ethylene polymers is contrasted with heterogeneous ethylene polymers having two or more melting points (due to their broad branching distribution), one of which is about 126°C and is attributable to the high density linear polyethylene fraction in the heterogeneous ethylene polymer. The lower the density of the homogeneous linear ethylene polymer, the lower the melting point.
Some gaskets must withstand temperatures higher than room temperature (about 25°C) for brief times, particularly where the application is a "hot fill" application. For example, products which must undergo pasteurization must have gaskets that have melting points greater than 100°C. Thus the homogeneous linear ethylene polymer can be selected specifically for the application in question by selecting the appropriate density for use in the gasket environment.
The molecular weight of the ethylene or ethylene/a-olefin homogeneous linear olefin polymers in the present invention is .
conveniently indicated using a melt index measurement according tQ
ASTM D-1238, Condition 190°C/2.16 kg (formally known as "Condition (E)" and also known as I2). Melt index is inversely proportional to the molecular weight of the polymer. Thus, the higher the molecular weight, the lower the melt index, although the relationship is not linear. The melt index for the ethylene or ethylene/a-olefin homogeneous linear olefin polymers used herein is generally from 0.01 grams/10 minutes (g/10 min) to 1000 g/10 min, preferably from 1 g/10 min to 100 g/10 min, and especially from 10 g/10 min to 50 g/10 min. Molecular weight, as indicated by the melt index, will be dependent upon the shear rate necessary to process the polymer into the gasket.
Another measurement useful in characterizing the molecular weight of the homogeneous linear olefin polymers is conveniently indicated using a melt index measurement according to ASTM D-1238, Condition 190°C/10 kg (formerly known as "Condition (N)" and also known as hp). The ratio of these two melt index terms is the melt flow ratio and is designated as hp/I2. As with the traditional Ziegler polymerized heterogeneous ethylene polymers, as the hp/I2 ratio of the homogeneous linear ethylene/a-olefin polymers correlates with the molecular weight distribution (M~,~,/Mn): as the I1p/I2 increases, the MW/M" also increases.
Other polymers can also be combined with effective amounts of the homogeneous linear ethylene polymers to make the gaskets as well, depending upon the end use properties required.
These other polymers are thermoplastic polymers (that is, melt processable) and include polymers such as highly branched low density polyethylene, heterogeneously branched linear low density polyethylene, ethylene/vinyl acetate copolymers, and ethylene/acrylic acid copolymers (for example, PrimacorTM Adhesive Polymers made by The Dow Chemical Company).
The gaskets made from the homogeneous linear ethylene polymers must be hard enough to withstand compression, but still soft enough such that an adequate seal is formed. Thus, the hardness of the polymer enables varying gaskets to be made, depending on the use.
Hardness is measured herein as "Shore A" or "Shore D" hardness (as determined using ASTM D-2240). For the homogeneous linear ethylene polymers which comprise the gaskets, the Shore A hardness ranges from 70 to 100, even without the use of petroleum oils commonly included to reduce the hardness of the polymer and resulting gasket.
Melting point (and Vicat softening point) of the homogeneous linear ethylene polymers correlates primarily with the density of the polymer since the homogeneous linear ethylene polymers lack a high density (that is, linear) fraction, with some effects attributable to the molecular weight of the polymer (indicated as melt index). Melting point variation of the homogeneous linear ethylene polymers is contrasted with heterogeneous ethylene polymers having two or more melting points (due to their broad branching distribution), one of which is about 126°C and is attributable to the high density linear polyethylene fraction in the heterogeneous ethylene polymer. The lower the density of the homogeneous linear ethylene polymer, the lower the melting point.
Some gaskets must withstand temperatures higher than room temperature (about 25°C) for brief times, particularly where the application is a "hot fill" application. For example, products which must undergo pasteurization must have gaskets that have melting points greater than 100°C. Thus the homogeneous linear ethylene polymer can be selected specifically for the application in question by selecting the appropriate density for use in the gasket environment.
The molecular weight of the ethylene or ethylene/a-olefin homogeneous linear olefin polymers in the present invention is .
conveniently indicated using a melt index measurement according tQ
ASTM D-1238, Condition 190°C/2.16 kg (formally known as "Condition (E)" and also known as I2). Melt index is inversely proportional to the molecular weight of the polymer. Thus, the higher the molecular weight, the lower the melt index, although the relationship is not linear. The melt index for the ethylene or ethylene/a-olefin homogeneous linear olefin polymers used herein is generally from 0.01 grams/10 minutes (g/10 min) to 1000 g/10 min, preferably from 1 g/10 min to 100 g/10 min, and especially from 10 g/10 min to 50 g/10 min. Molecular weight, as indicated by the melt index, will be dependent upon the shear rate necessary to process the polymer into the gasket.
Another measurement useful in characterizing the molecular weight of the homogeneous linear olefin polymers is conveniently indicated using a melt index measurement according to ASTM D-1238, Condition 190°C/10 kg (formerly known as "Condition (N)" and also known as hp). The ratio of these two melt index terms is the melt flow ratio and is designated as hp/I2. As with the traditional Ziegler polymerized heterogeneous ethylene polymers, as the hp/I2 ratio of the homogeneous linear ethylene/a-olefin polymers correlates with the molecular weight distribution (M~,~,/Mn): as the I1p/I2 increases, the MW/M" also increases.
Other polymers can also be combined with effective amounts of the homogeneous linear ethylene polymers to make the gaskets as well, depending upon the end use properties required.
These other polymers are thermoplastic polymers (that is, melt processable) and include polymers such as highly branched low density polyethylene, heterogeneously branched linear low density polyethylene, ethylene/vinyl acetate copolymers, and ethylene/acrylic acid copolymers (for example, PrimacorTM Adhesive Polymers made by The Dow Chemical Company).
The gaskets made from the homogeneous linear ethylene polymers must be hard enough to withstand compression, but still soft enough such that an adequate seal is formed. Thus, the hardness of the polymer enables varying gaskets to be made, depending on the use.
Hardness is measured herein as "Shore A" or "Shore D" hardness (as determined using ASTM D-2240). For the homogeneous linear ethylene polymers which comprise the gaskets, the Shore A hardness ranges from 70 to 100, even without the use of petroleum oils commonly included to reduce the hardness of the polymer and resulting gasket.
2i6~~6'~ _.
Additives such as antioxidants (for example, hindered phenolics (for example, Irganox~ 1010 made by Ciba Geigy Corp.), phosphites (for example, Irgafos~ 168 made by Ciba Geigy Corp.)), cling additives (for example, polyisobutylene (PIB)), slip additives (for example, erucamide), antiblock additives, pigments, and the like can also be included in the polyethylene compositions, to the extent that they do not interfere with the enhanced properties discovered by Applicants.
The whole interpolymer product samples and the individual interpolymer samples are analyzed by gel permeation chromatography (GPC) on a Waters 150C high temperature chromatographic unit equipped with three mixed porosity columns (Polymer Laboratories 103, 104, 105, and 106), operating at a system temperature of 140°C. The solvent is 1,2,4-trichlorobenzene, from which 0.3 percent by weight solutions of the samples are prepared for injection. The flow rate is 1.0 milliliters/minute and the injection size is 200 microliters.
The molecular weight determination is deduced by using narrow molecular weight distribution polystyrene standards (from Polymer Laboratories) in conjunction with their elution volumes. The equivalent polyethylene molecular weights are determined by using appropriate Mark-Houwink coefficients for polyethylene and polystyrene (as described by Williams and Word in Iournal of Pol, Science, hymer Letters, Vol. 6, (621) 1968) to derive the following equation:
Mpolyethylene = a * (Mpolystyrene)b~
In this equation, a = 0.4316 and b = 1Ø Weight average molecular weight, MW, is calculated in the usual manner according to the following formula: M~,, _ ~ w;* M;, where w; and M; are the weight fraction and molecular weight, respectively, of the ith fraction eluting from the GPC column.
Additives such as antioxidants (for example, hindered phenolics (for example, Irganox~ 1010 made by Ciba Geigy Corp.), phosphites (for example, Irgafos~ 168 made by Ciba Geigy Corp.)), cling additives (for example, polyisobutylene (PIB)), slip additives (for example, erucamide), antiblock additives, pigments, and the like can also be included in the polyethylene compositions, to the extent that they do not interfere with the enhanced properties discovered by Applicants.
The whole interpolymer product samples and the individual interpolymer samples are analyzed by gel permeation chromatography (GPC) on a Waters 150C high temperature chromatographic unit equipped with three mixed porosity columns (Polymer Laboratories 103, 104, 105, and 106), operating at a system temperature of 140°C. The solvent is 1,2,4-trichlorobenzene, from which 0.3 percent by weight solutions of the samples are prepared for injection. The flow rate is 1.0 milliliters/minute and the injection size is 200 microliters.
The molecular weight determination is deduced by using narrow molecular weight distribution polystyrene standards (from Polymer Laboratories) in conjunction with their elution volumes. The equivalent polyethylene molecular weights are determined by using appropriate Mark-Houwink coefficients for polyethylene and polystyrene (as described by Williams and Word in Iournal of Pol, Science, hymer Letters, Vol. 6, (621) 1968) to derive the following equation:
Mpolyethylene = a * (Mpolystyrene)b~
In this equation, a = 0.4316 and b = 1Ø Weight average molecular weight, MW, is calculated in the usual manner according to the following formula: M~,, _ ~ w;* M;, where w; and M; are the weight fraction and molecular weight, respectively, of the ith fraction eluting from the GPC column.
The molecular weight distribution (Mw/Mn) for the homogeneous linear olefin polymers of the invention is generally from 1.5 to 2.5.
The homogeneous linear polymers of the present invention can be homopolymers of C2-C2o a-olefins, such as ethylene, propylene, 4-methyl-1-pentene, etc., or they can be interpolymers of ethylene with at least one C3-C2o a-olefin and/or Cz-Czo acetylenically unsaturated monomer and/or C4-C1g diolefins, or they can be copolymers of ethylene with at least one C3-C2o a-olefin. The homogeneous linear polymers of the present invention can also be interpolymers of ethylene with at least one of the above C3-C2o a-olefins, diolefins and/or acetylenically unsaturated monomers in combination with other unsaturated monomers.
Monomers usefully polymerized according to the present invention include, for example, ethylenically unsaturated monomers, acetylenic compounds, conjugated or nonconjugated dienes, polyenes, carbon monoxide, etc.
Preferred monomers include the Cz-Clo a-olefins especially ethylene, 1-propene, isobutylene, 1-butene, 1-hexene, 4-methyl-1-pentene, and 1-octene. Other preferred monomers include styrene, halo- or alkyl substituted styrenes, tetrafluoroethylene, vinylbenzocyclobutane, 1,4-hexadiene, and naphthenics (for example, cyclo-pentene, cyclo-hexene and cyclo-octene).
Other unsaturated monomers usefully polymerized according to the present invention include, for example, ethylenically unsaturated monomers, conjugated or nonconjugated dimes, polyenes, etc. Preferred monomers include the Cz-Clo a-olefins especially ethylene, propene, isobutylene, 1-butene, 1-hexene, 4-methyl-1-pentene, and 1-octene. Other preferred monomers include styrene, halo-_7_ or alkyl substituted styrenes, tetrafluoroethylene, vinylbenzocyclobutane, 1,4-hexadiene, and naphthenics (for example, cyclopentene, cyclohexene and cyclooctene).
Gaskets can have many different forms, including "o-rings" and flat seals (for example, "film-like" gaskets having a thickness commensurate with the intended use).
-7a-7 . PCT/US94/09377 21~g()6'~
Suitable end uses include beverage cap liners, hot fill juice cap liners, polypropylene cap liners, metal cap liners, high density polyethylene cap liners, window glass gaskets, sealed containers, closure caps, gaskets for medical devices, filter elements, pressure venting gaskets, hot melt gaskets, easy twist off caps, electrochemical cell gaskets, refrigerator gaskets, galvanic cell gaskets, leak proof cell gaskets, waterproofing sheet, reusable gaskets, synthetic cork like materials, thin cell electromembrane separator, magnetic rubber materials, disc gaskets for alcoholic beverage bottle caps, freeze resistant seal rings, gaskets for plastic castings, expansion joints and waterstops, corrosion-resistant conduit connectors, flexible magnetic plastics, pipe joint seals, integral weatherproof plastic lid and hinge for electrical outlets, magnetic faced foamed articles, jar rings, flexible gaskets, glass seals, tamper evident sealing liners, pressure applicators, combined bottle cap and straw structures, large condiment bottle liners and the like.
Gaskets made from the homogeneous linear ethylene polymers have numerous advantages, especially when used in food-stuff applications. These include: improved taste and odor over incumbent polymer gaskets such as ethylene/vinyl acetate; low adhesion to polar substrates (for example, polyethylene terephthalate, glass) which is useful for low torque removal of the closure/cap; low extractables (also useful for food-stuffs, especially regarding regulatory compliance); good adhesion to non-polar substrates (for example, polypropylene and high density polyethylene (either linear homopolymer polyethylene or linear heterogeneous high density polyethylene)); adequate oxygen, carbon dioxide and water barrier; high melting point relative to incumbent polymers (for example, ethylene/vinyl acetate); good stress crack resistance; good chemical resistance; and variable hardness (useful for specific packaging which may require more or less gasket stiffness, depending on the degree of torque required to seal the container and the internal pressure of the container).
_g_ Various gasket manufacturing techniques include those disclosed in USP 5,215,587 (McConnellogue et al.); USP 4,085,186 (gainer); USP 4,619,848 (Knight et al.); USP 5,104,710 (Knight); USP
4,981,231 (Knight); USP 4,717,034 (Mumford); USP 3,786,954 (Shull);
USP 3,779,965 (Lefforge et al.); USP 3,493,453 (Ceresa et al.); USP
3,183,144 (Caviglia); USP 3,300,072 (Caviglia); USP 4,984,703 (Burzynski);
USP 3,414,938 (Caviglia); USP 4,939,859 (Bayer); USP 5,137,164 (Bayer);
and USP 5,000,992 (Kelch). The gaskets claimed herein can also be made from extruded sheets or films by conventional techniques as blown, cast or extrusion coated films, followed by stamping or cutting the gasket from the sheet or film. Multilayer film structures are also suitable for making the gaskets disclosed herein, with the proviso that at least one layer (preferably the inner layer which is located adjacent to the product) comprises the homogeneous linear ethylene polymer.
The homogeneous linear polymers of the present invention can be homopolymers of C2-C2o a-olefins, such as ethylene, propylene, 4-methyl-1-pentene, etc., or they can be interpolymers of ethylene with at least one C3-C2o a-olefin and/or Cz-Czo acetylenically unsaturated monomer and/or C4-C1g diolefins, or they can be copolymers of ethylene with at least one C3-C2o a-olefin. The homogeneous linear polymers of the present invention can also be interpolymers of ethylene with at least one of the above C3-C2o a-olefins, diolefins and/or acetylenically unsaturated monomers in combination with other unsaturated monomers.
Monomers usefully polymerized according to the present invention include, for example, ethylenically unsaturated monomers, acetylenic compounds, conjugated or nonconjugated dienes, polyenes, carbon monoxide, etc.
Preferred monomers include the Cz-Clo a-olefins especially ethylene, 1-propene, isobutylene, 1-butene, 1-hexene, 4-methyl-1-pentene, and 1-octene. Other preferred monomers include styrene, halo- or alkyl substituted styrenes, tetrafluoroethylene, vinylbenzocyclobutane, 1,4-hexadiene, and naphthenics (for example, cyclo-pentene, cyclo-hexene and cyclo-octene).
Other unsaturated monomers usefully polymerized according to the present invention include, for example, ethylenically unsaturated monomers, conjugated or nonconjugated dimes, polyenes, etc. Preferred monomers include the Cz-Clo a-olefins especially ethylene, propene, isobutylene, 1-butene, 1-hexene, 4-methyl-1-pentene, and 1-octene. Other preferred monomers include styrene, halo-_7_ or alkyl substituted styrenes, tetrafluoroethylene, vinylbenzocyclobutane, 1,4-hexadiene, and naphthenics (for example, cyclopentene, cyclohexene and cyclooctene).
Gaskets can have many different forms, including "o-rings" and flat seals (for example, "film-like" gaskets having a thickness commensurate with the intended use).
-7a-7 . PCT/US94/09377 21~g()6'~
Suitable end uses include beverage cap liners, hot fill juice cap liners, polypropylene cap liners, metal cap liners, high density polyethylene cap liners, window glass gaskets, sealed containers, closure caps, gaskets for medical devices, filter elements, pressure venting gaskets, hot melt gaskets, easy twist off caps, electrochemical cell gaskets, refrigerator gaskets, galvanic cell gaskets, leak proof cell gaskets, waterproofing sheet, reusable gaskets, synthetic cork like materials, thin cell electromembrane separator, magnetic rubber materials, disc gaskets for alcoholic beverage bottle caps, freeze resistant seal rings, gaskets for plastic castings, expansion joints and waterstops, corrosion-resistant conduit connectors, flexible magnetic plastics, pipe joint seals, integral weatherproof plastic lid and hinge for electrical outlets, magnetic faced foamed articles, jar rings, flexible gaskets, glass seals, tamper evident sealing liners, pressure applicators, combined bottle cap and straw structures, large condiment bottle liners and the like.
Gaskets made from the homogeneous linear ethylene polymers have numerous advantages, especially when used in food-stuff applications. These include: improved taste and odor over incumbent polymer gaskets such as ethylene/vinyl acetate; low adhesion to polar substrates (for example, polyethylene terephthalate, glass) which is useful for low torque removal of the closure/cap; low extractables (also useful for food-stuffs, especially regarding regulatory compliance); good adhesion to non-polar substrates (for example, polypropylene and high density polyethylene (either linear homopolymer polyethylene or linear heterogeneous high density polyethylene)); adequate oxygen, carbon dioxide and water barrier; high melting point relative to incumbent polymers (for example, ethylene/vinyl acetate); good stress crack resistance; good chemical resistance; and variable hardness (useful for specific packaging which may require more or less gasket stiffness, depending on the degree of torque required to seal the container and the internal pressure of the container).
_g_ Various gasket manufacturing techniques include those disclosed in USP 5,215,587 (McConnellogue et al.); USP 4,085,186 (gainer); USP 4,619,848 (Knight et al.); USP 5,104,710 (Knight); USP
4,981,231 (Knight); USP 4,717,034 (Mumford); USP 3,786,954 (Shull);
USP 3,779,965 (Lefforge et al.); USP 3,493,453 (Ceresa et al.); USP
3,183,144 (Caviglia); USP 3,300,072 (Caviglia); USP 4,984,703 (Burzynski);
USP 3,414,938 (Caviglia); USP 4,939,859 (Bayer); USP 5,137,164 (Bayer);
and USP 5,000,992 (Kelch). The gaskets claimed herein can also be made from extruded sheets or films by conventional techniques as blown, cast or extrusion coated films, followed by stamping or cutting the gasket from the sheet or film. Multilayer film structures are also suitable for making the gaskets disclosed herein, with the proviso that at least one layer (preferably the inner layer which is located adjacent to the product) comprises the homogeneous linear ethylene polymer.
Claims (16)
1. A gasket comprising at least one homogeneous linear ethylene polymer having an absence of long chain branching, wherein the at least one homogeneous linear ethylene polymer is selected from a group consisting of a homopolymer of ethylene, an interpolymer of ethylene with at least one C3-C20 a-olefin and a copolymer of ethylene with a C3-C20 .alpha.-olefin, and the homogeneous linear ethylene polymer has a composition distribution breadth index greater than 50 percent.
2. The gasket of claim 1, wherein the homogeneous linear ethylene polymer is produced using a single site catalyst.
3. The gasket of claim 1, wherein the homogeneous linear ethylene polymer has a single melting point, as determined by differential scanning calorimetry.
4. The gasket of claim 1, wherein the homogeneous linear ethylene polymer has a density of from 0.85 to 0.93 g/cm3.
5. The gasket of claim 1, wherein the homogeneous linear ethylene polymer has a melt index (I2) of from 0.01 g/10 min. to 1000 8110 min.
6. The gasket of claim 1, wherein the homogeneous linear ethylene polymer has a melt index (I2) of 1 g/10 min.
to 100 g/10 min.
to 100 g/10 min.
7. The gasket of any one of claims 1 to 6 in the form of a beverage cap liner.
8. The gasket of claim 1, wherein the homogeneous linear ethylene polymer is a copolymer of ethylene and 1-hexene.
9. The gasket of claim 1, wherein the homogeneous linear ethylene polymer is a copolymer of ethylene and 1-octene.
10. The gasket of claim 1, wherein the homogeneous linear ethylene polymer has a Shore A hardness from 70 to 100.
11. The gasket of claim 1, wherein the gasket further comprises a thermoplastic polymer selected from the group consisting of highly branched low density polyethylene, heterogeneously branched linear low density polyethylene, ethylene/vinyl acetate copolymers and ethylene/acrylic acid copolymers.
12. The gasket of any one of claims 1 to 11, wherein the gasket further comprises an additive selected from the group consisting of antioxidants, cling additives, slip additives, antiblock additives, and pigments.
13. The gasket of claim 1, wherein the homogeneous linear ethylene polymer has a molecular weight distribution (M w/M n) in the range of from 1.5 to 2.5.
14. An article of manufacture comprising the gasket of any one of claims 1 to 13, and a polar substrate to which the gasket is releasably retained.
15. The article of manufacture of claim 14, wherein the polar substrate comprises glass or polyethylene terephthalate.
16. An article of manufacture comprising the gasket of claim 1, and a non-polar cap of polypropylene or high density polyethylene.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
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US10885593A | 1993-08-18 | 1993-08-18 | |
US08/108,855 | 1993-08-18 | ||
PCT/US1994/009377 WO1995005427A1 (en) | 1993-08-18 | 1994-08-18 | Gaskets made from homogeneous linear olefin polymers |
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CA2169067A1 CA2169067A1 (en) | 1995-02-23 |
CA2169067C true CA2169067C (en) | 2006-09-12 |
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CA002169067A Expired - Lifetime CA2169067C (en) | 1993-08-18 | 1994-08-18 | Gaskets made from homogeneous linear olefin polymers |
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