GB2552865A - Foam gasket and preparation method thereof - Google Patents

Foam gasket and preparation method thereof Download PDF

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Publication number
GB2552865A
GB2552865A GB1704539.4A GB201704539A GB2552865A GB 2552865 A GB2552865 A GB 2552865A GB 201704539 A GB201704539 A GB 201704539A GB 2552865 A GB2552865 A GB 2552865A
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United Kingdom
Prior art keywords
substrate layer
acid amide
screw extruder
film
raw materials
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Granted
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GB1704539.4A
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GB2552865B (en
GB201704539D0 (en
Inventor
Wang Yanping
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Jiangsu Jinhou New Material Tech Co Ltd
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Jiangsu Jinhou New Material Tech Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions 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
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/06Polyethene
    • 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
    • B32B5/00Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts
    • B32B5/18Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts characterised by features of a layer of foamed material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/02Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles
    • B29C44/04Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles consisting of at least two parts of chemically or physically different materials, e.g. having different densities
    • B29C44/06Making multilayered articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/20Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of indefinite length
    • B29C44/22Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of indefinite length consisting of at least two parts of chemically or physically different materials, e.g. having different densities
    • B29C44/24Making multilayered articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/36Feeding the material to be shaped
    • B29C44/46Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length
    • B29C44/50Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length using pressure difference, e.g. by extrusion or by spraying
    • 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
    • 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
    • B32B27/065Layered 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 foam
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    • 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
    • B32B27/32Layered products comprising a layer of synthetic resin comprising polyolefins
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS 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
    • B65D41/00Caps, e.g. crown caps or crown seals, i.e. members having parts arranged for engagement with the external periphery of a neck or wall defining a pouring opening or discharge aperture; Protective cap-like covers for closure members, e.g. decorative covers of metal foil or paper
    • B65D41/02Caps or cap-like covers without lines of weakness, tearing strips, tags, or like opening or removal devices
    • B65D41/04Threaded or like caps or cap-like covers secured by rotation
    • B65D41/0435Threaded or like caps or cap-like covers secured by rotation with separate sealing elements
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions 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
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/08Copolymers of ethene
    • C08L23/0807Copolymers of ethene with unsaturated hydrocarbons only containing more than three carbon atoms
    • C08L23/0815Copolymers of ethene with aliphatic 1-olefins
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions 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
    • C08L23/10Homopolymers or copolymers of propene
    • C08L23/12Polypropene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/36Feeding the material to be shaped
    • B29C44/46Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length
    • B29C44/50Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length using pressure difference, e.g. by extrusion or by spraying
    • B29C44/505Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length using pressure difference, e.g. by extrusion or by spraying extruding the compound through a flat die
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/04Polymers of ethylene
    • B29K2023/06PE, i.e. polyethylene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/10Polymers of propylene
    • B29K2023/12PP, i.e. polypropylene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2031/00Other particular articles
    • B29L2031/26Sealing devices, e.g. packaging for pistons or pipe joints
    • B29L2031/265Packings, Gaskets
    • 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
    • B32B2250/00Layers arrangement
    • B32B2250/24All layers being polymeric
    • B32B2250/242All polymers belonging to those covered by group B32B27/32
    • 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
    • B32B2250/00Layers arrangement
    • B32B2250/40Symmetrical or sandwich layers, e.g. ABA, ABCBA, ABCCBA
    • 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
    • B32B2266/00Composition of foam
    • B32B2266/02Organic
    • B32B2266/0207Materials belonging to B32B25/00
    • 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
    • B32B2266/00Composition of foam
    • B32B2266/02Organic
    • B32B2266/0214Materials belonging to B32B27/00
    • B32B2266/025Polyolefin
    • 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
    • B32B2266/00Composition of foam
    • B32B2266/10Composition of foam characterised by the foam pores
    • B32B2266/102Nanopores, i.e. with average diameter smaller than 0.1 µm
    • 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
    • B32B2266/00Composition of foam
    • B32B2266/10Composition of foam characterised by the foam pores
    • B32B2266/104Micropores, i.e. with average diameter in the range from 0.1 µm to 0.1 mm
    • 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
    • B32B2266/00Composition of foam
    • B32B2266/10Composition of foam characterised by the foam pores
    • B32B2266/106Unimodal pore distribution
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
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    • B32B2307/00Properties of the layers or laminate
    • B32B2307/50Properties of the layers or laminate having particular mechanical properties
    • B32B2307/546Flexural strength; Flexion stiffness
    • 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
    • B32B2307/00Properties of the layers or laminate
    • B32B2307/70Other properties
    • B32B2307/72Density
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00Properties of the layers or laminate
    • B32B2307/70Other properties
    • B32B2307/732Dimensional properties
    • 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
    • B32B2435/00Closures, end caps, stoppers
    • B32B2435/02Closures, end caps, stoppers for containers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/14Applications used for foams
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/16Applications used for films
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • C08L2205/035Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend

Abstract

The foam gasket comprises a substrate layer and a film layer covering the upper and lower surfaces of the substrate layer. The substrate layer is a foam body and a uniform capillary pore body. The average pore diameter of the capillary pores is 1-100 µm. The film layer is uniform and compact. The foam comprises polyethylene (PE) and/or polypropylene (PP), polyethylene octene (POE), styrene butadiene styrene (SBS) and/or styrene ethylene butadiene styrene (SEBS), release agent, and nucleating agent. The film comprises at least two of PE, PP and POE, release agent and anti-block agent. The gasket is formed by extrusion foaming using supercritical carbon dioxide and then extrusion coating. The gasket is used for sealing caps on food and medicine packaging.

Description

(54) Title of the Invention: Foam gasket and preparation method thereof Abstract Title: Foam gasket and production thereof (57) The foam gasket comprises a substrate layer and a film layer covering the upper and lower surfaces of the substrate layer. The substrate layer is a foam body and a uniform capillary pore body. The average pore diameter of the capillary pores is 1-100 pm. The film layer is uniform and compact. The foam comprises polyethylene (PE) and/ or polypropylene (PP), polyethylene octene (POE), styrene butadiene styrene (SBS) and/or styrene ethylene butadiene styrene (SEBS), release agent, and nucleating agent. The film comprises at least two of PE, PP and POE, release agent and anti-block agent. The gasket is formed by extrusion foaming using supercritical carbon dioxide and then extrusion coating. The gasket is used for sealing caps on food and medicine packaging.
Foam gasket and preparation method thereof
Technical field
The present invention belongs to the technical field of high safety fields such as food packaging, medicine packaging and so on, and relates to a foam gasket and a preparation method thereof, and more particularly to a sealing gasket for bottle caps and a preparation method thereof.
Background art
Bottle cap gasket is made of rubber, copper sheet, or paper. It is a material used to fit between two planes to reinforce sealing and has an effect of preventing fluid leakage. With the continuous development of the economy, bottle cap gaskets are widely used in wines, food, cosmetics, pharmaceutical and other industries.
According to the relevant news reports, there is a growing demand currently on bottle cap gaskets in wine packaging and beverage packaging in China, and bottle cap gaskets used in wine packaging cover more than 70% of the total amount of used cap gaskets. With the rapid development of China's wine and beverage industry, bottle cap gasket industry gradually rises. China's bottle cap gasket production in 2014 has a year-on-year increase of 14% compared to 2013, this huge demand not only pulls the price of bottle cap gaskets up all the way, but also makes the number of manufacturers of bottle cap gaskets increase rapidly. At present, China has become the largest consumer and exporter in the world for bottle cap gaskets.
There are as many as hundreds of products in China's bottle cap gasket market, and various specifications and types of bottle cap gaskets exist in the market of food packaging containers. At present, the materials of gaskets used in food packaging are PVC (polyvinyl chloride), PE (polyethylene), Warrior cushion, aluminum foil composite gaskets, paper-plastic-aluminum composite gaskets and others, wherein PVC and PE are the main materials.
CN 104250404A discloses a granule of can bottle cap gasket and its preparation method, wherein the granule of can bottle cap gasket comprises the following materials in parts by mass: 30-50 parts of polypropylene, 30-50 parts of polyethylene, 10-30 parts of a thermoplastic elastomer, and 0.4-5 parts of a processing agent. The granule of can bottle cap gasket is prepared by mixing the above raw materials by a high-speed mixer, extruding by an extruder, cooling, and dicing. The granule of can bottle cap gasket is completely prepared from safe and non-toxic raw materials, free of harmful plasticizers such as phthalates, can meet the safe and non-toxic requirements on the granule of can bottle cap gasket and is excellent in leak tightness.
CN 1465507A discloses a lining material for bottle caps and its application in the hot-filled beverage plastic bottle cap. Said lining material is made of a combination of maleic acid modified EVA (ethylene-vinyl acetate copolymer), SEBS (hydrophenylethylene diene copolymer), hydrogenated paraffin oil, branched low-density polyethylene, polypropylene, polystyrene and low-molecular lubricant. Said lining material comprises EVA having a VA (vinyl acetate) content of 18%, and the weight ratio of the EVA is 5-60%. Ethylene-a-olefin copolymer was added and the weight ratio thereof is 90-35%. This material is not available in conventional cap lining materials. This lining material made by such blending has excellent performances compared with the existing lining material for beverage packaging plastic cap. This gasket material not only is inexpensive, but also has better effects than lining materials of conventional hot-filled beverage plastic bottle caps.
However, the sealability of the existing bottle cap gaskets need to be further improved.
Contents of the Invention
In view of the deficiencies existing in the prior art, the purpose of the present invention is to provide a foam gasket and a preparation method thereof. The foam gasket has good flexibility, softness and elasticity, and is a food-grade plastic sheet, and has excellent sealability when used as a bottle cap gasket. Meanwhile, the preparation method thereof is simple, and easy to be applied in industrial applications.
bar = 0.1 MPa.
In order to achieve the above purpose, the present invention utilizes the following technical solution.
The first purpose of the present invention is to provide a foam gasket comprising a substrate layer and a film layer covering the upper and lower surfaces of the substrate layer. The substrate layer is a foam body and a uniform capillary pore body. The average pore diameter of the capillary pores is 1-100 pm, for example, 2 pm, 5 pm, 8 pm, 10 pm, 12 pm, 15 pm, 18 pm, 20 pm, 30 pm, 40 pm, 50 pm, 60 pm, 80 pm, 90 pm, or 95 pm, etc. The film layer is uniform and compact.
The substrate layer is mainly prepared from the following raw materials in mass percent:
PE (polyethylene), 0-90%, for example 2%, 5%, 10%, 20%, 30%, 40%, 50%, 60%, 70%, 80%, or 85%, etc.;
PP (polypropylene), 0-90%, for example 2%, 5%, 10%, 20%, 30%, 40%, 50%, 60%, 70%, 80%, or 85%, etc.;
any one of POE (ethylene-octene copolymer), SBS (block copolymer of styrene and butadiene), or SEBS (hydrogenated styrene-butadiene block copolymer), or a combination of at least two of them, 0-20% (not including 0), for example 0.5%, 1%, 2%, 3%, 5%, 6%, 8%, 10%, 12%, 15%, or 18%, etc.;
release agent, 0.2-1.0%, for example 0.3%, 0.5%, 0.6%, 0.7%, 0.8%, or 0.9%, etc.;
nucleating agent, 0.1-2.5%, for example 0.3%, 0.5%, 0.8%, 1.0%, 1.2%, 1.5%, 1.8%, 2.0%, or 2.3%, etc.;
color masterbatch, 0-2.0%, for example 0.1%, 0.5%, 0.8%, 1.0%, 1.2%, 1.3%, 1.5%, 1.7%, or 1.9%, etc.;
wherein at most one substance of PE and PP has a mass percentage of zero; combinations of POE, SBS or SEBS are, for example, a combination of POE and SBS, a combination of POE and SEBS, a combination of POE, SBS and SEBS.
The film layer is mainly prepared from the following raw materials in mass percent:
PE, 0-93%, for example 2%, 3%, 5%, 10%, 20%, 30%, 50%, 60%, 70%, 80%, or 90%, etc.;
PP, 0-95%, for example 1%, 3%, 5%, 8%, 10%, 20%, 30%, 50%, 60%, 80%, or 90%, etc.;
POE, 0-93%, for example 2%, 3%, 5%, 10%, 20%, 30%, 50%, 60%, 70%, 80%, or 90%, etc.;
thickener, 0-30%, for example 1%, 3%, 5%, 8%, 10%, 12%, 15%, 18%, 20%, 23%, 25%, or 28%, etc.;
release agent, 0.2-1.1%, for example 0.3%, 0.5%, 0.8%, or 1.0%, etc.;
antiblocking agent, 0.1-3.0%, for example 0.3%, 0.5%, 0.8%, 1.0%, 1.2%, 1.5%, 1.8%, 2.0%, 2.1%, 2.3%, 2.5%, or 2.8%, etc.;
wherein at most one substance of PE, PP and POE has a mass percentage of zero.
The expression of “The substrate layer is a uniform capillary pore body” means that 4 the substrate layer comprises a plurality of capillary pores which are uniformly distributed.
As a preferred embodiment, the substrate layer is prepared from the following raw materials in mass percent:
PE 80%
PP 15% any one of POE, SBS, or SEBS, or a combination of at least two of them 1% release agent 1.0% nucleating agent 2.0% color masterbatch 1%.
Preferably, the release agent is any one selected from the group consisting of oleic acid amide, erucic acid amide, and masterbatch prepared from oleic acid amide and erucic acid amide with PE or PP as a carrier, or a combination of at least two of them. Typical but non-limiting combinations are for example a combination of oleic acid amide and erucic acid amide, a combination of oleic acid amide and masterbatch prepared from oleic acid amide and erucic acid amide with PE or PP as a carrier, and a combination of erucic acid amide and masterbatch prepared from oleic acid amide and erucic acid amide with PE or PP as a carrier.
Preferably, the nucleating agent is selected from masterbatches with sodium bicarbonate and citric acid as the main active ingredients and PE or PP or EVA as a carrier.
As a preferred embodiment, the film layer is mainly prepared from the following raw materials in mass percent:
PE
90%
PP 5%
POE 0.5% thickener 3.5% release agent 0.5% antiblocking agent 0.5%.
Preferably, the thickener is any one selected from the group consisting of EEA (ethylene-ethyl acrylate), polyester, and maleic anhydride grafted resin, or a combination of at least two of them. Typical but non-limiting combinations are for example a combination of EEA and polyester, a combination of EEA and maleic anhydride grafted resin, and a combination of EEA, polyester and maleic anhydride grafted resin.
Preferably, the release agent is any one selected from the group consisting of oleic acid amide, erucic acid amide, and masterbatch prepared from oleic acid amide and erucic acid amide with PE or PP as a carrier, or a combination of at least two of them. Typical but non-limiting combinations are for example a combination of oleic acid amide and erucic acid amide, a combination of oleic acid amide and masterbatch prepared from oleic acid amide and erucic acid amide with PE or PP as a carrier, and a combination of erucic acid amide and masterbatch prepared from oleic acid amide and erucic acid amide with PE or PP as a carrier.
Preferably, the antiblocking agent is selected from erucic acid amide.
The thickness of the substrate layer is 0.5 to 10.0 mm, for example 0.8 mm, 1.0 mm,
1.5 mm, 2.0 mm, 3.0 mm, 4.0 mm, 5.0 mm, 6.0 mm, 8.0 mm, or 9.0 mm, etc. If the substrate layer is too thick, the application performances such as the sealing 6 performance of the material would be not guaranteed; if it is too thin, the flexibility and coordinating complementary performance of the material would be poor.
Preferably, the density of the substrate layer is 100-800 kg/m3, for example 150 kg/m’ 200 kg/m3, 300 kg/m3, 400 kg/m3, 500 kg/m3, 600 kg/m3, or 700 kg/m3, etc.
The substrate layer is excellent in crosslinking sealing property since it is formed by supercritical physical foaming.
Preferably, the thickness of the fdm layer is 0.02 to 0.15 mm, for example 0.05 mm, 0.08 mm, 0.10 mm, 0.12 mm, or 0.14 mm, etc. If the film layer is too thick, the flexibility and coordinating complementary performance of the material would be poor; if the film layer is too thin, the application performances such as the sealing performance of the material would be not guaranteed. The expression “the thickness of the film layer is 0.02 to 0.15 mm” means that the thickness of the film layer on the upper surface of the substrate layer and the thickness of the film layer on the lower surface of the substrate layer are independently 0.02 to 0.15 mm.
The film layer makes the foam gasket meet sealing functional requirement, while allowing it have good flexibility matching performance.
The second purpose of the present invention is to provide a method for preparing the foam gasket described above, and the method comprises the following steps:
(1) The raw materials of the substrate layer with formula amounts are fed into the hopper of a single screw extruder, while supercritical carbon dioxide is charged in the middle of the single screw extruder. After extruding and foaming, a substrate layer is obtained. The supercritical carbon dioxide is a supercritical carbon dioxide under a pressure of 50 to 220 bar, for example a supercritical carbon dioxide under a pressure of 60 bar, 80 bar, 90 bar, 100 bar, 120 bar, 150 bar, 180 bar, or 200 bar;
(2) The raw materials of the film layer with formula amounts are fed into the hopper of the single screw extruder, coated onto the surface of the substrate layer to form a film, and thereby a foam gasket is obtained.
The single screw extruder in step (1) is a single screw extruder having heating, cooling and pressure resistance performances. Atypical but non-limiting single screw extruder is, for example, a foaming machine manufactured by Berstorff GmbH: 150-ISO-PAC.
In step (1), the host temperature of the single screw extruder during the extrusion process is less than or equal to 65°C, for example 63 °C, 60°C, 58°C, 55°C, 50°C, 45°C, or 30°C, etc. If the host temperature is too high, damage to the units will be caused.
Preferably, the extrusion temperature in step (1) is 90-210°C, for example 100°C, 110°C, 130°C, 150°C, 180°C, 190 °C, or 200°C, etc. If the extrusion temperature is too high, the film forming performance would be not good, the film would have an uneven thickness, and the foaming would be uneven. If the extrusion temperature is too low, the film would be unevenly foamed or foaming would not perform.
Preferably, the rotational speed of the screw during the extrusion process in step (1) is 1-100 rpm, for example 2 rpm, 3 rpm, 5 rpm, 10 rpm, 20 rpm, 30 rpm, 40 rpm, 50 rpm, 60 rpm, 70 rpm, 80 rpm, or 90 rpm, etc.
Preferably, the single screw extruder in step (1) has a bearing pressure range of 0 to 250 bar, for example 2 bar, 5 bar, 10 bar, 20 bar, 50 bar, 100 bar, 120 bar, 150 bar, 180 bar, 200 bar, 220 bar, or 240 bar, etc.
The flow rate of the supercritical carbon dioxide in step (1) is 0.10-2.50 kg/h, for example 0.3 kg/h, 0.5 kg/h, 0.8 kg/h, 1.0 kg/h, 1.2 kg/h, 1.5 kg/h, 1.8 kg/h, 2.0 kg/h, or 2.3 kg/h, etc. If the flow rate is high, the film would be foamed unevenly and excessively, and the material would fail in elasticity. If the flow rate is low, the foaming would be too low and the flexibility would not be enough.
Preferably, the thickness of the substrate layer in step (1) is 0.5-10.0 mm, for example 0.8 mm, 1.0 mm, 1.5 mm, 2.0 mm, 3.0 mm, 4.0 mm, 5.0 mm, 6.0 mm, 8.0 mm, or 9.0 mm, etc.
Preferably, the density of the substrate layer in step (1) is 100-800 kg/m , for example 150 kg/m3, 200 kg/m3, 300 kg/m3, 400 kg/m3, 500 kg/m3, 600 kg/m3, or 700 kg/m3.
The extrusion temperature in step (2) is 80-250°C, for example 85°C, 90°C, 95°C, 100°C, 120°C, 130°C, 150°C, 180°C, 200°C, 210°C, 220°C, or 240°C, etc.
Preferably, the rotational speed of the screw during the extrusion process in step (2) is 1-100 rpm, for example 2 rpm, 3 rpm, 5 rpm, 10 rpm, 20 rpm, 30 rpm, 40 rpm, 50 rpm, 60 rpm, 70 rpm, 80 rpm, or 90 rpm, etc.
The thickness of the film covering the substrate layer in step (2) is 0.02-0.15 mm, for example 0.05 mm, 0.08 mm, 0.10 mm, 0.12 mm, or 0.14 mm, etc.
The coated-film in step (2) can be prepared as a functional film according to the downstream application requirements.
As a preferred embodiment, the preparation method comprises the following steps:
(1) The raw materials of the substrate layer with formula amounts are fed into the hopper of a single screw extruder, while supercritical carbon dioxide under a pressure of 50-220 bar is charged in the middle of the single screw extruder at a flow rate of 0.10-2.50 kg/h. After extruding, a substrate layer having a density of 100-800 kg/m3 and a thickness of 0.5-10.0 mm is obtained. Wherein the host temperature of the single screw extruder during the extrusion process is less than or equal to 65°C, the extrusion temperature is 90-210°C, the rotational speed of the screw during the extrusion process is 1-100 rpm, and the bearing pressure range of the single screw extruder is 0-250 bar;
(2) The raw materials of the film layer with formula amounts are fed into the hopper of the single screw extruder, coated onto the surface of the substrate layer to form a film, and thereby a foam gasket having a covering film thickness of 0.02-0.15 mm is obtained. Wherein the extrusion temperature is 80-250°C, and the rotational speed of the screw during the extrusion process is 1-100 rpm.
Compared with the prior art, the present invention has the following beneficial effects:
The foam gasket provided by the present invention is composed of a substrate layer and a film layer. The substrate layer is made by foaming, and the cross-linking sealing property, flexibility, softness and elasticity thereof are better. The film covering the substrate layer makes the foam gasket possess good flexibility matching performance and meet sealing functional requirement. The Shore A hardness of the foam gasket is 35-50. The foam gasket has excellent sealing performance and good opening performance when used as a bottle cap gasket, and also has the effects of bonding and improving the flatness. In addition, the foam gasket is a food-grade plastic sheet.
The preparation method of the foam gasket provided by the present invention is simple and convenient for industrial application.
Embodiments
The technical solution of the present invention is further explained by combining with the following specific embodiments.
In the method of the following examples, the single screw extruder in step (1) is a single screw extruder having heating, cooling and pressure resistance performances—a foaming machine manufactured by Berstorff GmbH: 150-ISO-PAC.
In the following examples, the thickness of the film layer described as a certain number means that the thickness of the film layer on the upper surface of the substrate io layer and the thickness of the film layer on the lower surface of the substrate layer are independently a certain number.
Example 1
A foam gasket comprises a substrate layer and a film layer covering the upper and lower surfaces of the substrate layer. The substrate layer is a foam body and a uniform capillary pore body. The average pore diameter of the capillary pores is 1-30 pm. The film layer is a coated-film layer, and is uniform and compact. The substrate layer has a thickness of 0.5 mm. The film layer has a thickness of 0.02 mm.
The substrate layer is mainly prepared from the following raw materials in mass percent:
PE 90%
POE
9.7% release agent nucleating agent
0.2%
0.1%;
the release agent is selected from oleic acid amide;
the nucleating agent is selected from a masterbatch with sodium bicarbonate and citric acid as the main active ingredients and PE or PP or EVA as a carrier.
The film layer is mainly prepared from the following raw materials in mass percent:
PE
POE
93%
2.9% release agent
1.1% antiblocking agent
3.0%;
the thickener is selected from EEA (ethylene-ethyl acrylate);
the release agent is selected from oleic acid amide;
the antiblocking agent is selected from erucic acid amide.
The method for preparing the foam gasket comprises the following steps:
(1) The raw materials of the substrate layer with formula amounts were fed into the hopper of a single screw extruder, while supercritical carbon dioxide under a pressure of 50 bar was charged in the middle of the single screw extruder at a flow rate of 2.50 kg/h. After extruding and foaming, a substrate layer was obtained. Wherein the host temperature of the single screw extruder during the extrusion process was 65°C, the extrusion temperature was 210°C, the rotational speed of the screw during the extrusion process was 1 rpm, and the bearing pressure range of the single-screw extruder was 250 bar;
(2) The raw materials of the film layer with formula amounts were fed into the hopper of the single screw extruder, coated onto the surface of the substrate layer to form a film, and thereby a foam gasket having a covering film thickness of 0.02 mm was obtained. Wherein the extrusion temperature was 80°C, and the rotational speed of the screw during the extrusion process was 100 rpm.
Example 2
A foam gasket comprises a substrate layer and a film layer covering the upper and lower surfaces of the substrate layer. The substrate layer is a foam body and a uniform capillary pore body. The average pore diameter of the capillary pores is 50-100 pm. The film layer is a coated-film layer, and is uniform and compact. The substrate layer has a thickness of 10.0 mm. The film layer has a thickness of 0.15 mm.
The substrate layer is mainly prepared from the following raw materials in mass percent:
PP 90%
SBS 4.5% release agent 1.0% nucleating agent 2.5% color masterbatch 2.0%;
the release agent is selected from oleic acid amide and erucic acid amide.
Preferably, the nucleating agent is selected from a masterbatch with sodium bicarbonate and citric acid as the main active ingredients and PE or PP or EVA as a carrier.
The film layer is mainly prepared from the following raw materials in mass percent:
PP 95%
POE 3.7% thickener 1% release agent 0.2% antiblocking agent 0.1%;
the thickener is selected from EEA and polyester;
the release agent is selected from a masterbatch prepared from oleic acid amide and erucic acid amide with PE or PP as a carrier.
the antiblocking agent is selected from erucic acid amide.
The method for preparing the foam gasket comprises the following steps:
(1) The raw materials of the substrate layer with formula amounts were fed into the hopper of a single screw extruder, while supercritical carbon dioxide under a pressure of 220 bar was charged in the middle of the single screw extruder at a flow rate of 0.10 kg/h. After extruding and foaming, a substrate layer was obtained. Wherein the host temperature of the single screw extruder during the extrusion process was 50°C, the extrusion temperature was 90°C, the rotational speed of the screw during the extrusion process was 100 rpm, and the bearing pressure range of the single-screw extruder was 100 bar;
(2) The raw materials of the fdm layer with formula amounts were fed into the hopper of the single screw extruder, coated onto the surface of the substrate layer to form a fdm, and thereby a foam gasket having a covering fdm thickness of 0.15 mm was obtained. Wherein the extrusion temperature was 250°C, and the rotational speed of the screw during the extrusion process was 1 rpm.
Example 3
A foam gasket comprises a substrate layer and a fdm layer covering the upper and lower surfaces of the substrate layer. The substrate layer is a foam body and a uniform capillary pore body. The average pore diameter of the capillary pores is 30-80 pm. The fdm layer is a coated-fdm layer, and is uniform and compact. The substrate layer has a thickness of 5.0 mm. The film layer has a thickness of 0.10 mm.
The substrate layer is mainly prepared from the following raw materials in mass percent:
PE 50%
PP 26.5%
SEBS 20% release agent 0.5% nucleating agent 2.0% color masterbatch 1.0%;
the release agent is selected from erucic acid amide.
Preferably, the nucleating agent is selected from a masterbatch with sodium bicarbonate and citric acid as the main active ingredients and PE or PP or EVA as a carrier.
The film layer is mainly prepared from the following raw materials in mass percent:
PE 1%
PP 1%
POE 93% thickener 2% release agent E0% antiblocking agent 2.0%.
The thickener is selected from maleic anhydride grafted resin.
The release agent is selected from a masterbatch prepared from oleic acid amide and erucic acid amide with PE or PP as a carrier.
The antiblocking agent is selected from erucic acid amide.
The method for preparing the foam gasket comprises the following steps:
(1) The raw materials of the substrate layer with formula amounts were fed into the hopper of a single screw extruder, while supercritical carbon dioxide under a pressure of 100 bar was charged in the middle of the single screw extruder at a flow rate of 1.00 kg/h. After extruding and foaming, a substrate layer was obtained. Wherein the host temperature of the single screw extruder during the extrusion process was 60°C, the extrusion temperature was 120°C, the rotational speed of the screw during the extrusion process was 20 rpm, and the bearing pressure range of the single screw extruder was 120 bar;
(2) The raw materials of the film layer with formula amounts were fed into the hopper of the single screw extruder, coated onto the surface of the substrate layer to form a film, and thereby a foam gasket having a covering film thickness of 0.10 mm was obtained. Wherein the extrusion temperature was 100°C, and the rotational speed of the screw during the extrusion process was 20 rpm.
Example 4
A foam gasket comprises a substrate layer and a film layer covering the upper and lower surfaces of the substrate layer. The substrate layer is a foam body and a uniform capillary pore body. The average pore diameter of the capillary pores is 1-30 pm. The film layer is a coated-film layer, and is uniform and compact. The substrate layer has a thickness of 3.0 mm. The film layer has a thickness of 0.05 mm.
The substrate layer is mainly prepared from the following raw materials in mass percent:
PE 60%
PP 30%
POE and SBS with a mass ratio of 1:1 7% release agent 0.5% nucleating agent 1.5% color masterbatch 1.0%.
The release agent is selected from a masterbatch prepared from oleic acid amide and erucic acid amide with PE or PP as a carrier.
The nucleating agent is selected from a masterbatch with sodium bicarbonate and citric acid as the main active ingredients and PE or PP or EVA as a carrier.
The film layer is mainly prepared from the following raw materials in mass percent:
PE 18.5%
PP 30%
POE 20% thickener 30% release agent 0.5% antiblocking agent 1.0%.
Preferably, the thickener is selected from a combination of EEA, polyester and maleic anhydride grafted resin with a mass ratio of 1:1:1.
The release agent is selected from oleic acid amide.
The antiblocking agent is selected from erucic acid amide.
The method for preparing the foam gasket comprises the following steps:
(1) The raw materials of the substrate layer with formula amounts were fed into the hopper of a single screw extruder, while supercritical carbon dioxide under a pressure of 150 bar was charged in the middle of the single screw extruder at a flow rate of 2.0 kg/h. After extruding and foaming, a substrate layer was obtained. Wherein the host temperature of the single screw extruder during the extrusion process was 55°C, the extrusion temperature was 170°C, the rotational speed of the screw during the extrusion process was 80 rpm, and the bearing pressure range of the single-screw extruder was 150 bar;
(2) The raw materials of the film layer with formula amounts were fed into the hopper of the single screw extruder, coated onto the surface of the substrate layer to form a film, and thereby a foam gasket having a covering film thickness of 0.05 mm was obtained. Wherein the extrusion temperature was 180°C, and the rotational speed of the screw during the extrusion process was 90 rpm.
Example 5
A foam gasket comprises a substrate layer and a film layer covering the upper and lower surfaces of the substrate layer. The substrate layer is a foam body and a uniform capillary pore body. The average pore diameter of the capillary pores is 1-100 pm. The film layer is a coated-film layer, and is uniform and compact. The substrate layer has a thickness of 3.0 mm. The film layer has a thickness of 0.05 mm.
The substrate layer is mainly prepared from the following raw materials in mass percent:
PE 80%
PP 15%
POE 1% release agent 1.5% nucleating agent 1.5% color masterbatch 1%.
The release agent is selected from oleic acid amide.
The nucleating agent is selected from a masterbatch with sodium bicarbonate and citric acid as the main active ingredients and PE or PP or EVA as a carrier.
The film layer is mainly prepared from the following raw materials in mass percent:
PE 90%
PP 5%
POE 0.5% thickener 3.5% release agent 0.5% antiblocking agent 0.5%.
The thickener is selected from maleic anhydride grafted resin.
The release agent is selected from a masterbatch prepared from oleic acid amide and erucic acid amide with PE or PP as a carrier.
The antiblocking agent is selected from erucic acid amide.
The method for preparing the foam gasket comprises the following steps:
(1) The raw materials of the substrate layer with formula amounts were fed into the hopper of a single screw extruder, while supercritical carbon dioxide under a pressure of 150 bar was charged in the middle of the single screw extruder at a flow rate of 2.0 kg/h. After extruding and foaming, a substrate layer was obtained. Wherein the host temperature of the single screw extruder during the extrusion process was 55°C, the extrusion temperature was 170°C, the rotational speed of the screw during the extrusion process was 80 rpm, and the bearing pressure range of the single-screw extruder was 150 bar;
(2) The raw materials of the film layer with formula amounts were fed into the hopper of the single screw extruder, coated onto the surface of the substrate layer to form a film, and thereby a foam gasket having a covering film thickness of 0.05 mm was obtained. Wherein the extrusion temperature was 180°C, and the rotational speed of the screw during the extrusion process was 90 rpm.
Comparative Example 1
The product of comparative example 1 is the substrate layer prepared in Example 3.
Comparative Example 2
The product of comparative example 2 is a commercially available PE gasket (Manufacturer: Shanghai Mingyuan Plastic Products Co., Ltd).
Comparative Example 3
A foam gasket and its preparation method, which are the same as those in Example 5, except that the flow rate of supercritical carbon dioxide is 0.08 kg/h.
Comparative Example 4
A foam gasket and its preparation method, which are the same as those in Example 5, except that the flow rate of supercritical carbon dioxide is 2.60 kg/h.
The properties of the products obtained in Examples 1 to 5 and Comparative Examples 1 to 4 were tested. The test methods for density, flexibility, Shore hardness and sealability are respectively GB1033, perceptual test, GB2411, and self-made oil penetration method (a glass bottle filled with edible oil was sealed by a bottle cap made of the foam gaskets, and side-placed on a platform paved with a white paper. After 10 days, observation was carried out to confirm whether or not the oil was penetrated onto the white paper. If yes, it is not qualified; if not, it is qualified) The test results are shown in table 1.
Table 1
Density Flexibility Shore A hardness Sealability when used as a bottle cap
Example 1 300 g/L excellent 50 qualified
Example 2 288 g/L good 51 qualified
Example 3 425 g/L excellent 45 qualified
Example 4 403 g/L good 48 qualified
Example 5 389 g/L excellent 35 qualified
Comparati ve Example 1 305 g/L common 57 qualified
Comparati 297 g/L common 60 qualified
ve Example 2
Comparati ve Example 3 412 g/L common 65 qualified
Comparati ve Example 4 263 g/L common 62 qualified
It can be seen that the foam gasket provided by the present invention has excellent performances and is excellent in sealing performance as a bottle cap gasket. In addition, the present invention provides a foam gasket which meets food-grade requirements and can be widely used in high safety areas such as food packaging and pharmaceutical packaging and so on.
The applicant states that the present invention illustrates detailed methods of the present invention by the above examples, but the present invention is not limited to the above examples, that is to say, it does not mean that the present invention must be conducted relying on the above examples. Those skilled in the art should understand that any modification to the present invention, any equivalent replacement of each raw material of the products of the present invention and the addition of auxiliary ingredients, the selection of specific embodiment and the like all fall into the protection scope and the disclosure scope of the present invention.

Claims (12)

Claims
1. A foam gasket, characterized in that the foam gasket comprises a substrate layer and a film layer covering the upper and lower surfaces of the substrate layer; the substrate layer is a foam body and a uniform capillary pore body; the average pore diameter of the capillary pores is 1-100 pm;
the substrate layer is mainly prepared from the following raw materials in mass percent:
PE 0-90% PP 0-90% any one of POE, SBS or SEBS, or a combination of at least two of them 0-20% (not including 0)
release agent 0.2-1.0% nucleating agent 0.1-2.5% color masterbatch 0-2.0%;
wherein at most one substance of PE and PP has a mass percentage of zero;
the film layer is mainly prepared from the following raw materials in mass percent
PE 0-93%
PP 0-95% POE 0-93% thickener 0-30%
release agent
0.2-1.1% antiblocking agent 0.1 -3.0%;
wherein at most one substance of PE, PP and POE has a mass percentage of zero.
2. The foam gasket of claim 1, characterized in that the substrate layer is mainly prepared from the following raw materials in mass percent:
PE 80%
PP 15% any one of POE, SBS or SEBS, or a combination of at least two of them 1% release agent 1.0% nucleating agent 2.0% color masterbatch 1%.
3. The foam gasket of claim 1 or 2, characterized in that the release agent is any one selected from the group consisting of oleic acid amide, erucic acid amide, and masterbatch prepared from oleic acid amide and erucic acid amide with PE or PP as a carrier, or a combination of at least two of them.
4. The foam gasket of any one of claims 1-3, characterized in that the nucleating agent is selected from masterbatches with sodium bicarbonate and citric acid as the main active ingredients and PE or PP or EVA as a carrier.
5. The foam gasket of any one of claims 1-4, characterized in that the film layer is mainly prepared from the following raw materials in mass percent:
PE 90%
PP
5%
POE
0.5% thickener release agent antiblocking agent
3.5%
0.5%
0.5%;
preferably, the thickener is any one selected from the group consisting of EEA, polyester, and maleic anhydride grafted resin, or a combination of at least two of them;
preferably, the release agent is any one selected from the group consisting of oleic acid amide, erucic acid amide, and masterbatch prepared from oleic acid amide and erucic acid amide with PE or PP as a carrier, or a combination of at least two of them;
preferably, the antiblocking agent is selected from erucic acid amide.
6. The foam gasket of any one of claims 1-5, characterized in that the thickness of the substrate layer is 0.5 to 10.0 mm;
□ preferably, the density of the substrate layer is 100-800 kg/m ;
preferably, the thickness of the film layer is 0.02 to 0.15 mm.
7. A method for preparing the foam gasket of any one of claims 1-6, characterized in that the method comprises the following steps:
(1) The raw materials of the substrate layer with formula amounts are fed into the hopper of a single screw extruder, while supercritical carbon dioxide is charged in the middle of the single screw extruder; a substrate layer is obtained by extruding and foaming; the supercritical carbon dioxide is a supercritical carbon dioxide under a 25 pressure of 50 to 220 bar;
(2) The raw materials of the film layer with formula amounts are fed into the hopper of the single screw extruder, coated onto the surface of the substrate layer to form a film, and thereby the foam gasket is obtained.
8. The method of claim 7, characterized in that the host temperature of the single screw extruder during the extrusion process is less than or equal to 65°C;
preferably, the extrusion temperature in step (1) is 90-210°C;
preferably, the rotational speed of the screw during the extrusion process in step (1) is 1-100 rpm;
preferably, the bearing pressure range of the single screw extruder in step (1) is 0 to 250 bar.
9. The method of claim 7 or 8, characterized in that the flow rate of the supercritical carbon dioxide in step (1) is 0.10-2.50 kg/h;
preferably, the thickness of the substrate layer in step (1) is 0.5-10.0 mm;
□ preferably, the density of the substrate layer in step (1) is 100-800 kg/m .
10. The method of any one of claims 7-9, characterized in that the extrusion temperature in step (2) is 80-250°C;
preferably, the rotational speed of the screw during the extrusion process in step (2) is 1-100 rpm.
11. The method of any one of claims 7-10, characterized in that the thickness of the film covering the substrate layer in step (2) is 0.02-0.15 mm.
12. The method of any one of claims 7-11, characterized in that the method comprises the following steps:
(1) The raw materials of the substrate layer with formula amounts are fed into the hopper of a single screw extruder, while supercritical carbon dioxide under a pressure of 50-220 bar is charged in the middle of the single screw extruder at a flow rate of 0.10-2.50 kg/h; After extruding and foaming, a substrate layer having a density of 100-800 kg/m3 and a thickness of 0.5-10.0 mm is obtained; wherein the host temperature of the single screw extruder during the extrusion process is less than or equal to 65°C, the extrusion temperature is 90-210°C, the rotational speed of the screw during the extrusion process is 1-100 rpm, and the bearing pressure range of the single-screw extruder is 0-250 bar;
(2) The raw materials of the film layer with formula amounts are fed into the hopper of the single screw extruder, coated onto the surface of the substrate layer to form a film, and thereby a foam gasket having a covering film thickness of 0.02-0.15 mm is obtained; wherein the extrusion temperature is 80-250°C, and the rotational speed of the screw during the extrusion process is 1-100 rpm.
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Application No: Claims searched:
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GB2570873B (en) * 2018-02-01 2023-03-22 Douwe Egberts Bv Container lid and liner, and method of manufacturing the same
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FR3054974A1 (en) 2018-02-16
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