WO1987002680A2 - Polyamide packaging material - Google Patents

Polyamide packaging material Download PDF

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Publication number
WO1987002680A2
WO1987002680A2 PCT/JP1986/000542 JP8600542W WO8702680A2 WO 1987002680 A2 WO1987002680 A2 WO 1987002680A2 JP 8600542 W JP8600542 W JP 8600542W WO 8702680 A2 WO8702680 A2 WO 8702680A2
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WO
WIPO (PCT)
Prior art keywords
polyamide
acid
packaging material
layer
gas barrier
Prior art date
Application number
PCT/JP1986/000542
Other languages
French (fr)
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WO1987002680A3 (en
Inventor
Seiichi Yamashiro
Tooru Matsubayashi
Kouichi Sakai
Hiroshi Toyao
Original Assignee
Teijin Limited
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from JP60244111A external-priority patent/JPS62109738A/en
Priority claimed from JP24411085A external-priority patent/JPS62106926A/en
Application filed by Teijin Limited filed Critical Teijin Limited
Publication of WO1987002680A2 publication Critical patent/WO1987002680A2/en
Priority to KR870700567A priority Critical patent/KR880700003A/en
Publication of WO1987002680A3 publication Critical patent/WO1987002680A3/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G69/00Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/02Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
    • C08G69/26Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from polyamines and polycarboxylic acids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/06Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/08Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/34Layered products comprising a layer of synthetic resin comprising polyamides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/36Layered products comprising a layer of synthetic resin comprising polyesters
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G69/00Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/02Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
    • C08G69/26Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from polyamines and polycarboxylic acids
    • C08G69/265Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from polyamines and polycarboxylic acids from at least two different diamines or at least two different dicarboxylic acids
    • 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
    • B32B2307/724Permeability to gases, adsorption
    • B32B2307/7242Non-permeable
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2367/00Polyesters, e.g. PET, i.e. polyethylene terephthalate
    • 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
    • B32B2377/00Polyamides
    • 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
    • B32B2439/00Containers; Receptacles
    • B32B2439/70Food packaging

Definitions

  • the present invention relates to a packaging material made of a polyamide, more particularly, it relates to a packaging material made of a copolymerized polyamide having excellent gas barrier properties, strength and heat resistance.
  • a material having high gas barrier properties is required in packaging, especially in food packaging to elongate the shelf life of the food or to keep the freshness of the food.
  • a packaging material having excellent oxgen barrier property is desired to prevent the progress of the deterioration of the food caused by the transmission of oxygen.
  • a packaging material having excellent barrier property to carbon dioxide gas is desired for the container of a carbonated beverage, etc. to keep its refreshness.
  • Various materials have been developed to meet the above requirements, for example, polyvinylidene chloride, ethylene-vinyl alcohol copolymer, polyamide, polyethylene terephthalate, etc., and various methods have been proposed.
  • a gas barrier material such as polyvinylidene chloride or a saponified ethylene/vinyl acetate copolymer (vide; Japanese Unexamined Patent Publications No. 117565/79 and No.
  • a further object of the present invention is to provide a packaging material suitable for a multi-layer structure composed of the polyamide component and polyethylene terephthalate component.
  • This invention is directed to a polyamide packaging material exellent in the resistance to the permeation of oxygen and carbon oxide gases, which comprises a copolymerized polyamide comprising tetramethylene adipamide unit and tetramethylene isophthalamide unit.
  • a copolymerized polyamide comprising tetramethylene adipamide unit and tetramethylene isophthalamide unit.
  • Best Mode of Carrying out the Invention Copolymerized polyamide valuably used for the packaging material of the present invention comprises 10 to 90 mole% of tetramethylene adipamide units and 90 to 10 mole% of tetramethylene isophthalamide units. It has been unexpectedly found that by copolymerizing polytetramethylene adipamide with the isophthalic acid, the gas barrier property is highly improved as well as moldability.
  • the ratio of tetramethylene adipamide unit and tetramethylene isophthalamide unit is preferably 20:80 to 80:20.
  • the copolymerized polyamide layer having a tetramethylene adipamide content of not more than 90 has a rate of crystallization suitable for the drawing or stretching of said multi- layer structure.
  • the ratio of tetramethylene adipamide unit exceeds 90, the rate of crystallization of the polymer becomes extremely high, and the clouding phenomenon tends to occur in the obtained molded article such as preform.
  • the preform comprising the multi-layer structure above-mentioned must be preheated at the vicinity of 150°C in the drawing step, therefore, the clouding or crystallization of polyethylene terephthalate layer cannot be avoided.
  • the copolymerized polyamide may comprises other comonomer component, so far as the characteristic properties are not degraded.
  • the polyamide of the present invention contains other comonomer units in an amount of less than 20% of the whole recurring units, and a part of the tetramethylenediamine and a part of adipic acid or isophthalic acid are substituted with one or more kinds of other diamines, aminocarboxylic acids, lactam or dicarboxylic acids.
  • the comonomer components are aliphatic diamines such as ethylenediamide, trimethylenediamine, hexamethylenediamine, etc.; aromatic diamines such as phenylenediamine, xylylene- diamine, 3,6-diaminoacridine, N-methyl-p-phenylenediamine, N,N-dimethyl-p-phenylenediamine, tolylenediamine, etc.; alicyclic diamines such as 1,2-diaminocylobutane, etc.; aliphatic aminocarboxylic acids such as glycine, alanine, valine, etc.; aromatic aminocarboxylic acids such as phenylalanine, amino- benzoic acid, etc.; alicyclic aminocarboxylic acids such as aminocyclohexanecarboxylic acid, etc.; lactam such as ⁇ propiolactam, r-butyrolactam, ⁇ -caprolactam
  • the relative viscosity (r)rel; 1.0 wt% solution using 96% sulfuric acid as the solvent; measured at 20°C) of the polyamide of the present invention is preferably 2.0 or higher from the viewpoint of the strength of the obtained film or article.
  • the copolymerized polyamide can be produced by the conventional method known as the process for the production of polyamide. For example, it can be produced by condensing tetramethylenediamine with isophthalic acid, and tetramethylenediamine with adipic acid to form respective salts, and subjecting the resultant reaction product to the polycondensation reaction.
  • Various polycondensation catalysts, stabilizers, etc. can be used in the above production process. If necessary, other additives such as colorants fluorescent blighteners, oxidation stabilizers, ultraviolet absorbing agents, antistatic agents, flameretardants, etc. may be used in the process.
  • the polyamide packaging material of the present invention is, for example, a film and a container such as bottle, cup, etc. produced by a molding method accompanying with the drawing process.
  • the film or the sheet can be manufactured by the conventional methods known as the film-forming or sheet- forming methods.
  • the resin is dried at a temperature not lower than 80°C for 30 minutes of more, melted and extruded with an extruder furnished with a T-die or I-die, etc., and quenched to obtain an undrawn film or sheet, which may be further drawn along uniaxial or biaxial directions to obtain a drawn film or sheet.
  • the polyamide packaging material of the present invention is used for one component of a multi-layer structure.
  • the multi-layer structure comprises a layer of self-supportable polymer component, such as polyethylene terephthalate, and a layer of the copolymerized polyamide component.
  • the weight ratio of the copolymerized polyamide layer is preferably 5 to 50 wt%, especially 10 to 30 wt% to keep the physical properties and to attain high gas barrier properties of the obtained multi-layer drawn polyester sheet or bottle. Any combination of two of more polymers including the copolymerized polyamide may have an integral structure of a polymer-blend. The integral structure has also excellent gas barrier properties.
  • the polyethylene terephthalate that can be used in combination with the polyamide packaging material of the present invention is a polyester comprising at least 80 mole% of ethylene terephthalate units based on the total recurring units.
  • a part of the terephthalic acid component may be replaced by at least one member selected from bifunctional carboxylic acids; for example; aromatic dicarboxylic acids such as isophthalic acid, naphthalenedicarboxylic acid, diphenyldicarboxylic acid, diphenoxyethanedicarboxylic acid, diphenyl etherdicarboxylic acid, diphenylsulfonedicarboxylic acid; alicyclic carboxylic acids such as hexahydroterephthalic acid and hexahydroisophthalic acid; aliphatic dicarboxylic acids such as adipic acid, sebacic acid, and azelaic acid; and hydroxyacids such as p- ⁇ -hydroxyethoxybenzoic acid,
  • the packaging material of the present invention there can be mentioned a container formed by the molding method including the drawing steps, such as a cup or bottle. Furthermore, the material may be a container obtained by the deep drawing of undrawn laminated sheet or a container obtained by drawing a bottom-closed laminated pipe. Moreover, a tray manufactured by the vaccum forming or the air pressure forming of a sheet is one of embodiments of the present invention.
  • the multi-layer drawn bottle of the present invention is manufactured basically by the hitherto developed process for the forming of polyester bottles, that is, by the process comprising the forming of a multi-layer preform and the orientation blow-molding of the preform.
  • the multi-layer preform can be formed e.g. by forming a multi-layer pipe composed of a polyetylene terephthalate layer and a copolymerized polyamide layer by the multi-layer co-extrusion technique, cutting the pipe to a prescribed length, and forming both ends in the desired forms of mouth and bottom by thermal forming.
  • a preform having multi-layer structure can be manufactured by the multi-layer injection molding process wherein the copolymerized polyamide is injected successively to the inner surface, outer surface or between the layers of polyethylene terephthalate.
  • the draw ratio of the bottle at the barrel portion in the drawing of the blow expansion of the multi-layer preform is preferably 1.2 or more, especially 2 or more in terms of areal ratio.
  • the packaging material of the present invention made of a polyamide has excellent gas barrier properties.
  • the carbon dioxide gas permeability constant of the material is 1/5 to 1/10 of that of nylon 6 and accordingly the material is extremely useful for the packaging of a material to which high gas barrier properties are especially required.
  • an advantage of the present invention is that a multi-layer structure having good processability is prepared by using the conventional methods and equipments.
  • nylon 46 A polytetramethylene adipamide (hereinafter referred to as nylon 46) having an rel of 3.5 was prepared from tetramethylenediamine and adipic acid according to the method disclosed in the specification of Japanese Patent Unexamined Publication No. 149430/81.
  • the nylon 46 was dried by a vacuum drier at 100°C for 24 hours, and a single-layer film having a thickness of about 100 ⁇ m was manufactured by using a 30mm-diameter extruder at cylinder temperature of 300°C and a casting roll temperature of about 20°C.
  • the obtained film had an opaque white appearance.
  • nylon 46 has excellent gas barrier properties, however, nylon 46 is not formed into a transparent film. Examples 1 and 2, Comparative Examples 4 and 5
  • Polyamides were prepared by the polycondensation of tetramethylenediamine, adipic acid and isophthalic acid. The rel, appearances and gas barrier properties of the polyamides are shown in Table 2.
  • PET Polyethylene terephthalate
  • the copolymerized polyamide shown in the table 3 was dried at 100°C for 24 hours in vacuum.
  • the polyethylene terephthalate and the polyamide were supplied to the cylinders A and B of the ASB-50EX-T-type one-stage multilayer biaxial orientation stretch blow-molding machine made by Nissei ASB Machine Co.
  • a preform having a weight ratio of the intermediate layer of 20 wt% was manufactured by this process.
  • the preform had a cylindrical form closed at one end and having an outer diameter of 25 to 26 mm, a thickness of 3.5 mm and a total length of 155 mm.
  • the preform was pre-heated at a temperature of 120 to
  • the preform was drawn axially in a bottle-shaped mold and expanded laterally with compressed air to form a bottle having an outer body diameter of 82 mm, a total height of 280 mm, a barrel portion thickness of 250 to 360 ⁇ m , and an inner volume of 1040 - 1050 ml.
  • the drawability (blow-moldability) of the preform in the above procedure and the gas barrier properties measured by using the test pieces prepared by cutting the barrel of the bottle are shown in the table 3.
  • Preforms were manufactured by using the copolymerized polyamide used in the Example 4, by the method similar to the Example 4 except for the thickness relationship between the polyamide layer and the PET layer, which was varied in a manner shown in the table 4, and the drawabilities and the gas barrier properties of the preforms were measured.
  • the bottle of the present invention has excellent moldability and gas barrier properties.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Laminated Bodies (AREA)
  • Polyamides (AREA)

Abstract

A polyamide packaging material comprises a copolymerized polyamide comprising 10 to 90 mole% of tetramethylene adipamide units and 90 to 10 mole% of tetramethylene isophthalamide units. The copolymerized polyamide has excellent gas barrier properties and good moldability.

Description

SPECIFICATION Title of the Invention
Polyamide Packaging Material Technical Field The present invention relates to a packaging material made of a polyamide, more particularly, it relates to a packaging material made of a copolymerized polyamide having excellent gas barrier properties, strength and heat resistance. Background Art
A material having high gas barrier properties is required in packaging, especially in food packaging to elongate the shelf life of the food or to keep the freshness of the food. For example, in the case of packaging a food containing an oleaginous component, a packaging material having excellent oxgen barrier property is desired to prevent the progress of the deterioration of the food caused by the transmission of oxygen.
Furthermore, a packaging material having excellent barrier property to carbon dioxide gas is desired for the container of a carbonated beverage, etc. to keep its refreshness. Various materials have been developed to meet the above requirements, for example, polyvinylidene chloride, ethylene-vinyl alcohol copolymer, polyamide, polyethylene terephthalate, etc., and various methods have been proposed. For example, there have been proposed a method in which a polymer film is coated or laminated with a gas barrier material such as polyvinylidene chloride or a saponified ethylene/vinyl acetate copolymer (vide; Japanese Unexamined Patent Publications No. 117565/79 and No. 64839/81), and a method in which a polyester is blended with a gas barrier material (European Unexamined Patent 105826). To satisfy various requirements other than gas barrier properties such as mechanical strength, moisture permeability, weathering resistance, etc., an article composed of two or more polymers is formed or converted to a multi-layer structure by co- extrusion or co-injection technique. Among the above-mentioned materials, polyamide has excellent processability, heat resistance and strength, and is used widely as a packaging material; however, the gas barrier properties of nylon 6 and nylon 66 are not necessarily sufficient, and the developement of a new material having further excellent gas barrier properties is wanted. Disclosure of Invention
It is a primary object of the present invention to provide a polyamide packaging material which is excellent moldability and gas barrier properties. A further object of the present invention is to provide a packaging material suitable for a multi-layer structure composed of the polyamide component and polyethylene terephthalate component.
This invention is directed to a polyamide packaging material exellent in the resistance to the permeation of oxygen and carbon oxide gases, which comprises a copolymerized polyamide comprising tetramethylene adipamide unit and tetramethylene isophthalamide unit. Best Mode of Carrying out the Invention Copolymerized polyamide valuably used for the packaging material of the present invention comprises 10 to 90 mole% of tetramethylene adipamide units and 90 to 10 mole% of tetramethylene isophthalamide units. It has been unexpectedly found that by copolymerizing polytetramethylene adipamide with the isophthalic acid, the gas barrier property is highly improved as well as moldability.
The ratio of tetramethylene adipamide unit and tetramethylene isophthalamide unit is preferably 20:80 to 80:20. In a case of manufacturing a multi-layer structure comprising a polyethylene terephthalate layer and a polyamide layer, the copolymerized polyamide layer having a tetramethylene adipamide content of not more than 90 has a rate of crystallization suitable for the drawing or stretching of said multi- layer structure. In other words, when the ratio of tetramethylene adipamide unit exceeds 90, the rate of crystallization of the polymer becomes extremely high, and the clouding phenomenon tends to occur in the obtained molded article such as preform. On the other hand, when the ratio of tetramethylene isophthalamide content exceeds 90, the preform comprising the multi-layer structure above-mentioned must be preheated at the vicinity of 150°C in the drawing step, therefore, the clouding or crystallization of polyethylene terephthalate layer cannot be avoided. The copolymerized polyamide may comprises other comonomer component, so far as the characteristic properties are not degraded. Accordingly, the polyamide of the present invention contains other comonomer units in an amount of less than 20% of the whole recurring units, and a part of the tetramethylenediamine and a part of adipic acid or isophthalic acid are substituted with one or more kinds of other diamines, aminocarboxylic acids, lactam or dicarboxylic acids. For example, the comonomer components are aliphatic diamines such as ethylenediamide, trimethylenediamine, hexamethylenediamine, etc.; aromatic diamines such as phenylenediamine, xylylene- diamine, 3,6-diaminoacridine, N-methyl-p-phenylenediamine, N,N-dimethyl-p-phenylenediamine, tolylenediamine, etc.; alicyclic diamines such as 1,2-diaminocylobutane, etc.; aliphatic aminocarboxylic acids such as glycine, alanine, valine, etc.; aromatic aminocarboxylic acids such as phenylalanine, amino- benzoic acid, etc.; alicyclic aminocarboxylic acids such as aminocyclohexanecarboxylic acid, etc.; lactam such asβpropiolactam, r-butyrolactam, ε-caprolactam, etc.; aromatic dicarboxylic acids such as terephthalic acid, naphthalenedicarboxylic acid, diphenyldicarboxylic acid, diphenoxyethanedicarboxylic acid, diphenyl ether dicarboxylic acid, diphenyl sulfone dicarboxylic acid, diphenyl ketone dicarboxylic acid, sodium-sulfoisophthalic acid, dibromoterephthalic acid, etc.; alicyclic dicarboxylic acids such as decalinedicarboxylic acid, etc.; and aliphatic dicarboxylic acids such as succinic acid, sebacic acid, etc.
The relative viscosity (r)rel; 1.0 wt% solution using 96% sulfuric acid as the solvent; measured at 20°C) of the polyamide of the present invention is preferably 2.0 or higher from the viewpoint of the strength of the obtained film or article. The copolymerized polyamide can be produced by the conventional method known as the process for the production of polyamide. For example, it can be produced by condensing tetramethylenediamine with isophthalic acid, and tetramethylenediamine with adipic acid to form respective salts, and subjecting the resultant reaction product to the polycondensation reaction. Various polycondensation catalysts, stabilizers, etc. can be used in the above production process. If necessary, other additives such as colorants fluorescent blighteners, oxidation stabilizers, ultraviolet absorbing agents, antistatic agents, flameretardants, etc. may be used in the process.
The polyamide packaging material of the present invention is, for example, a film and a container such as bottle, cup, etc. produced by a molding method accompanying with the drawing process.
The film or the sheet can be manufactured by the conventional methods known as the film-forming or sheet- forming methods. For example, the resin is dried at a temperature not lower than 80°C for 30 minutes of more, melted and extruded with an extruder furnished with a T-die or I-die, etc., and quenched to obtain an undrawn film or sheet, which may be further drawn along uniaxial or biaxial directions to obtain a drawn film or sheet. Furthermore, the polyamide packaging material of the present invention is used for one component of a multi-layer structure. The multi-layer structure comprises a layer of self-supportable polymer component, such as polyethylene terephthalate, and a layer of the copolymerized polyamide component. A double-layer structure wherein the inner layer is a polyethylene terephthalate layer and the outer layer is a copolymerized polyamide layer, a triple-layer structure wherein the inner and the outer layers are polyethylene terephthalate layers and the intermediate layer is made of the copolymerized polyamide, and the five-layer structure corresponding to the above triple-layer structure containing two adhesive interlayers inserted between the above three layers are preferable. The weight ratio of the copolymerized polyamide layer is preferably 5 to 50 wt%, especially 10 to 30 wt% to keep the physical properties and to attain high gas barrier properties of the obtained multi-layer drawn polyester sheet or bottle. Any combination of two of more polymers including the copolymerized polyamide may have an integral structure of a polymer-blend. The integral structure has also excellent gas barrier properties.
The polyethylene terephthalate that can be used in combination with the polyamide packaging material of the present invention is a polyester comprising at least 80 mole% of ethylene terephthalate units based on the total recurring units. A part of the terephthalic acid component may be replaced by at least one member selected from bifunctional carboxylic acids; for example; aromatic dicarboxylic acids such as isophthalic acid, naphthalenedicarboxylic acid, diphenyldicarboxylic acid, diphenoxyethanedicarboxylic acid, diphenyl etherdicarboxylic acid, diphenylsulfonedicarboxylic acid; alicyclic carboxylic acids such as hexahydroterephthalic acid and hexahydroisophthalic acid; aliphatic dicarboxylic acids such as adipic acid, sebacic acid, and azelaic acid; and hydroxyacids such as p-β-hydroxyethoxybenzoic acid, p-hydroxybenzoic acid, and ε-hydroxycaproic acid, and/or a part of the ethylene glycol component may be replaced by at least one member selected from other glycols such as trimethylene glycol, tetramethylene glycol, hexamethylene glycol, decamethylene glycol, neopentyl glycol, diethylene glycol, 1,1- cyclohexane dimethylol, 1,4-cyclohexane dimethylol, 2,2- bis (4-β-hydroxyethoxyphenyl) propane, and bis(4-β-hydroxy- ethoxyphenyl)sulfone, and these copolyesters may be used as the polyethylene terephthalate so long as the above-mentioned requirement of the content of ethylene terephthalate units is satisfied. In view of the mechanical properties, preferably the inherent viscosity
Figure imgf000009_0001
of the polyethylene terephthalate is at least 0.5, especially at least 0.6, as measured in ochlorophenol as the solvent at 35°C.
As the packaging material of the present invention, there can be mentioned a container formed by the molding method including the drawing steps, such as a cup or bottle. Furthermore, the material may be a container obtained by the deep drawing of undrawn laminated sheet or a container obtained by drawing a bottom-closed laminated pipe. Moreover, a tray manufactured by the vaccum forming or the air pressure forming of a sheet is one of embodiments of the present invention.
The multi-layer drawn bottle of the present invention is manufactured basically by the hitherto developed process for the forming of polyester bottles, that is, by the process comprising the forming of a multi-layer preform and the orientation blow-molding of the preform. The multi-layer preform can be formed e.g. by forming a multi-layer pipe composed of a polyetylene terephthalate layer and a copolymerized polyamide layer by the multi-layer co-extrusion technique, cutting the pipe to a prescribed length, and forming both ends in the desired forms of mouth and bottom by thermal forming. As an alternative method, a preform having multi-layer structure can be manufactured by the multi-layer injection molding process wherein the copolymerized polyamide is injected successively to the inner surface, outer surface or between the layers of polyethylene terephthalate. The draw ratio of the bottle at the barrel portion in the drawing of the blow expansion of the multi-layer preform is preferably 1.2 or more, especially 2 or more in terms of areal ratio.
The packaging material of the present invention made of a polyamide has excellent gas barrier properties. For example, the carbon dioxide gas permeability constant of the material is 1/5 to 1/10 of that of nylon 6 and accordingly the material is extremely useful for the packaging of a material to which high gas barrier properties are especially required.
Furthermore, gas barrier properties of nylon 6, nylon 66 and polytetramethylene adipamide become poor in the presence of water, whereas the copolymerized polyamide of the present invention retains sufficient resistance to gas permeation under high humidity environment. Moreover, an advantage of the present invention is that a multi-layer structure having good processability is prepared by using the conventional methods and equipments.
The present invention will now be described in detail with reference to the following examples. The properties mentioned in the examples are measured according to the following methods.
(a) Relative viscosity Qrel) of the polyamide
Figure imgf000011_0001
Measured at 20°C using 96% sulfuric acid at 1.0 wt% concentration.
(b) Intrinsic viscosity of the thermoplastic polyester Measured at 35°C using o-chlorophenol as the solvent.
(c) Oxygen gas permeability constant (Po2) and carbon dioxide gas permeability constant (Pco2) The transmission rates of oxygen gas and carbon dioxide gas were measure at 30°C by a GPM-200-type gas permeability tester (product of Lyssy Co., Switzerland) using a mixture of O2 and CO2 at a volume ratio (O2/CO2) of 80/20. Comparative Examples 1 through 3
A polytetramethylene adipamide (hereinafter referred to as nylon 46) having an
Figure imgf000011_0002
rel of 3.5 was prepared from tetramethylenediamine and adipic acid according to the method disclosed in the specification of Japanese Patent Unexamined Publication No. 149430/81. The nylon 46 was dried by a vacuum drier at 100°C for 24 hours, and a single-layer film having a thickness of about 100 μ m was manufactured by using a 30mm-diameter extruder at cylinder temperature of 300°C and a casting roll temperature of about 20°C.
The obtained film had an opaque white appearance.
For comparison, films of nylon 6 (
Figure imgf000012_0001
= 1.2) and nylon 66 ( = 1.3) were manufactured by similar methods.
The results obtained by the measurement of the gas barrier properties of these films are shown in Table 1.
Figure imgf000012_0002
It can be seen from Table 1 that nylon 46 has excellent gas barrier properties, however, nylon 46 is not formed into a transparent film. Examples 1 and 2, Comparative Examples 4 and 5
Polyamides were prepared by the polycondensation of tetramethylenediamine, adipic acid and isophthalic acid. The rel, appearances and gas barrier properties of the polyamides are shown in Table 2.
Figure imgf000013_0001
Examples 3 through 5 and Comparative Examples 6 through 10
Polyethylene terephthalate (hereinafter abbreviated as PET) having an intrinsic viscosity of 0.74 was dried at 160°C for 5 hours with hot air. Separately, the copolymerized polyamide shown in the table 3 was dried at 100°C for 24 hours in vacuum. The polyethylene terephthalate and the polyamide were supplied to the cylinders A and B of the ASB-50EX-T-type one-stage multilayer biaxial orientation stretch blow-molding machine made by Nissei ASB Machine Co. Ltd., respectively, and were injected by the co-injection molding into a mold cooled with cooling water of 15°C while setting the temperature of the cylinder A at 260 to 280°C and that of the cylinder B (for intermediate layer) at 240 to 300°C. A preform having a weight ratio of the intermediate layer of 20 wt% was manufactured by this process. The preform had a cylindrical form closed at one end and having an outer diameter of 25 to 26 mm, a thickness of 3.5 mm and a total length of 155 mm. The preform was pre-heated at a temperature of 120 to
150°C, the preform was drawn axially in a bottle-shaped mold and expanded laterally with compressed air to form a bottle having an outer body diameter of 82 mm, a total height of 280 mm, a barrel portion thickness of 250 to 360 μm , and an inner volume of 1040 - 1050 ml. The drawability (blow-moldability) of the preform in the above procedure and the gas barrier properties measured by using the test pieces prepared by cutting the barrel of the bottle are shown in the table 3.
Figure imgf000015_0001
In the preheating step the polyethylene terephthalate outer layer of the preform of Comparative Example 9 got clouding and the obtained bottle (drawn preform) gave nonuniform wall thickness after drawing the partially crystallized preform. Examples 6 through 8
Preforms were manufactured by using the copolymerized polyamide used in the Example 4, by the method similar to the Example 4 except for the thickness relationship between the polyamide layer and the PET layer, which was varied in a manner shown in the table 4, and the drawabilities and the gas barrier properties of the preforms were measured.
The results are shown in the table 4.
It can be seen also from the table 4 that the bottle of the present invention has excellent moldability and gas barrier properties.
Figure imgf000016_0001
PCT WORLD INTELLECTUAL PROPERTY ORGANIZATION
International Bureau
Figure imgf000018_0001
INTERNATIONAL APPLICATION PUBLISHED UNDER THE PATENT COOPERATION TREATY (PCT)
Figure imgf000018_0002
FOR THE PURPOSES OFINFORMAπON ONLY
Codes used to identify Statesparty to thePCTonthe frontpages of pamphlets publishing interaationalappli- cations under the PCT.
AT Austria FR France ML Mali
AU Australia GA Gabon MR Mauritania
BB Barbados GB United Kingdom MW Malawi
BE Belgium HU Hungary NL Netherlands
BG Bulgaria IT Italy NO Norway
BJ Benin JP Japan RO Romania
BR Brazil KP Democratic People'* Republic SD Sudan
CF Central African Republic of Korea SE Sweden
CG Congo KR Republic of Korea S.N Senegal
CH Switzerland LI Liechtenstein SU Soviet Union
CM Cameroon LK Sri Lanka TD Chad
DE Germany, Fed eral Republic of LU Luxembourg TG Togo
DK Denmark MC Monaco US United States of America
FI Finland MG Madagascar

Claims

1. A polyamide packaging material excellent in the resistance to the permeation of gases, which comprises a copolymerized polyamide comprising 10 to 90 mole% of tetramethylene adipamide units and 90 to 10 mole% of tetramethylene isophthalamide units.
2. A packaging material comprises a component of polyethylene terephthalate and a component of copolymerized polyamide comprising 10 to 90 mole% of tetramethylene adipamide units and 90 to 10 mole% of tetramethylene isophthalamide units.
3. A packaging material as set forth in claim 2, wherein the polyethylene terephthalate component and the copolymerized polyamide component are formed into a multi-layer structure.
4. A packaging material as set forth in claim 2, wherein the polyethylene terephthalate component and the copolymerized polyamide component are blended and formed into an integral structure.
PCT/JP1986/000542 1985-11-01 1986-10-28 Polyamide packaging material WO1987002680A2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR870700567A KR880700003A (en) 1985-11-01 1987-06-30 Polyamide packaging material

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP60/244110 1985-11-01
JP60244111A JPS62109738A (en) 1985-11-01 1985-11-01 Multilayer oriented polyester bottle
JP24411085A JPS62106926A (en) 1985-11-01 1985-11-01 Polyamide packaging material
JP60/244111 1985-11-01

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WO1987002680A2 true WO1987002680A2 (en) 1987-05-07
WO1987002680A3 WO1987002680A3 (en) 1988-03-24

Family

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EP (1) EP0247203A1 (en)
KR (1) KR880700003A (en)
WO (1) WO1987002680A2 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0288972A2 (en) * 1987-04-27 1988-11-02 Mitsubishi Gas Chemical Company, Inc. Gas-barrier multilayered structure
EP0542184A1 (en) * 1991-11-14 1993-05-19 Hüls Aktiengesellschaft Multilayered plastic pipe
EP0542185A1 (en) * 1991-11-14 1993-05-19 Hüls Aktiengesellschaft Multilayered plastic pipe
EP0411709B1 (en) * 1989-08-05 1994-06-01 Dsm N.V. Polyamide composition
WO2006047776A2 (en) * 2004-10-27 2006-05-04 E.I. Dupont De Nemours And Company Marine umbilical comprising hydrolysis resistant polyamides
WO2006047774A1 (en) * 2004-10-27 2006-05-04 E.I. Dupont De Nemours And Company Multilayered pipes comprising hydrolysis resistant polyamides
CN103619956A (en) * 2011-06-27 2014-03-05 三菱瓦斯化学株式会社 Injection-molded body
CN103635538A (en) * 2011-06-27 2014-03-12 三菱瓦斯化学株式会社 Film and film packaging container
EP2724860A1 (en) * 2011-06-27 2014-04-30 Mitsubishi Gas Chemical Company, Inc. Multilayer injection-molded body

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4229340A (en) * 1979-08-27 1980-10-21 Celanese Corporation Glass fiber-reinforced polyethylene terephthalate/polyamide blends
EP0077106A1 (en) * 1981-10-13 1983-04-20 Stamicarbon B.V. Process for making polytetramethyleneadipamide

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4229340A (en) * 1979-08-27 1980-10-21 Celanese Corporation Glass fiber-reinforced polyethylene terephthalate/polyamide blends
EP0077106A1 (en) * 1981-10-13 1983-04-20 Stamicarbon B.V. Process for making polytetramethyleneadipamide

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0288972A2 (en) * 1987-04-27 1988-11-02 Mitsubishi Gas Chemical Company, Inc. Gas-barrier multilayered structure
EP0288972A3 (en) * 1987-04-27 1989-11-15 Mitsubishi Gas Chemical Company, Inc. Gas-barrier multilayered structure
EP0411709B1 (en) * 1989-08-05 1994-06-01 Dsm N.V. Polyamide composition
EP0542184A1 (en) * 1991-11-14 1993-05-19 Hüls Aktiengesellschaft Multilayered plastic pipe
EP0542185A1 (en) * 1991-11-14 1993-05-19 Hüls Aktiengesellschaft Multilayered plastic pipe
US5404915A (en) * 1991-11-14 1995-04-11 Huels Aktiengesellschaft Multilayer plastic pipe
US5425817A (en) * 1991-11-14 1995-06-20 Huels Aktiengesellschaft Multilayer plastic pipe with polyamide inner and outer layers and a linear crystalline polyester intermediate layer
WO2006047776A2 (en) * 2004-10-27 2006-05-04 E.I. Dupont De Nemours And Company Marine umbilical comprising hydrolysis resistant polyamides
WO2006047774A1 (en) * 2004-10-27 2006-05-04 E.I. Dupont De Nemours And Company Multilayered pipes comprising hydrolysis resistant polyamides
WO2006047776A3 (en) * 2004-10-27 2006-06-01 Du Pont Marine umbilical comprising hydrolysis resistant polyamides
CN103619956A (en) * 2011-06-27 2014-03-05 三菱瓦斯化学株式会社 Injection-molded body
CN103635538A (en) * 2011-06-27 2014-03-12 三菱瓦斯化学株式会社 Film and film packaging container
EP2725066A1 (en) * 2011-06-27 2014-04-30 Mitsubishi Gas Chemical Company, Inc. Film and film packaging container
EP2724860A1 (en) * 2011-06-27 2014-04-30 Mitsubishi Gas Chemical Company, Inc. Multilayer injection-molded body
EP2725065A1 (en) * 2011-06-27 2014-04-30 Mitsubishi Gas Chemical Company, Inc. Injection-molded body
EP2725066A4 (en) * 2011-06-27 2014-12-03 Mitsubishi Gas Chemical Co Film and film packaging container
EP2725065A4 (en) * 2011-06-27 2014-12-03 Mitsubishi Gas Chemical Co Injection-molded body
EP2724860A4 (en) * 2011-06-27 2015-01-28 Mitsubishi Gas Chemical Co Multilayer injection-molded body
US9718955B2 (en) 2011-06-27 2017-08-01 Mitsubishi Gas Chemical Company, Inc. Injection-molded body
US9731482B2 (en) 2011-06-27 2017-08-15 Mitsubishi Gas Chemical Company, Inc. Multilayer injection-molded body

Also Published As

Publication number Publication date
WO1987002680A3 (en) 1988-03-24
KR880700003A (en) 1988-02-15
EP0247203A1 (en) 1987-12-02

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