Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
  • B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/16—Layered products comprising a layer of synthetic resin specially treated, e.g. irradiated
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/18—Layered products comprising a layer of synthetic resin characterised by the use of special additives
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/18—Layered products comprising a layer of synthetic resin characterised by the use of special additives
  • B32B27/20—Layered products comprising a layer of synthetic resin characterised by the use of special additives using fillers, pigments, thixotroping agents
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/30—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
  • B32B27/306—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers comprising vinyl acetate or vinyl alcohol (co)polymers
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/34—Layered products comprising a layer of synthetic resin comprising polyamides
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/36—Layered products comprising a layer of synthetic resin comprising polyesters
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B7/00—Layered products characterised by the relation between layers; Layered products characterised by the relative orientation of features between layers, or by the relative values of a measurable parameter between layers, i.e. products comprising layers having different physical, chemical or physicochemical properties; Layered products characterised by the interconnection of layers
  • B32B7/04—Interconnection of layers
  • B32B7/12—Interconnection of layers using interposed adhesives or interposed materials with bonding properties
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
  • B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
  • B65D65/00—Wrappers or flexible covers; Packaging materials of special type or form
  • B65D65/38—Packaging materials of special type or form
  • B65D65/40—Applications of laminates for particular packaging purposes
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2250/00—Layers arrangement
  • B32B2250/05—5 or more layers
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2250/00—Layers arrangement
  • B32B2250/24—All layers being polymeric
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2264/00—Composition or properties of particles which form a particulate layer or are present as additives
  • B32B2264/10—Inorganic particles
  • B32B2264/102—Oxide or hydroxide
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2270/00—Resin or rubber layer containing a blend of at least two different polymers
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2307/00—Properties of the layers or laminate
  • B32B2307/30—Properties of the layers or laminate having particular thermal properties
  • B32B2307/306—Resistant to heat
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2307/00—Properties of the layers or laminate
  • B32B2307/30—Properties of the layers or laminate having particular thermal properties
  • B32B2307/31—Heat sealable
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2307/00—Properties of the layers or laminate
  • B32B2307/40—Properties of the layers or laminate having particular optical properties
  • B32B2307/412—Transparent
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2307/00—Properties of the layers or laminate
  • B32B2307/50—Properties of the layers or laminate having particular mechanical properties
  • B32B2307/514—Oriented
  • B32B2307/518—Oriented bi-axially
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2307/00—Properties of the layers or laminate
  • B32B2307/50—Properties of the layers or laminate having particular mechanical properties
  • B32B2307/558—Impact strength, toughness
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2307/00—Properties of the layers or laminate
  • B32B2307/70—Other properties
  • B32B2307/724—Permeability to gases, adsorption
  • B32B2307/7242—Non-permeable
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2377/00—Polyamides
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2439/00—Containers; Receptacles
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2439/00—Containers; Receptacles
  • B32B2439/40—Closed containers
  • B32B2439/46—Bags
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2439/00—Containers; Receptacles
  • B32B2439/70—Food packaging

Definitions

• the present invention relates to a laminated film suitable for use in packaging bags and the like.
• a biaxially stretched film made of an aliphatic polyamide represented by polyamide 6 is excellent in impact resistance and bending pinhole resistance, and is widely used as various packaging materials.
• Biomass is an organic compound that is photosynthesised from carbon dioxide and water.By using it, it becomes carbon dioxide and water again.It is a so-called carbon-neutral raw material, that is, the emission and absorption of carbon dioxide in the environment. Since the amount is the same, it is a raw material that can suppress the increase of carbon dioxide, which is a greenhouse gas. Biomass plastics using these biomass as raw materials have been rapidly put to practical use, and biaxially stretched polyamide films using biomass-derived raw materials have also been proposed (see, for example, Patent Document 1).
• the biaxially stretched polyamide film When used as a package, the biaxially stretched polyamide film is made into a laminated film by laminating a sealant film or the like, and then processed into a packaging bag or the like.
• a sealant film unstretched linear low-density polyethylene film, unstretched polypropylene film, etc. are used. From the viewpoint of carbon neutrality, a sealant film containing polyethylene polymerized using biomass-derived raw materials has been proposed. (See Patent Document 2, for example).
• An object of the present invention is to provide a carbon-neutral heat-sealable laminate film using biomass-derived raw materials while being excellent in heat resistance, impact resistance, and bending pinhole resistance.
• the present invention consists of the following configurations.
• a laminated film having at least a substrate layer and a sealant layer,
• the base layer is a biaxially stretched polyamide film
• the biaxially stretched polyamide film is laminated with a layer B on at least one side of the layer A
• the layer A is a polyamide containing ⁇ -caprolactam derived from fossil fuel as a lactam unit.
• the sealant layer is an unstretched polyolefin film, and the unstretched polyolefin film is a polypropylene-based resin of 70% by mass or more and 95% by mass or less, and at least part of the raw material is biomass-derived linear low-density polyethylene resin 5.
• a laminated film containing at least 30% by mass and no more than 30% by mass.
• the polyamide resin in which at least part of the raw material in the base material layer is derived from biomass is at least one polyamide resin selected from the group consisting of polyamide 11, polyamide 410, polyamide 610, and polyamide 1010, [ 1] The laminated film according to any one of [3].
• the sealant layer has a seal layer, a core layer and a laminate layer,
• the resin composition constituting the seal layer contains 94% by mass or more and 100% by mass or less of a propylene- ⁇ -olefin random copolymer and 0% by mass or more and 3% by mass or less of linear low-density polyethylene
• the resin composition constituting the core layer contains 25% by mass or more and 97% by mass or less of a propylene- ⁇ -olefin random copolymer and 3% by mass or more and 40% by mass or less of a linear low-density polyethylene
• the resin composition constituting the laminate layer contains 25% by mass or more and 70% by mass or less of a propylene- ⁇ -olefin random copolymer and 3% by mass or more and 50% by mass or less of
• the substrate layer of the present invention is preferably composed of a biaxially stretched polyamide film.
• the biaxially stretched polyamide film is a biaxially stretched polyamide film in which a B layer is laminated on at least one side of an A layer.
• Layer A is preferably composed of a polyamide resin composition containing at least 70% by mass to 99% by mass of polyamide 6 resin and 1% by mass to 30% by mass of a polyamide resin containing raw materials derived from biomass.
• a biaxially stretched polyamide film having excellent mechanical strength such as impact strength and gas barrier properties such as oxygen can be obtained.
• the A layer contains 1% by mass or more and 30% by mass or less of a polyamide resin containing biomass-derived raw materials, so that it is a carbon-neutral biaxially stretched polyamide film using biomass-derived raw materials.
• the bending pinhole resistance of the polyamide film is improved.
• a polyamide resin containing a biomass-derived raw material at a ratio of 1% by mass or more and 30% by mass or less, a biaxially stretched polyamide film having excellent flex pinhole resistance and friction pinhole resistance at the same time is obtained. can get.
• the upper limit of the content of the polyamide resin containing raw materials derived from biomass in the A layer is preferably 30% by mass, more preferably 20% by mass. If the content of the polyamide resin containing the raw material derived from biomass exceeds 30% by mass, the melted film becomes unstable when the melted film is cast, and it may be difficult to obtain a homogeneous unstretched film.
• Polyamide 6 used for the A layer is usually produced by ring-opening polymerization of ⁇ -caprolactam.
• Polyamide 6 obtained by ring-opening polymerization is melt-extruded by an extruder after removing the lactam monomer with hot water and drying.
• the relative viscosity of polyamide 6 is preferably 1.8 or more and 4.5 or less, more preferably 2.6 or more and 3.2 or less.
• the relative viscosity is 1.8 or more, impact strength required for the film can be obtained.
• the relative viscosity is 4.5 or less, it becomes easy to form an unstretched film by melt extruding the raw material resin from an extruder.
• polyamide 6 in addition to those polymerized from commonly used fossil fuel-derived monomers, polyamide 6 chemically recycled from used polyamide 6 products such as waste plastic products, waste tire rubber, fibers, and fishing nets can also be used.
• a method of obtaining chemically recycled polyamide 6 from used polyamide 6 products for example, after collecting used polyamide products, depolymerization is performed to obtain ⁇ -caprolactam, which is purified and then polyamide 6 can be used.
• mechanically recycled polyamide 6 can be used together.
• Mechanically recycled polyamide 6 is, for example, a non-standard film that cannot be shipped when producing a biaxially stretched polyamide film, and waste materials generated as cut ends (edge trim) are collected, melted, extruded and compressed. It is a raw material pelletized by molding.
• Polyamide at least part of which is derived from biomass examples include polyamide 11, polyamide 410, polyamide 610, polyamide 1010, polyamide MXD10, and polyamide 11/6T copolymer resin.
• Polyamide 11 is a polyamide resin having a structure in which monomers having 11 carbon atoms are bonded via amide bonds.
• Polyamide 11 is usually obtained using aminoundecanoic acid or undecanelactam as a monomer.
• aminoundecanoic acid is desirable from the viewpoint of carbon neutrality because it is a monomer obtained from castor oil.
• These structural units derived from monomers having 11 carbon atoms account for preferably 50 mol% or more, more preferably 80 mol% or more, more preferably 80 mol% or more, and 100 mol% of all structural units in polyamide 11. good too.
• Polyamide 11 is usually produced by the ring-opening polymerization of undecanelactam described above.
• Polyamide 11 obtained by ring-opening polymerization is usually melt-extruded by an extruder after removing the lactam monomer with hot water and then drying.
• the relative viscosity of polyamide 11 is preferably 1.8 or more and 4.5 or less, more preferably 2.4 or more and 3.2 or less. When the relative viscosity is 1.8 or more, impact strength required for the film can be obtained. When the relative viscosity is 4.5 or less, it becomes easy to form an unstretched film by melt extruding the raw material resin from an extruder.
• Polyamide 410 is a polyamide resin having a structure in which a monomer having 4 carbon atoms and a diamine having 10 carbon atoms are copolymerized. Polyamide 410 typically utilizes sebacic acid and tetramethylene diamine. Sebacic acid is preferably made from castor oil, which is a vegetable oil, from an environmental point of view. Sebacic acid used here is preferably obtained from castor oil from the viewpoint of environmental protection, particularly from the viewpoint of carbon neutrality.
• Polyamide 610 is a polyamide resin having a structure in which a diamine having 6 carbon atoms and a dicarboxylic acid having 10 carbon atoms are polymerized. Hexamethylenediamine and sebacic acid are commonly used. Of these, sebacic acid is a monomer obtained from castor oil, and is desirable from the viewpoint of carbon neutrality. Structural units derived from these monomers having 6 carbon atoms and structural units derived from monomers having 10 carbon atoms, the total in PA610 is 50 mol of all structural units % or more, more preferably 80 mol % or more, and may be 100 mol %.
• Polyamide 1010 is a polyamide resin having a structure in which a diamine having 10 carbon atoms and a dicarboxylic acid having 10 carbon atoms are polymerized.
• Polyamide 1010 typically utilizes 1,10-decanediamine (decamethylenediamine) and sebacic acid. Decamethylenediamine and sebacic acid are monomers obtained from castor oil, and thus are desirable from the carbon neutral point of view.
• the structural unit derived from a diamine having 10 carbon atoms and the structural unit derived from a dicarboxylic acid having 10 carbon atoms account for 50 mol% or more of all structural units in polyamide 1010. is preferred, more preferably 80 mol % or more, and may be 100 mol %.
• the lower limit of the content of the polyamide, at least part of which is derived from biomass, in the A layer is not particularly limited, but is preferably 1% by mass, more preferably 3% by mass.
• the upper limit of the content is 30% by mass, more preferably 20% by mass. If the content of the polyamide, at least part of which is derived from biomass, exceeds 30% by mass, the melt film may become unstable during casting, making it difficult to obtain a homogeneous unstretched film.
• additives Various additives such as other thermoplastic resins, lubricants, heat stabilizers, antioxidants, antistatic agents, antifogging agents, ultraviolet absorbers, dyes, and pigments may be added to the A layer as necessary. can be done.
• the A layer may contain a thermoplastic resin in addition to the polyamide 6 and the polyamide resin at least partially derived from biomass as long as the object of the present invention is not impaired.
• a thermoplastic resin such as polyamide 12 resin, polyamide 66 resin, polyamide 6/12 copolymer resin, polyamide 6/66 copolymer resin, and polyamide MXD6 resin.
• Thermoplastic resins other than polyamides for example, polyester polymers such as polyethylene terephthalate, polybutylene terephthalate, and polyethylene-2,6-naphthalate, and polyolefin polymers such as polyethylene and polypropylene, may be added as necessary. good. It is preferable that the raw materials of these thermoplastic resins are biomass-derived, because they do not affect the increase or decrease of carbon dioxide on the ground, and the environmental load can be reduced.
• Layer B is preferably composed of a polyamide resin composition containing polyamide 6 resin in a proportion of 70% by mass or more and 100% by mass or less. By containing 70% by mass or more of the polyamide 6 resin, the layer B can obtain a biaxially stretched polyamide film having excellent mechanical strength such as impact strength and gas barrier properties such as oxygen.
• the polyamide 6 resin the same polyamide 6 resin as used in the layer A can be used.
• the B layer has various additives such as other thermoplastic resins, lubricants, heat stabilizers, antioxidants, antistatic agents, antifogging agents, ultraviolet absorbers, dyes, and pigments on the surface of the B layer. It can be contained depending on the function. When the B layer is used on the outside of the packaging bag, it is necessary to have friction pinhole resistance, so it is not preferable to contain a soft resin such as a polyamide elastomer or a polyolefin elastomer or a substance that generates a large amount of voids.
• a soft resin such as a polyamide elastomer or a polyolefin elastomer or a substance that generates a large amount of voids.
• the B layer can contain a thermoplastic resin in addition to the polyamide 6 as long as it does not impair the purpose of the present invention.
• a thermoplastic resin in addition to the polyamide 6 as long as it does not impair the purpose of the present invention.
• examples thereof include polyamide resins such as polyamide MXD6 resin, polyamide 11 resin, polyamide 12 resin, polyamide 66 resin, polyamide 6/12 copolymer resin, and polyamide 6/66 copolymer resin.
• Thermoplastic resins other than polyamides for example, polyester polymers such as polyethylene terephthalate, polybutylene terephthalate, and polyethylene-2,6-naphthalate, and polyolefin polymers such as polyethylene and polypropylene, may be added as necessary. good.
• the layer B preferably contains fine particles or an organic lubricant such as fatty acid amide as a lubricant in order to improve the film's lubricity and make it easy to handle.
• an organic lubricant such as fatty acid amide as a lubricant
• the fine particles inorganic fine particles such as silica, kaolin, and zeolite, and polymer-based organic fine particles such as acryl-based and polystyrene-based organic fine particles can be appropriately selected and used. From the viewpoint of transparency and slipperiness, it is preferable to use fine silica particles.
• the fine particles preferably have an average particle size of 0.5 ⁇ m or more and 5.0 ⁇ m or less, more preferably 1.0 ⁇ m or more and 3.0 ⁇ m or less. When the average particle size is 0.5 ⁇ m or more, good lubricity can be obtained. On the other hand, when it is 5.0 ⁇ m or less, it is possible to suppress poor appearance due to the degree of surface roughness of
• the pore volume of silica is preferably 0.5 ml/g or more and 2.0 ml/g or less, more preferably 0.8 ml/g or more and 1.6 ml/g or less.
• the pore volume is 0.5 ml/g or more, it is possible to suppress the deterioration of the transparency of the film due to the generation of voids. Easy to form protrusions.
• the B layer can contain fatty acid amide and/or fatty acid bisamide for the purpose of improving slipperiness.
• Fatty acid amides and/or fatty acid bisamides include erucic acid amide, stearic acid amide, ethylene bis stearic acid amide, ethylene bis behenic acid amide, ethylene bis oleic acid amide and the like.
• the content of fatty acid amide and/or fatty acid bisamide is preferably 0.01% by mass or more and 0.40% by mass or less, more preferably 0.05% by mass or more and 0.30% by mass or less. When the content of fatty acid amide and/or fatty acid bisamide is 0.01% by mass or more, lubricity can be imparted, and when the content is 0.40% by mass or less, wettability can be maintained.
• a polyamide resin such as a polyamide MXD6 resin, a polyamide 12 resin, a polyamide 66 resin, a polyamide 6/12 copolymer resin, or a polyamide 6/66 copolymer resin can be added to the B layer for the purpose of improving slipperiness.
• the layers A and B of the biaxially stretched polyamide film of the present invention may contain an antioxidant.
• Phenolic antioxidants are preferred as antioxidants.
• the phenolic antioxidant is preferably a fully hindered phenolic compound or a partially hindered phenolic compound.
• the substrate layer in the present invention is a biaxially stretched polyamide film in which a B layer is laminated on at least one side of an A layer.
• a B layer is laminated on at least one side of an A layer.
• Specific examples include a two-layer structure of A layer/B layer and a three-layer structure of B layer/A layer/B layer.
• the thickness of the base material layer is not particularly limited, but when used as a packaging material, it is usually preferably 100 ⁇ m or less, may be 5 ⁇ m or more and 50 ⁇ m or less, or 8 ⁇ m or more and 30 ⁇ m or less. There may be.
• the biaxially stretched polyamide film of the base layer preferably has a heat shrinkage rate of 0.6% or more and 3.0% or less at 160 ° C. for 10 minutes in both the MD and TD directions, more preferably , 0.6% or more and 2.5% or less. If the heat shrinkage rate exceeds 3.0%, curling or shrinkage may occur when heat is applied in the next step such as lamination or printing. Moreover, the lamination strength with the sealant film may be weakened. Although it is possible to set the heat shrinkage rate to less than 0.6%, it may become mechanically brittle, and the productivity may deteriorate.
• the impact strength of the biaxially stretched polyamide film is preferably 0.7 J/15 ⁇ m or more.
• a more preferable impact strength is 0.9 J/15 ⁇ m or more.
• the haze value of the biaxially stretched polyamide film is preferably 10% or less. More preferably 7% or less, still more preferably 5% or less. If the haze value is small, it has transparency and gloss, and is particularly suitable for packaging bags. If fine particles are added to improve the slipperiness of the film, the haze value increases. Therefore, when the film has two or more layers, it is preferable to add fine particles only to the B layer because the haze value can be reduced.
• the dynamic friction coefficient of the biaxially stretched polyamide film is preferably 1.0 or less. It is more preferably 0.7 or less, still more preferably 0.5 or less. If the coefficient of dynamic friction of the film is small, the slipperiness is improved and the handling of the film is facilitated. If the coefficient of dynamic friction of the film is too small, it may become too slippery to handle, and the coefficient of dynamic friction is preferably 0.15 or more.
• the biaxially stretched polyamide film has a content of biomass-derived carbon measured by radioactive carbon 14 C of ASTM D6866-18, that is, a degree of biomass, of 1% or more and 30% or less with respect to the total carbon in the polyamide film. is preferred. Since carbon dioxide in the atmosphere contains 14 C at a certain rate (105.5 pMC), the 14 C content in plants that grow by taking in carbon dioxide in the atmosphere, such as corn, is also about 105.5 pMC. is known to be It is also known that fossil fuels contain almost no 14 C. Therefore, by measuring the ratio of 14 C contained in the total carbon atoms in the film, the ratio of biomass-derived carbon can be calculated.
• the biaxially stretched polyamide film of the substrate layer can be produced by a known production method. A typical production example is described below.
• the resin composition forming the A layer and the resin composition forming the B layer are melt-extruded using an extruder, and the A and B layers are laminated using a feed block or multi-manifold to form a film from a T die. It is extruded into a shape, cast on a cooling roll and cooled to obtain an unstretched film.
• the melting temperature of the resin is preferably 220°C or higher and 350°C or lower. If it is less than the above range, unmelted materials may occur, resulting in appearance defects such as defects.
• the die temperature is preferably 250° C. or higher and 350° C. or lower.
• the cooling roll temperature is preferably ⁇ 30° C. or higher and 80° C. or lower, more preferably 0° C. or higher and 50° C. or lower.
• a method using an air knife or an electrostatic adhesion method in which an electrostatic charge is applied can be applied. . Especially the latter is preferably used.
• the unstretched film thus obtained is biaxially stretched to obtain a biaxially stretched polyamide film.
• the stretching method may be a simultaneous biaxial stretching method or a sequential biaxial stretching method.
• single-stage stretching or multi-stage stretching such as two-stage stretching can be used as the stretching method in the MD direction.
• multi-stage stretching in the MD direction such as two-stage stretching is preferable in terms of physical properties and uniformity of physical properties in the MD and TD directions, that is, isotropy, rather than single-stage stretching.
• Stretching in the MD direction in the sequential biaxial stretching method is preferably roll stretching.
• the lower limit of the stretching temperature in the MD direction is preferably 50°C, more preferably 55°C, and still more preferably 60°C. If the temperature is less than 50°C, the resin may not be softened, making stretching difficult.
• the upper limit of the stretching temperature in the MD direction is preferably 120°C, more preferably 115°C, still more preferably 110°C. If the temperature exceeds 120°C, the resin may become too soft to allow stable stretching.
• the lower limit of the draw ratio in the MD direction is preferably 2.2 times, more preferably 2.5 times, and still more preferably 2.8 times.
• the above stretching ratio is the total stretching ratio obtained by multiplying the ratio of each stage. If it is less than 2.2 times, the thickness accuracy in the MD direction may be lowered, and the crystallinity may be too low, resulting in a decrease in impact strength.
• the upper limit of the draw ratio in the MD direction is preferably 5.0 times, more preferably 4.5 times, and most preferably 4.0 times. If it exceeds 5.0 times, subsequent stretching may become difficult.
• the stretching in the MD direction is performed in multiple stages, the stretching as described above is possible in each stretching. It is necessary to adjust the draw ratio.
• the first stage stretching should be 1.5 times or more and 2.1 times or less, and the second stage stretching should be 1.5 times or more and 1.8 times or less. is preferred.
• the film stretched in the MD direction is stretched in the TD direction with a tenter, heat-set, and subjected to relaxation treatment.
• the lower limit of the stretching temperature in the TD direction is preferably 50°C, more preferably 55°C, still more preferably 60°C. If the temperature is less than 50°C, the resin may not be softened, making stretching difficult.
• the upper limit of the stretching temperature in the TD direction is preferably 190°C, more preferably 185°C, still more preferably 180°C. If the temperature exceeds 190°C, crystallization may occur, making stretching difficult.
• the lower limit of the draw ratio in the TD direction is preferably 2.8 times, more preferably 3.2 times, still more preferably 3.5 times, and particularly preferably 3.8 times.
• the above stretching ratio is the total stretching ratio obtained by multiplying the ratio of each stage. If it is less than 2.8 times, the thickness accuracy in the TD direction may be lowered, and the impact strength may be lowered due to the lower crystallinity.
• the upper limit of the draw ratio in the TD direction is preferably 5.5 times, more preferably 5.0 times, still more preferably 4.7 times, particularly preferably 4.5 times, and most preferably 4.3 times. If it exceeds 5.5 times, the productivity may decrease.
• the lower limit of the heat setting temperature is preferably 210°C, more preferably 212°C. If the heat setting temperature is too low, the heat shrinkage tends to be too large, resulting in a poor appearance after lamination or a reduction in lamination strength.
• the upper limit of the heat setting temperature is preferably 220°C, more preferably 218°C. If the heat setting temperature is too high, the impact strength tends to decrease.
• the heat setting time is preferably 0.5 seconds or more and 20 seconds or less. Furthermore, it is 1 second or more and 15 seconds or less.
• the heat setting time can be set to an appropriate time in consideration of the heat setting temperature and the wind speed in the heat setting zone. By setting the heat setting conditions within the above range, desired crystallization and orientation relaxation can be achieved.
• the temperature for the relaxation treatment can be selected in the range from the heat setting temperature to the glass transition temperature Tg of the resin, but is preferably "heat setting temperature (°C) -10°C" or higher and "glass transition temperature +10°C” or lower.
• the lower limit of the relaxation rate of the relaxation process is preferably 0.5%, more preferably 1%.
• the upper limit of the relaxation rate is preferably 20%, more preferably 15%, still more preferably 10%.
• the biaxially stretched polyamide film of the base layer can be subjected to heat treatment or humidity conditioning treatment to improve dimensional stability depending on the application.
• heat treatment or humidity conditioning treatment to improve dimensional stability depending on the application.
• vapor deposition film formed by the vapor deposition process a vapor deposition film of aluminum, a vapor deposition film of a single substance or a mixture of silicon oxide or aluminum oxide is preferably used.
• a protective layer or the like on these vapor-deposited films, the oxygen barrier properties and the like can be improved.
• the sealant layer of the present invention is preferably composed of an unstretched polyolefin film.
• the unstretched polyolefin film contains 70% by mass or more and 95% by mass or less of a polypropylene resin and 5% by mass of a linear low-density polypropylene resin in which at least part of the raw material is derived from biomass. Above, it contains in the ratio of 30 mass % or less.
• the unstretched polyolefin film preferably has a laminated structure, and more preferably includes a seal layer, a core layer and a laminate layer.
• the seal layer and laminate layer are layers positioned on the surface side of the unstretched polyolefin film, and the core layer is preferably positioned between them.
• the laminate layer is a layer suitable for laminating a biaxially stretched polyamide film, and is preferably laminated with the biaxially stretched polyamide film via an adhesive resin.
• the sealing layer is a layer suitable for heat sealing to produce a packaging bag.
• the polypropylene-based resin composition that constitutes the sealing layer preferably contains a propylene- ⁇ -olefin random copolymer.
• the content of the propylene- ⁇ -olefin random copolymer in the polypropylene resin composition constituting the seal layer is preferably 94% by mass or more, more preferably 97% by mass or more, still more preferably 99% by mass or more, and 100% by mass. Especially preferred. Sufficient heat-sealing strength is obtained by making it 94 mass % or more.
• the polypropylene-based resin composition that constitutes the seal layer may contain a propylene homopolymer.
• a propylene homopolymer By containing the propylene homopolymer, it is possible to improve the lubricity.
• the content of the propylene homopolymer is preferably 3% by mass or less, more preferably 2% by mass, even more preferably 1% by mass or less, and particularly preferably 0% by mass, from the viewpoint of heat seal strength.
• the sealing layer can contain linear low-density polyethylene.
• the linear low-density polyethylene By containing the linear low-density polyethylene, the bending pinhole resistance can be improved.
• the content of the linear low-density polyethylene is preferably 3% by mass or less, more preferably 2% by mass, even more preferably 1% by mass or less, and particularly preferably 0% by mass, from the viewpoint of heat seal strength.
• the polypropylene-based resin composition constituting the core layer preferably contains a propylene- ⁇ -olefin random copolymer.
• the heat seal strength can be improved by containing the propylene- ⁇ -olefin random copolymer.
• the content of the propylene- ⁇ -olefin random copolymer is preferably 25% by mass or more, more preferably 40% by mass or more, still more preferably 60% by mass or more, and particularly preferably 75% by mass or more, from the viewpoint of heat seal strength. 80% by mass or more is particularly preferred. From the viewpoint of bending pinhole resistance, it is preferably 97% by mass or less, more preferably 90% by mass or less, and even more preferably 85% by mass or less.
• the polypropylene-based resin composition that constitutes the core layer may contain a propylene homopolymer.
• the content of the propylene homopolymer is preferably 60% by mass or less, more preferably 50% by mass or less, and even more preferably 40% by mass or less, from the viewpoint of heat seal strength and bag breakage resistance.
• the core layer can contain linear low-density polyethylene.
• linear low-density polyethylene By containing the linear low-density polyethylene, the bending pinhole resistance can be improved.
• the content of linear low-density polyethylene is preferably 3% by mass or more, more preferably 8% by mass or more, still more preferably 12% by mass or more, and particularly preferably 15% by mass or more. From the viewpoint of heat resistance, it is preferably 40% by mass or less, more preferably 35% by mass or less, even more preferably 30% by mass or less, and particularly preferably 25% by mass or less.
• the polypropylene-based resin composition that constitutes the laminate layer preferably contains a propylene- ⁇ -olefin random copolymer.
• the heat seal strength can be improved by containing the propylene- ⁇ -olefin random copolymer.
• the content of the propylene- ⁇ -olefin random copolymer is preferably 20% by mass or more, more preferably 40% by mass or more, and even more preferably 70% by mass or more. From the viewpoint of bending pinhole resistance, the content is preferably 90% by mass or less, more preferably 80% by mass or less.
• the polypropylene-based resin composition that constitutes the laminate layer may contain a propylene homopolymer.
• the content of the propylene homopolymer is preferably 60% by mass or less, more preferably 50% by mass or less, and even more preferably 40% by mass or less, from the viewpoint of heat seal strength and bag breakage resistance.
• the laminate layer can contain linear low-density polyethylene.
• linear low-density polyethylene By containing the linear low-density polyethylene, the bending pinhole resistance can be improved.
• the content of linear low-density polyethylene is preferably 3% by weight or more, more preferably 8% by weight or more, still more preferably 15% by weight or more, particularly preferably 20% by weight or more, and most preferably 25% by weight or more. From the viewpoint of heat resistance and heat seal strength, the content is preferably 50% by weight or less, more preferably 40% by weight or less, and even more preferably 30% by weight or less.
• the difference in linear low-density polyethylene content between the seal layer and the core layer is preferably 1% by mass or more and 28% by mass or less. It is more preferably 1% by mass or more and 23% by mass or less, still more preferably 1% by mass or more and 18% by mass or less, and particularly preferably 1% by mass or more and 15% by mass or less.
• the difference in content of linear low-density polyethylene between the core layer and the laminate layer is preferably 1% by mass or more and 28% by mass or less. It is more preferably 1% by mass or more and 23% by mass or less, still more preferably 1% by mass or more and 18% by mass or less, and particularly preferably 1% by mass or more and 15% by mass or less.
• the content of linear low-density polyethylene in the core layer is higher than the content of linear low-density polyethylene in the seal layer, and the core layer contains linear low-density polyethylene. It is preferable that the linear low-density polyethylene content in the laminate layer is higher than the ratio. By doing so, the linear low-density polyethylene in the film tends to be uniformly dispersed, which is advantageous in terms of bending pinhole resistance. In addition, high heat seal strength can be obtained due to the large ratio of the polypropylene-based resin in the resin near the heat seal surface.
• Propylene- ⁇ -olefin random copolymer with a low melting point is used for the seal layer, and propylene- ⁇ -olefin random copolymer with a high melting point is used for the core layer and laminate layer to improve heat seal strength. At the same time, the heat resistance and bending pinhole resistance can be further enhanced.
• propylene- ⁇ -olefin random copolymer examples include copolymers of propylene and at least one ⁇ -olefin other than propylene having 2 or 4 to 20 carbon atoms.
• ⁇ -olefin monomers having 2 or 4 to 20 carbon atoms include ethylene, butene-1, pentene-1, 4-methylpentene-1, hexene-1, and octene-1.
• the propylene- ⁇ -olefin random copolymer preferably contains ethylene as the ⁇ -olefin in terms of heat sealability. At least one type or more may be used, and two or more types may be mixed and used as needed. Particularly suitable is a propylene-ethylene-butene random copolymer in which the main monomer is propylene and certain amounts of ethylene and butene are copolymerized.
• the lower limit of the melt flow rate MFR of the propylene- ⁇ -olefin random copolymer is preferably 0.6 g/10 min, more preferably 1.0 g/10 min, still more preferably 1.2 g/10 min.
• the upper limit of the melt flow rate of the random copolymer is preferably 12.0 g/10 min, more preferably 9.0 g/10 min, still more preferably 8.0 g/10 min.
• the melt flow rate (MFR) of the propylene homopolymer is not particularly limited, but is preferably 1.0 g/10 min or more and 10.0 g/10 min or less, and 2.0 g/min or more. 0 g/min or less is more preferable. If it is less than 1.0 g / 10 min, the viscosity is too high and extrusion with a T die may be difficult, and if it exceeds 10.0 g / 10 min, the film becomes sticky and the impact resistance of the film Problems such as poor strength (impact strength) may occur.
• isotactic polypropylene which has high crystallinity and can suppress deterioration of thermal shrinkage, is preferable.
• Linear low-density polyethylene can be produced by a production method such as a high-pressure method, a solution method, or a gas phase method.
• Examples of linear low-density polyethylene include copolymers of ethylene and at least one ⁇ -olefin having 3 or more carbon atoms.
• the ⁇ -olefin having 3 or more carbon atoms may be propylene, butene-1, hexene-1, octene-1, 4-methyl-1-pentene.
• copolymer of ethylene and ⁇ -olefin examples include ethylene/hexene-1 copolymer, ethylene/butene-1 copolymer, ethylene/octene-1 copolymer, and the like. -hexene copolymers are preferred.
• Linear low-density polyethylene is a biomass-derived linear low-density polyethylene polymerized using ethylene derived from plants such as sugar cane and ethylene derived from fossil fuels such as petroleum or plants as part of the raw material. can contain. From the viewpoint of carbon neutrality, biomass-derived linear low-density polyethylene is said to be effective in reducing the amount of carbon dioxide generated, and to be able to suppress global warming.
• biomass-derived linear low-density polyethylene contains biomass-derived ethylene
• the content of biomass-derived ethylene is preferably 50% by mass or more, more preferably 80% by mass or more. When it is 50% by mass or more, the effect of reducing carbon dioxide is excellent.
• the upper limit is preferably 98% by mass, more preferably 96% by mass. Since it is preferable to copolymerize an ⁇ -olefin other than ethylene from the viewpoint of bending pinhole resistance, it is preferably 98% by mass or less.
• the lower limit of the melt flow rate MFR (190°C, 2.18 kg measurement) of linear low-density polyethylene is preferably 1.0 g/10 min, more preferably 2.0 g/10 min.
• the upper limit is preferably 7.0 g/min, more preferably 5.0 g/min. Within the above range, good compatibility with the polypropylene-based resin and high seal strength can be obtained.
• the lower limit of the density of linear low density polyethylene is preferably 910 kg/m 3 , more preferably 913 kg/m 3 .
• Good anti-blocking property can be obtained by making it 910 kg/m 3 or more.
• the upper limit is 935 kg/m 3 , more preferably 930 kg/m 3 .
• Good resistance to bag breakage can be obtained when it is 935 kg/m 3 or less.
• the polyolefin-based resin composition that constitutes the unstretched polyolefin film may contain an antiblocking agent.
• an antiblocking agent may be used, but it is better to blend two or more types of inorganic particles with different particle sizes and shapes. be able to.
• the anti-blocking agent to be added is not particularly limited, but inorganic particles such as spherical silica, amorphous silica, zeolite, talc, mica, alumina, hydrotalcite, aluminum borate, polymethyl methacrylate, ultra high molecular weight Organic particles such as polyethylene can be added.
• the anti-blocking agent contained in the polypropylene-based resin composition constituting the seal layer is preferably 0.30% by mass or less, more preferably 0.25% by mass or less, relative to the polyolefin-based resin of the layer to which it is added. By making it 0.30% by mass or less, it is possible to reduce the shedding of the antiblocking agent. Moreover, it is preferably 0.05% by mass or more, and more preferably 0.10% by mass or more. Favorable anti-blocking property can be obtained by making it 0.05 mass % or more.
• the anti-blocking agent contained in the polypropylene-based resin composition constituting the laminate layer is preferably 0.30% by mass or less, more preferably 0.25% by mass or less, relative to the polyolefin-based resin of the layer to be added. 0.10% by mass or less is even more preferable, and 0.05% by mass or less is particularly preferable. By setting the amount to 0.30% by mass or less, it is possible to reduce detachment of the antiblocking agent from the surface of the laminate layer.
• the polyolefin-based resin composition that constitutes the unstretched polyolefin film can contain an organic lubricant.
• an organic lubricant By containing an organic lubricant, the lubricity and anti-blocking effect of the film are improved, and the handleability of the film is improved. It is believed that the reason for this is that the organic lubricant bleeds out and is present on the film surface, thereby exhibiting the lubricant effect and the release effect.
• the organic lubricant preferably has a melting point above room temperature. Examples of organic lubricants include fatty acid amides and fatty acid esters.
• the content of the organic lubricant in the polypropylene-based resin composition is preferably 0.15% by mass or less, more preferably 0.10% by mass or less. By making it 0.15% by mass or less, blocking is less likely to occur even when stored in a place exposed to high temperatures such as a warehouse in summer. Moreover, it is preferably 0.02% by mass or more, and more preferably 0.025% by mass or more. Favorable lubricity can be obtained by making it 0.02% by mass or more.
• the polyolefin-based resin composition that constitutes the unstretched polyolefin film can contain an antioxidant.
• antioxidants include phenolic antioxidants, phosphite antioxidants, combinations thereof, and those having phenolic and phosphite skeletons in one molecule. Calcium stearate etc. are mentioned as a neutralizing agent.
• the lower limit of the thickness of the unstretched polyolefin film of the sealant layer is preferably 15 ⁇ m, more preferably 20 ⁇ m, still more preferably 25 ⁇ m. When the thickness is 15 ⁇ m or more, it is easy to obtain heat seal strength and bag breakage resistance.
• the upper limit of the film thickness is preferably 80 ⁇ m, more preferably 70 ⁇ m, still more preferably 60 ⁇ m, and particularly preferably 50 ⁇ m. When the thickness is 80 ⁇ m or less, the film has an appropriate stiffness and is easy to process, and is suitable for producing packaging bags.
• the haze value of the unstretched polyolefin film is preferably 20% or less. It is more preferably 15% or less, still more preferably 10% or less. When it is 20% or less, the visibility of the package can be easily obtained. Linear low-density polyethylene has high crystallinity and tends to increase haze, but if added within the above preferred range, increase in haze can be suppressed.
• the lower limit is preferably 1%, more preferably 2%. If it is 1% or more, the film surface does not have an extremely small unevenness, so blocking on the inner surface of the package is unlikely to occur.
• the coefficient of static friction of the unstretched polyolefin film is preferably 0.70 or less, more preferably 0.50 or less, still more preferably 0.40 or less. When it is 0.70 or less, the surfaces that are not present when the package is filled with food or when the package is opened are slippery and the opening is good.
• the lower limit is preferably 0.10 or more, more preferably 0.20 or more, and particularly preferably 0.30 or more. When it is 0.10 or more, it is difficult for the rolled film to collapse during transportation.
• the impact strength of the unstretched polyolefin film is preferably 0.20 J/15 ⁇ m or more, more preferably 0.25 J/15 ⁇ m or more, still more preferably 0.30 J/15 ⁇ m or more. By making it 0.20 J/15 ⁇ m or more, the drop bag breakage resistance of the package can be enhanced. Although the upper limit of the impact strength is not particularly limited, it is preferably 1.0 J/15 ⁇ m or less. Impact strength is highly dependent on the thickness and molecular orientation of the film. Moreover, the impact strength and the drop bag breakage resistance are not necessarily correlated.
• the puncture strength of the unstretched polyolefin film is preferably 1.0 N/ ⁇ m or more, more preferably 1.5 N/ ⁇ m or more, and still more preferably 1.7 N/ ⁇ m or more. When it is 1.0 N/ ⁇ m or more, the laminate has good pierce pinhole resistance.
• the plane orientation coefficient of the unstretched polyolefin film is preferably 0.000 or more, more preferably 0.001 or more.
• the upper limit of the plane orientation of the film is preferably 0.010 or less, more preferably 0.008 or less, and still more preferably 0.006 or less. By being 0.010 or less, a film with a uniform thickness can be obtained.
• the heat-seal initiation temperature of the unstretched polyolefin film is preferably 110°C or higher, more preferably 120°C or higher. When the temperature is 110° C. or higher, the film has a firm feeling and is easy to handle.
• the upper limit of the heat seal initiation temperature is 150°C, preferably 140°C, and still more preferably 130°C. When the temperature is 150°C or lower, the package can be produced at high speed, which is economically advantageous.
• the heat seal initiation temperature is greatly affected by the melting point of the seal layer.
• the surface wetting tension of the unstretched polyolefin film is preferably 30 mN/m or more, more preferably 35 mN/m or more. When it is 30 mN/m or more, the laminate strength is less likely to decrease.
• the upper limit of the wetting tension is preferably 55 mN/m, more preferably 50 mN/m. If it is 55 mN/m or less, blocking between films is less likely to occur when the polyolefin resin film is wound on a roll.
• the unstretched polyolefin film contains 3% or more and 30% or less of the total carbon in the unstretched polyolefin film, that is, the content of biomass-derived carbon measured by radioactive carbon 14 C according to ASTM D6866-18, that is, the degree of biomass. is preferred.
• Method for producing unstretched polyolefin film for example, an inflation method or a T-die method can be used, but the T-die method is preferable in order to improve transparency.
• the inflation method uses air as a cooling medium, whereas the T-die method uses cooling rolls, and is therefore an advantageous manufacturing method for increasing the cooling rate. Since crystallization of the unstretched sheet can be suppressed by increasing the cooling rate, transparency is advantageous. For these reasons, it is preferable to use a non-oriented sheet in the T-die method.
• the raw materials of the polypropylene resin composition for the seal layer, core layer, and laminate layer are mixed, melt-mixed and extruded by separate extruders, and the laminated sheets of the seal layer, core layer, and laminate layer melted from the T-die are cooled. Cast on rolls to obtain non-oriented sheets.
• the lower limit of the temperature of the chill roll is preferably 15°C, more preferably 20°C. If it is less than the above, dew condensation may occur on the cooling roll, resulting in insufficient adhesion.
• the upper limit of the chill roll is preferably 60°C, more preferably 50°C. Transparency may deteriorate when the above is exceeded.
• the laminated film of the present invention has a substrate layer and a sealant layer, but the laminated film can also be constructed by interposing an adhesive layer, a printed layer, a metal layer, or the like between the substrate layer and the sealant layer.
• a lamination method known methods such as dry lamination and extrusion lamination can be used, but any lamination method may be used. Specific examples are shown below.
• Example of layer structure of the laminated film of the present invention ONY/adhesive/CPP, ONY/adhesive/Al/adhesive/CPP, PET/adhesive/ONY/adhesive/CPP, PET/adhesive/ONY/adhesive Agent/Al/adhesive/CPP, PET/adhesive/Al/adhesive/ONY/adhesive/CPP, ONY/adhesive/PET/adhesive/CPP, ONY/PE/CPP, ONY/adhesive/EVOH /adhesive/CPP, ONY/adhesive/aluminum-deposited PET/adhesive/CPP, CPP/adhesive/ONY/adhesive/LLDPE, ONY/adhesive/aluminum-deposited CPP.
• the flex resistance of the laminated film of the present invention can be measured by pinhole evaluation.
• the number of pinholes after bending the laminated film 1000 times at 1° C. is preferably 20 or less, more preferably 15 or less, and particularly preferably 10 or less. If the number is 20 or less, pinholes are less likely to occur due to bending impact during transportation of the packaging bag.
• the puncture strength of the laminated film of the present invention is preferably 10 N or more, more preferably 12 N or more, and still more preferably 14 N or more.
• the tension is 10 N or more, pinholes are less likely to occur when the protrusions come into contact with the package.
• the heat seal strength of the laminated film of the present invention is preferably 20 N/15 mm or more, more preferably 25 N/15 mm or more, still more preferably 30 N/15 mm or more. When it is 20 N/15 mm or more, the resistance to bag breakage is likely to be obtained. A heat seal strength of 60 N/15 mm is very good, and 35 N/15 mm is sufficient.
• the content of biomass-derived carbon measured by radioactive carbon 14 C according to ASTM D6866-18, that is, the degree of biomass is 2% or more and 30% or less with respect to the total carbon in the laminated film. is preferred.
• the laminated film of the present invention is processed into a packaging bag intended mainly to protect contents such as foodstuffs and beverages from dust and gas in the natural world.
• the packaging bag is manufactured by bonding the inner surfaces of the laminated film with a heat-seal bar or ultrasonic waves to form a bag shape.
• a heat-seal bar or ultrasonic waves For example, two rectangular laminates are stacked so that the sealant layer side faces inward, and the four sides are heat-sealed to form a four-sided seal bag.
• the laminated film of the present invention can be processed into packaging bags such as bottom seal bags, side seal bags, three side seal bags, pillow bags, standing pouches, gusset bags and square bottom bags.
• the package of the present invention preferably has a falling bag breakage resistance of 15 times or more, more preferably 20 times or more, and still more preferably 22 times or more. If it is 15 times or more, even when the package containing the food is dropped, the bag is less likely to break. About 30 times of falling bag breakage resistance is sufficient.
• the falling bag breakage resistance of the package is affected by the flex pinhole resistance, puncture strength, and heat seal strength of the laminate, and these characteristics are preferably set within a preferable range.
• Film evaluation was performed by the following measurement methods. Unless otherwise specified, measurements were carried out in a measurement room at 23° C. and a relative humidity of 65%.
• Thickness of Film The film thus obtained is cut into a length of 100 mm in a stack of 10 sheets, and is conditioned at a temperature of 23° C. and a relative humidity of 65% for 2 hours or more. After that, the width direction of the film is divided into 10 equal parts (for narrow films, the width is divided so that the width that can measure the thickness can be secured), and the thickness is measured using a thickness measuring instrument manufactured by Tester Sangyo. The thickness of the film was obtained by dividing the average value by the number of films stacked. In addition, the thickness of the A layer in the biaxially stretched polyamide film was calculated based on the ratio of the discharge amount of the resins of the A layer and the B layer.
• Thermal shrinkage rate [(length before treatment - length after treatment) / length before treatment] x 100 (%)
• Puncture strength The pierce strength of the film is determined according to the Food Sanitation Law, Standards and Standards for Foods, Additives, etc. No. 3: Utensils, Containers and Packaging (Ministry of Health and Welfare Notification No. 20, 1982), Section 2. Test methods for strength, etc. ” was measured in accordance with A needle having a tip diameter of 0.7 mm was pierced into the film at a piercing speed of 50 mm/min. When the puncture strength was expressed in units of N/ ⁇ m, the value obtained by dividing the puncture strength of the film (unit: N) by the thickness of the film (unit: ⁇ m) was defined as the puncture strength.
• Heat-seal initiation temperature The heat-seal initiation temperature of the unstretched polyolefin film was measured according to JIS Z 1713-2009. At this time, the film was cut into a rectangular test piece of 50 mm in the TD direction ⁇ 250 mm in the MD direction. The seal layer portions of the two test pieces are overlapped, and a thermal gradient tester (heat seal tester) manufactured by Toyo Seiki Seisakusho Co., Ltd. is used, with a heat seal pressure of 0.2 MPa and a heat seal time of 1.0 sec. bottom. Then, heat-sealing was performed under the condition that the temperature was increased with an inclination of 5°C.
• a thermal gradient tester heat seal tester manufactured by Toyo Seiki Seisakusho Co., Ltd.
• test piece was cut out with a width of 15 mm.
• the test piece fused by heat sealing was opened at 180°, the unsealed portion was sandwiched between chucks, and the sealed portion was peeled off. Then, the temperature at which the heat seal strength reached 4.9 N was determined.
• Heat Seal Strength was measured according to JIS Z1707. Show specific steps. Using a heat sealer, the seal layers of the unstretched polyolefin films were adhered to each other using the two laminated films. The heat sealing conditions were an upper bar temperature of 120° C., a lower bar temperature of 30° C., a pressure of 0.2 MPa, and a time of 2 seconds. The adhesive sample was cut so that the seal width was 15 mm. The peel strength was measured using a tensile tester "AGS-KNX" (manufactured by Shimadzu Corporation) at a tensile speed of 200 mm/min. The peel strength is indicated by strength per 15 mm: unit N/15 mm.
• the number of pinholes was measured by the following method.
• the film was placed on filter paper (No. 50, manufactured by Advantech) with the unstretched polyolefin film side facing downward, and the four corners were fixed with Sellotape (registered trademark).
• the resin compositions of the A layer and the B layer are as follows.
• Layer A Polyamide 6 (manufactured by Toyobo Co., Ltd., relative viscosity 2.8, melting point 220 ° C.) 97 parts by mass; and polyamide 11 (manufactured by Shusei Co., Ltd., relative viscosity 2.5, melting point 186 ° C.) 3.0 parts by mass
• Layer B Polyamide 6 (manufactured by Toyobo Co., Ltd., relative viscosity 2.8, melting point 220 ° C.) 95 parts by mass;
• Polyamide MXD6 Mitsubishi Gas Chemical Co., Ltd., relative viscosity 2.1, melting point 237 ° C.) 5.0 parts by mass; Porous silica fine particles (Fuji Silysia Chemical Co., Ltd., average particle diameter 2.0 ⁇ m, pore volume 1.6 ml / g) 0.54 parts by mass; 0.15 parts by mass
• the feed block was configured so that the final total thickness of the biaxially stretched polyamide film was 15 ⁇ m, the thickness of the A layer was 12 ⁇ m, and the thickness of each of the B layers arranged on both sides of the A layer was 1.5 ⁇ m. and the discharge rate of the extruder were adjusted.
• the obtained unstretched film was guided to a roll type stretching machine, and after being stretched 1.73 times in the MD direction at 80°C by utilizing the peripheral speed difference of the rolls, it was further stretched 1.85 times at 70°C. Subsequently, this uniaxially stretched film was continuously guided to a tenter type stretching machine, preheated at 110°C, and stretched in the TD direction at 120°C for 1.2 times, 130°C for 1.7 times, and 160°C for 2.0 times. After being stretched and heat-set at 218° C., it was subjected to a relaxation treatment of 7% at 218° C., and then the surface to be dry-laminated with the sealant layer was subjected to corona discharge treatment to obtain a biaxially stretched polyamide film. Table 1 shows the evaluation results of the obtained biaxially stretched polyamide film.
• Polyamide 410, polyamide 610, and polyamide 1010 which are polyamide resins at least partially containing raw materials derived from biomass, used the following.
• PP-1 Sumitomo Chemical propylene-ethylene-butene random copolymer FL6745A (MFR 6.0 g/10 min, melting point 130 ° C.)
• LL-1 Braskem ethylene-hexene copolymer (plant-derived linear low-density polyethylene) SLH218 (MFR 2.3 g/min, density 916 kg/m 3 , melting point 126°C)
• Silica particles Shin-Etsu Chemical Co., Ltd. amorphous silica KMP130-4 (average particle size 4 ⁇ m)
• Organic lubricant Behenic acid amide BNT-22H manufactured by Nippon Fine Chemical Co., Ltd.
• PP-2 Sumitomo Chemical propylene-ethylene-butene random copolymer FL8115A (MFR 7.0 g/10 min, melting point 148 ° C.)
• PP-3 Propylene homopolymer FLX80E4 manufactured by Sumitomo Chemical Co., Ltd.
• LL-1 Braskem ethylene-hexene copolymer (plant-derived linear low-density polyethylene) SLH218 (MFR 2.3 g/min, density 916 kg/m 3 , melting point 126°C)
• LL-2 Ethylene-hexene copolymer (fossil fuel-derived linear low-density polyethylene) FV405 (MFR 4.0 g/min, density 923 kg/m 3 , melting point 118°C) manufactured by Sumitomo Chemical Co., Ltd.
• LDPE-1 Braskem ethylene-hexene copolymer (plant-derived low-density polyethylene) SLH818 (MFR 8.1 g/min, density 918 kg/m 3 )
• Organic lubricant Behenic acid amide BNT-22H manufactured by Nippon Fine Chemical Co., Ltd.
• PP-2 Sumitomo Chemical propylene-ethylene-butene random copolymer FL8115A (MFR 7.0 g/10 min, melting point 148 ° C.)
• PP-3 Propylene homopolymer FLX80E4 manufactured by Sumitomo Chemical Co., Ltd.
• LL-1 Braskem ethylene-hexene copolymer (plant-derived linear low-density polyethylene) SLH218 (MFR 2.3 g/min, density 916 kg/m 3 , melting point 126°C)
• LL-2 Ethylene-hexene copolymer (fossil fuel-derived linear low-density polyethylene) FV405 (MFR 4.0 g/min, density 923 kg/m 3 , melting point 118°C) manufactured by Sumitomo Chemical Co., Ltd.
• LDPE-1 Braskem ethylene-hexene copolymer (plant-derived low-density polyethylene) SLH818 (MFR 8.1 g/min, density 918 kg/m 3 ) These raw materials were uniformly mixed at the ratios shown in Table 2 to obtain a mixed raw material for producing an unstretched polyolefin film.
• a three-stage single screw extruder with a screw diameter of 90 mm is used for the mixed raw material used for the core layer, and a three-stage single screw extruder with a diameter of 65 mm and a diameter of 45 mm is used for the mixed raw material for the seal layer and the laminate layer, respectively. It was introduced in the order of layer/core layer/laminate layer and extruded using a T-slot die at a die exit temperature of 230°C. The thickness ratios of seal layer/core layer/laminate layer were 25%/50%/25%, respectively.
• the molten resin sheet coming out of the die was cooled with a cooling roll at 35°C to obtain an unstretched polyolefin film with a thickness of 30 ⁇ m.
• both ends of the film on the cooling roll are fixed with air nozzles, the entire width of the molten resin sheet is pressed against the cooling roll with an air knife, and at the same time a vacuum chamber is applied between the molten resin sheet and the cooling roll. Prevents entrainment of air into Both ends of the air nozzle were installed in series in the film traveling direction.
• the die was surrounded by a sheet to prevent wind from hitting the molten resin sheet. Also, the direction of the suction port of the vacuum chamber was aligned with the traveling direction of the extruded sheet.
• the surface of the laminate layer of the film was subjected to corona treatment (power density 20 W ⁇ min/m 2 ).
• the film forming speed was 20 m/min.
• the formed film was trimmed at the edges and wound into a roll.
• CPP2 to CPP14 In CPP1, raw materials shown in Table 2 were used, and an unstretched polyolefin film having a thickness shown in Table 2 was obtained in the same manner. However, for CPP12, the materials shown in Table 2 were used, and an unstretched polyolefin film with a single layer of 30 ⁇ m was obtained in the same manner using an extruder for the core layer only. Table 2 shows the evaluation results of the films of CPP1 to CPP14.
• the laminated films of Examples had good heat seal strength, bending pinhole resistance, and drop bag breakage resistance even when the biomass content was increased.
• the laminated film using the biaxially stretched polyamide film containing no material for modifying the bending pinhole resistance of Comparative Examples 1 and 2 and the biaxially stretched polyamide film containing too little polyamide 11 of Comparative Example 3 the bending pinhole resistance was inferior.
• Comparative Example 4 since the thickness and thickness ratio of the A layer were small, the bending pinhole resistance of the film was inferior.
• the amount of polyamide MXD6 in the layer B was large and the amount of polyamide 6 resin was small, so that the film had poor flex pinhole resistance.
• Comparative Example 6 since linear low-density polyethylene was not added to the core layer and the laminate layer, the bending pinhole resistance was poor.
• Comparative Examples 7 and 8 the difference in the content of linear low-density polyethylene between the seal layer and the core layer was large, so the heat seal strength was poor.
• Comparative Example 9 the content of linear low-density polyethylene in the seal layer was large, so the heat seal strength was poor.
• Comparative Example 10 since a large amount of linear low-density polyethylene was contained over the entire film region, a large amount of linear low-density polyethylene was contained near the surface of the film, resulting in poor heat seal strength.
• Comparative Example 11 the linear low-density polyethylene was contained in the core layer, but the laminate layer did not contain linear low-density polyethylene, so that the bending pinhole resistance was inferior.
• Comparative Example 12 high-pressure low-density polyethylene (LDPE) was added as polyethylene, so the heat seal strength was poor.
• LDPE high-pressure low-density polyethylene

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