Classifications

• • 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
  • 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
  • B32B27/32—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
  • B32B2250/00—Layers arrangement
  • B32B2250/03—3 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
  • B32B2250/242—All polymers belonging to those covered by group B32B27/32
• • 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
  • B32B2255/00—Coating on the layer surface
  • B32B2255/10—Coating on the layer surface on synthetic resin layer or on natural or synthetic rubber layer
• • 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
  • B32B2255/00—Coating on the layer surface
  • B32B2255/20—Inorganic coating
  • B32B2255/205—Metallic coating
• • 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
  • B32B2255/00—Coating on the layer surface
  • B32B2255/24—Organic non-macromolecular coating
• • 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
  • B32B2255/00—Coating on the layer surface
  • B32B2255/28—Multiple coating on one surface
• • 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
  • B32B2307/70—Other properties
  • B32B2307/724—Permeability to gases, adsorption
  • B32B2307/7242—Non-permeable
  • B32B2307/7244—Oxygen barrier
• • 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
  • B32B2307/7246—Water vapor barrier
• • 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
  • B32B2307/748—Releasability
• • 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

Definitions

• the present invention relates to packaging materials that have excellent gas barrier properties and adhesive strength even after being subjected to wet heat treatments such as so-called boiling sterilization and retort sterilization.
• the present invention also relates to a laminate excellent in material recycling aptitude and a packaging material using the same.
• Packaging materials used for foods, pharmaceuticals, etc. must have the property of blocking gases such as oxygen and water vapor, that is, gas barrier properties, in order to suppress the oxidation of proteins and fats, preserve the taste and freshness, and maintain the efficacy of pharmaceuticals. It has been demanded. Further, gas barrier materials used in solar cells, electronic devices such as organic EL, and electronic parts require gas barrier properties higher than those of food packaging materials.
• gas-barrier laminate films which are made by forming thin films of metals such as aluminum, or thin films of inorganic oxides such as silicon oxide and aluminum oxide, on the surface of plastic substrate films, need to block various gases such as water vapor and oxygen. It is commonly used in food applications such as Among them, thin films of inorganic oxides such as silicon oxide, aluminum oxide, and mixtures thereof are widely used because they are transparent and allow confirmation of the contents.
• the above-mentioned gas barrier laminate film becomes locally hot during the formation process, causing damage to the base material, decomposition of low molecular weight parts or additives such as plasticizers, degassing, etc. Defects, pinholes, etc. may be generated in the thin film layer, and the gas barrier properties may deteriorate. Furthermore, there is a problem that the inorganic thin film layer cracks and cracks occur during the post-processing of the packaging material such as printing, lamination, bag making, etc., and the gas barrier property deteriorates.
• various water-based polyurethane resins, polyester resins, or mixtures of polyurethane and polyester are used between the polyester base film and the inorganic thin film layer formed by, for example, vapor deposition.
• a method of providing a coating layer consisting of is known (for example, Patent Document 1).
• gas barrier films obtained by coating a base film with a resin composition.
• coating agents using polyvinyl alcohol or ethylene-vinyl alcohol copolymer, which themselves have high oxygen barrier properties, have been put to practical use.
• a gas barrier film has been proposed in which a base film made of plastic is coated with a gas barrier layer obtained by blending an inorganic layered compound such as montmorillonite with the vinyl alcohol resin.
• a layer having gas barrier properties composed of polyvinyl alcohol, a cross-linking agent, and an inorganic stratiform compound is provided on the substrate film.
• An example of providing a layer having gas barrier properties made of an inorganic stratiform compound see, for example, Patent Documents 2 and 3). Since these gas barrier films are crosslinked resins, they can withstand moisture resistance and boiling water resistance. However, the gas barrier property and lamination strength of the film were not sufficiently satisfactory.
• the present invention has been made against the background of such problems of the prior art, and its object is to provide a laminate having excellent oxygen and water vapor barrier properties even after retort treatment and adhesion that does not cause delamination after retort treatment. to provide the film.
• the present inventors have found that by designing a predetermined laminated film that meets the required performance, it is possible to provide a film that maintains good gas barrier properties and adhesion even when subjected to retort treatment. I have completed my invention.
• the present invention consists of the following configurations.
• an anchor coat layer and an inorganic thin film layer are formed via other layers. Or a laminated film laminated in this order without an intervening layer, wherein the surface layer (B) is made of a resin composition containing two or more resins, and the adhesion amount of the anchor coat layer is less than 0.50 g/m 2 and a moisture content of the laminated film of 0.2% by mass or less.
• the anchor coat layer contains at least one of polyester resin and polyurethane resin. Laminated film according to. 3.
• the inorganic thin film layer is made of a metal oxide; or 2.
• the substrate layer (A) is made of a resin containing polyolefin as a main component. ⁇ 3.
• a laminate comprising the laminate film according to any one of the above and an olefinic sealant layer laminated on the surface opposite to the surface layer (C). 6. 5.
• the laminate has a lamination strength of 2.0 N/15 mm or more; The laminate according to . 7.
• the oxygen permeability value of the laminate measured under conditions of 23 ° C.
• x 65% RH is defined as (A), and after being subjected to retort treatment in which it is held in pressurized hot water at a temperature of 130 ° C. for 30 minutes, 23 ° C. x 5.
• the barrier value deterioration rate after wet heat treatment represented by the following formula is 150% or less, where (B) is the value of oxygen permeability measured under 65% RH conditions; or 6.
• Barrier value deterioration rate (%) after wet heat treatment (B/A) ⁇ 100 Formula (1) 8. 1 above. ⁇ 4. 5.
• a packaging material comprising at least one layer of the laminate according to 1.
• the inventors of the present invention have made it possible to provide a laminate that has necessary properties such as barrier properties and adhesive properties required for packaging materials even after retorting.
• an anchor coat layer and an inorganic thin film layer are formed via other layers.
• a laminated film laminated in this order without an intervening layer wherein the surface layer (B) is made of a resin composition containing two or more resins, and the adhesion amount of the anchor coat layer is less than 0.50 g/m 2 and a moisture content of the laminated film of 0.2% by mass or less.
• Base layer (A) It is preferable that the base material layer of the present invention contains a polyolefin such as polypropylene or polyethylene resin as a main component so that the moisture content in the laminated film is 0.20% by mass or less.
• the term "main component” means that a specific component accounts for 50% by mass or more of all components, more preferably 80% by mass or more, still more preferably 90% by mass or more, and particularly preferably It is 95% by mass or more.
• Polypropylene obtained by copolymerizing 0.5 mol % or less of ethylene and/or an ⁇ -olefin having 4 or more carbon atoms can also be used as the polypropylene used for the layer.
• Such copolymerized polypropylene is also included in the polypropylene of the present invention (hereinafter referred to as polypropylene).
• the content of the copolymer component is preferably 0.3 mol % or less, more preferably 0.1 mol % or less, and most preferably complete homopolypropylene containing no copolymer component.
• ethylene and/or ⁇ -olefins having 4 or more carbon atoms are copolymerized in excess of 0.5 mol %, the crystallinity and rigidity are excessively lowered, and the thermal shrinkage at high temperatures may increase.
• a blend of such resins may be used.
• the mesopentad fraction ([mmmm]%) measured by 13C-NMR, which is an index of stereoregularity, of the polypropylene constituting the base layer (A) of the laminated film of the present invention is 98 to 99.5%. is preferred. More preferably, it is 98.1% or more, and still more preferably 98.2% or more.
• the mesopentad ratio of polypropylene is small, the elastic modulus is low, and the heat resistance may be insufficient. 99.5% is a realistic upper limit.
• the weight-average molecular weight (Mw) of polypropylene constituting the base layer (A) of the laminated film of the present invention is preferably 180,000 to 500,000. If it is less than 180,000, the melt viscosity is so low that it may not be stable during casting, resulting in poor film formability. If Mw exceeds 500,000, the amount of components having a molecular weight of 100,000 or less will be 35% by mass, resulting in poor heat resistance.
• a more preferable lower limit of Mw is 190,000, more preferably 200,000, and a more preferable upper limit of Mw is 320,000, more preferably 300,000, and particularly preferably 250,000.
• the number average molecular weight (Mn) of the polypropylene constituting the base layer (A) of the laminated film of the present invention is preferably 20,000 to 200,000. If it is less than 20,000, the melt viscosity is so low that it may not be stable during casting, resulting in poor film formability. If it exceeds 200,000, the heat resistance deteriorates.
• a more preferable lower limit of Mn is 30,000, more preferably 40,000, particularly preferably 50,000, and a more preferable upper limit of Mn is 80,000, more preferably 70,000, particularly preferably 60,000. be.
• Mw/Mn which is an index of molecular weight distribution
• Mw/Mn is preferably 2.8 to 10 for the polypropylene constituting the base material layer (A). It is more preferably 2.8 to 8, still more preferably 2.8 to 6, and particularly preferably 2.8 to 5.4. Also, the lower limit is preferably 3 or more, more preferably 3.3 or more.
• the molecular weight distribution of polypropylene can be determined by polymerizing components with different molecular weights in multiple stages in a series of plants, by blending components with different molecular weights offline in a kneader, or by blending catalysts with different performance. or by using a catalyst capable of realizing a desired molecular weight distribution.
• the polypropylene constituting the base layer (A) of the laminated film of the present invention has a melt flow rate (MFR; 230 ° C., 2.16 kgf) of 2 g when Mw / Mn is in the range of 2.8 to 5.4. /10 min to 20 g/10 min.
• the lower limit of the MFR of the polypropylene of the substrate layer (A) is more preferably 3 g/10 minutes, even more preferably 4 g/10 minutes, and particularly preferably 5 g/10 minutes.
• the upper limit of the MFR of the polypropylene constituting the base material layer (A) is more preferably 15 g/10 minutes, still more preferably 12 g/10 minutes.
• the surface layer (B) of the present invention contains polyolefin such as polypropylene or polyethylene resin as a main component so that the water content in the laminated film is 0.20% by mass or less.
• the term "main component” means that a specific component accounts for 50% by mass or more of all components, more preferably 80% by mass or more, still more preferably 90% by mass or more, and particularly preferably It is 95% by mass or more.
• polypropylene will be described as an example.
• the polypropylene resin composition constituting the surface layer (B) of the laminated film of the present invention comprises a resin composition containing two or more resins, and has an MFR of 1.0 g/10 min to 10.0 g/10 min. is preferred.
• the lower limit of the MFR of the polypropylene resin composition constituting the surface layer (B) is more preferably 2.0 g/10 minutes, still more preferably 3.0 g/10 minutes, and 4.0 g/10 minutes. is particularly preferred.
• the upper limit of the MFR of the polypropylene resin composition constituting the surface layer (B) is more preferably 9.0 g/10 minutes, still more preferably 8.0 g/10 minutes, and 5.5 g/10 minutes. is particularly preferred. Within this range, the film formability is good and the appearance is excellent.
• the MFR of the polypropylene resin composition constituting the surface layer (B) is less than 1.0 g/10 min, and when the MFR of the polypropylene constituting the base layer (A) is large, the base layer (A) and the surface layer Since the difference in viscosity of (B) becomes large, unevenness (raw fabric unevenness) tends to occur during film formation.
• the MFR of the polypropylene resin composition constituting the surface layer (B) exceeds 10 g/10 minutes, the adhesion to the cooling roll deteriorates, air is entrained, and the smoothness is poor, which is the starting point of defects. It is possible that there will be more.
• Polypropylene obtained by copolymerizing ethylene and/or an ⁇ -olefin having 4 or more carbon atoms can also be used as the polypropylene resin having a smaller MFR.
• ⁇ -olefins having 4 or more carbon atoms include 1-butene, 1-hexene, 4-methyl-1-pentene, and 1-octene.
• maleic acid or the like having polarity may be used as another copolymerization component.
• the total content of ethylene and/or ⁇ -olefins having 4 or more carbon atoms and other copolymer components is preferably 8.0 mol % or less. If it is copolymerized in excess of 8.0 mol %, the film may turn white and have a poor appearance, or may become sticky and difficult to form.
• Each resin to be blended may be copolymerized in an amount of more than 8.0 mol %, but the blend preferably contains 8.0 mol % or less of monomers other than propylene per monomer unit.
• the polypropylene-based resin having a larger MFR the above-mentioned copolymerized polypropylene can be used, and a homopolypropylene resin can also be used.
• the polypropylene-based resin composition constituting the surface layer (B) of the laminated film of the present invention is preferably a mixture of resin compositions having different crystallinities.
• the degree of crystallinity can be partially changed on the film surface, and the surface roughness of the film can be controlled.
• the hardness of the surface can be controlled within a desired range, and it is speculated that these effects enable the adhesion to be maintained even after boiling or retorting.
• the anti-blocking agent inorganic particles such as silica, calcium carbonate, kaolin, and zeolite, and organic particles such as acrylic, polymethacrylic, and polystyrene particles can be appropriately selected and used. Among these, it is particularly preferable to use silica and polymethacrylic particles.
• the average particle size of the antiblocking agent is preferably 1.0-3.0 ⁇ m, more preferably 1.0-2.7 ⁇ m.
• the method of measuring the average particle diameter as used herein is to take a photograph with a scanning electron microscope, measure the Feret diameter in the horizontal direction using an image analyzer, and display the average value.
• the amount of the antiblocking agent added to the surface layer (B) and the surface layer (C) is such that the haze, dynamic friction coefficient, center surface average roughness (SRa), and air release time are within the predetermined ranges. is adjusted, there is no particular limitation.
• the surface wetting tension of the surface layer (B) of the laminated film of the present invention is preferably 38 mN/m or more.
• the wetting tension represents the numerical value of the surface tension (mN/m) of the mixed solution reagent determined to wet the film surface, and is related to the wettability of the printing ink or adhesive.
• the wetting tension is 38 mN/m or more, the adhesion with the adhesive used for lamination with vapor deposition films, coating films, and films of other members is improved.
• additives such as antistatic agents and surfactants are usually used.
• Physicochemical surface treatments such as corona treatment and heat treatment are preferably performed. For example, in corona treatment, it is preferable to use a preheated roll and a treatment roll to perform discharge in the air.
• the laminated film of the present invention may have a surface layer (C) on the surface of the substrate layer (A) opposite to the surface layer (B).
• the main component of the surface layer (C) of the present invention is preferably polyolefin such as polypropylene or polyethylene resin, since the moisture content in the laminated film is 0.20% by mass or less.
• the term "main component” means that a specific component accounts for 50% by mass or more of all components, more preferably 80% by mass or more, still more preferably 90% by mass or more, and particularly preferably It is 95% by mass or more.
• Polypropylene obtained by copolymerizing 0.5 mol % or less of ethylene and/or an ⁇ -olefin having 4 or more carbon atoms can also be used as the polypropylene used for the layer.
• Such copolymerized polypropylene is also included in the polypropylene of the present invention (hereinafter referred to as polypropylene).
• the content of the copolymer component is preferably 0.3 mol % or less, more preferably 0.1 mol % or less, and most preferably complete homopolypropylene containing no copolymer component.
• the surface layer (C) preferably has a center surface average roughness (SRa) of 0.020 ⁇ m or more as determined by a three-dimensional surface roughness meter.
• the center plane average roughness (SRa) of the surface layer (C) is more preferably 0.022 ⁇ m or more, still more preferably 0.025 ⁇ m or more, and particularly preferably 0.028 ⁇ m or more. If the surface center plane average roughness (SRa) of the surface layer (C) is less than 0.020 ⁇ m, the surface unevenness is small, and the slipperiness of the film, the air release time between films, and the blocking resistance deteriorate.
• the surface layer (C) of the laminate of the present invention preferably has a center plane average roughness (SRa) of 0.040 ⁇ m or less measured by a three-dimensional roughness meter.
• the polypropylene resin used in the present invention is obtained by polymerizing raw material propylene using a known catalyst such as a Ziegler-Natta catalyst or a metallocene catalyst. Among them, it is preferable to use a Ziegler-Natta catalyst in order to eliminate heterogeneous bonds, and to use a catalyst capable of polymerizing with high stereoregularity.
• a known method for polymerizing propylene as a raw material a known method may be adopted. A method of adding a catalyst to a monomer and polymerizing in a gas phase, or a method of polymerizing by combining these methods can be used.
• the base layer (A) and/or the surface layer (B) and/or the surface layer (C) of the laminated film of the present invention may contain additives and other resins.
• additives include antioxidants, ultraviolet absorbers, nucleating agents, adhesives, antifog agents, flame retardants, inorganic or organic fillers, and the like.
• Other resins include polypropylene resins other than the polypropylene resin used in the present invention, random copolymers that are copolymers of propylene and ethylene and/or ⁇ -olefins having 4 or more carbon atoms, and various elastomers.
• the base film of the present invention it is preferable that it is a biaxially oriented film, and a polypropylene resin composition constituting the base layer (A) and a polypropylene resin composition constituting the surface layer (B).
• the polypropylene resin composition constituting the surface layer (C) is melt-extruded by separate extruders, co-extruded from a die, cooled by cooling rolls to form an unstretched sheet, and the unstretched sheet is longitudinally It can be obtained by stretching in the direction (MD) and the transverse direction (TD), followed by heat setting.
• the melt extrusion temperature is preferably about 200 to 280° C.
• polypropylene raw material for the base layer (A) and polypropylene for the surface layer (B) It is preferable to set the viscosity difference (MFR difference) of the raw materials to 6.0 g/10 minutes or less. If the viscosity difference is more than 6 g/10 minutes, the layers tend to be disordered and the appearance is poor.
• the viscosity difference is more preferably 5.5 g/10 minutes or less, still more preferably 5.0 g/10 minutes or less.
• the cooling roll surface temperature is preferably 25 to 35°C, more preferably 27 to 33°C.
• the lower limit of the draw ratio in the machine direction (MD) is preferably 3 times, more preferably 3.5 times. If it is less than the above, the film thickness may become uneven.
• the upper limit of the MD draw ratio is preferably 8 times, more preferably 7 times. If the above is exceeded, it may become difficult to perform subsequent TD stretching.
• the lower limit of the MD stretching temperature is preferably 120°C, more preferably 125°C, and still more preferably 130°C. If it is less than the above, the mechanical load may increase, the thickness unevenness may increase, and the surface of the film may become rough.
• the upper limit of the MD stretching temperature is preferably 160°C, more preferably 155°C, still more preferably 150°C. The higher the temperature, the smaller the dimensional change during wet heat treatment, which is preferable because it can reduce the deterioration of barrier properties and adhesiveness.
• the lower limit of the draw ratio in the width direction (TD) is preferably 4 times, more preferably 5 times, and still more preferably 6 times. If it is less than the above, thickness unevenness may occur.
• the upper limit of the TD draw ratio is preferably 20 times, more preferably 17 times, still more preferably 15 times, and particularly preferably 12 times. If the above is exceeded, the heat shrinkage rate may increase, or breakage may occur during stretching.
• the preheating temperature in TD stretching is preferably set 5 to 15° C. higher than the stretching temperature in order to quickly raise the film temperature to the vicinity of the stretching temperature.
• the lower limit of the TD stretching temperature is preferably 150°C, more preferably 155°C, even more preferably 158°C, and particularly preferably 160°C.
• the upper limit of the TD stretching temperature is preferably 170°C, more preferably 168°C, still more preferably 165°C. In order to reduce the dimensional change, a higher temperature is preferable, but if the temperature exceeds the above range, the low-molecular-weight components melt and recrystallize, which not only lowers the orientation but also causes surface roughness and whitening of the film.
• the film after stretching is heat-set.
• the lower limit of the heat setting temperature is preferably 163°C, more preferably 165°C. If it is less than the above, the dimensional change is large during wet heat treatment, and the barrier properties and adhesion may deteriorate. In addition, long-time treatment is required to reduce dimensional change, which may result in poor productivity.
• the upper limit of the heat setting temperature is preferably 176°C, more preferably 175°C. If the above is exceeded, the low-molecular-weight components may melt and recrystallize, resulting in surface roughness and whitening of the film.
• the lower limit of the relaxation rate is preferably 2%, more preferably 3%. When it is less than the above, the dimensional change is large during the wet heat treatment, and the barrier properties and adhesion may be deteriorated.
• the upper limit of the relaxation rate is preferably 10%, more preferably 8%. When the above is exceeded, thickness unevenness may become large.
• the film produced by the above process can be once wound into a roll and then annealed off-line.
• the biaxially oriented polypropylene laminate thus obtained is optionally subjected to corona discharge, plasma treatment, flame treatment, etc., and then wound with a winder to obtain the biaxially oriented polypropylene film roll of the present invention. can be done.
• an anchor coat layer is provided on the surface layer (B).
• the anchor coat layer By having the anchor coat layer, it is possible to suppress exposure of oligomers and anti-blocking materials from the polypropylene resin. Furthermore, when laminating another layer on the anchor coat layer, it is also possible to increase the adhesion between the layers. In particular, in the formation of an inorganic thin film layer, there is a problem that not only the adhesive strength but also the thin film cannot be formed at the protrusions due to the unevenness of the surface, resulting in poor barrier properties and the like. In addition, by using a material having gas barrier properties for the anchor coat layer itself, the gas barrier properties of the laminate can be greatly improved.
• a water-resistant anchor coat layer prevents hot water from penetrating, and as a result, defects such as barrier properties and adhesion after boiling and retorting can be reduced.
• the anchor coat layer incorporates a resin component having a polar group or the like in order to ensure necessary adhesion, it is often made of a material with a high moisture content.
• the present inventors have newly discovered that the defects after the wet heat treatment can be improved by controlling the moisture content of the entire laminated film to a predetermined amount. In order to control the moisture content of the laminated film within the preferred range described below, it is necessary to employ a composition and/or processing conditions that exhibit adhesion and barrier properties in the anchor coat layer with a small amount of adhesion described below.
• the amount of the anchor coat layer applied is 0.01 to 0.50 g/m 2 .
• the adhesion amount of the anchor coat layer is preferably 0.05 g/m 2 or more, more preferably 0.10 g/m 2 or more, and preferably 0.47 g/m 2 or less, more preferably 0.45 g/m 2 . It is below. If the amount of the anchor coat layer deposited exceeds 0.50 g/m 2 , the gas barrier property is improved, but the thick film tends to increase the water content in the laminated film. In terms of workability, blocking may occur due to the thick film thickness.
• the film thickness of the protective layer is less than 0.01 g/m 2 , sufficient gas barrier properties and interlayer adhesion may not be obtained.
• the resin composition used for the anchor coat layer of the present invention includes urethane-, polyester-, acrylic-, titanium-, isocyanate-, imine-, and polybutadiene-based resins, and epoxy-, isocyanate-, and melamine-based resins.
• the one to which the agent was added is mentioned.
• a cross-linking agent such as a silicon-based cross-linking agent, an oxazoline compound, a carbodiimide compound and an epoxy compound can be included.
• the inclusion of urethane resin in addition to the barrier performance due to the high cohesion of the urethane bond itself, the polar group interacts with the inorganic thin film layer, and the presence of the amorphous part also provides flexibility, so the load from wet heat treatment is reduced. It is preferable because damage can be suppressed even when it is applied.
• a polyester resin is also suitable because a similar effect can be expected.
• Urethane resin used in the present invention preferably has a glass transition temperature (Tg) of 100°C or higher, more preferably 110°C or higher, and still more preferably 120°C, from the viewpoint of improving barrier properties due to cohesion. °C or higher.
• Tg glass transition temperature
• a flexible resin having excellent flexibility and a Tg of 100° C. or less may be mixed and used.
• the addition ratio of the flexible resin is preferably in the range of 0 to 80%. It is more preferably in the range of 10 to 70%, still more preferably in the range of 20 to 60%. When the addition ratio is within the above range, both cohesion and flexibility can be achieved, and barrier properties and adhesion are improved. If the addition ratio exceeds 80%, the film becomes too soft and the barrier performance is lowered.
• the urethane resin it is more preferable to use a urethane resin containing an aromatic or araliphatic diisocyanate component as a main component from the viewpoint of improving gas barrier properties.
• a urethane resin containing an aromatic or araliphatic diisocyanate component it is particularly preferable to contain a meta-xylylene diisocyanate component.
• the ratio of the aromatic or araliphatic diisocyanate in the urethane resin is preferably in the range of 50 mol% or more (50 to 100 mol%) in 100 mol% of the polyisocyanate component (F).
• the proportion of the total amount of aromatic or araliphatic diisocyanates is preferably 60-100 mol %, more preferably 70-100 mol %, still more preferably 80-100 mol %. If the total amount of aromatic or araliphatic diisocyanates is less than 50 mol %, good gas barrier properties may not be obtained.
• Silicon-based cross-linking agent Various cross-linking agents may be added to the urethane resin used in the present invention for the purpose of improving the cohesive strength of the film and improving the wet heat resistant adhesion within a range that does not impair the gas barrier properties.
• cross-linking agents include silicon-based cross-linking agents, oxazoline compounds, carbodiimide compounds, and epoxy compounds.
• the silicon-based cross-linking agent is particularly preferable from the viewpoint that the water-resistant adhesiveness to the inorganic thin film layer can be particularly improved by blending the silicon-based cross-linking agent.
• an oxazoline compound, a carbodiimide compound, an epoxy compound, or the like may be used in combination.
• silane coupling agent As the silicon-based cross-linking agent, a silane coupling agent is preferable from the viewpoint of cross-linking between an inorganic substance and an organic substance.
• silane coupling agents include hydrolyzable alkoxysilane compounds such as halogen-containing alkoxysilanes (2-chloroethyltrimethoxysilane, 2-chloroethyltriethoxysilane, 3-chloropropyltrimethoxysilane, 3-chloropropyltrimethoxysilane, chloro C2-4 alkyltri-C1-4 alkoxysilanes such as ethoxysilane), alkoxysilanes having an epoxy group [2-glycidyloxyethyltrimethoxysilane, 2-glycidyloxyethyltriethoxysilane, 3-glycidyloxypropyltrimethoxysilane silane, glycidyloxy C2-4 alkyltri-C
• silane coupling agents can be used alone or in combination of two or more. Among these silane coupling agents, silane coupling agents having an amino group are preferred.
• the silicon-based cross-linking agent is preferably added in an amount of 0.05 to 4.00% by mass, more preferably 0.10 to 3.50% by mass, and still more preferably 0.15 to 3.00% by mass. is.
• Addition of a silane coupling agent promotes curing of the film and improves cohesion, resulting in a film with excellent water-resistant adhesiveness, and is expected to have the effect of preventing the appearance of oligomers. If the amount added exceeds 3.00% by mass, the film will be cured and the cohesive strength will be improved, but some unreacted portions will be formed, and the adhesion between layers may be reduced. On the other hand, if the amount added is less than 0.05% by mass, sufficient cohesion may not be obtained.
• polyester resin used in the present invention is produced by polycondensing a polyhydric carboxylic acid component and a polyhydric alcohol component.
• the molecular weight of the polyester is not particularly limited as long as it can impart sufficient film toughness, coatability and solvent solubility as a coating material, but the number average molecular weight is 1000 to 50000, more preferably 1500 to 30000.
• the functional group at the end of the polyester is not particularly limited, and may have an alcohol end, a carboxylic acid end, or both. However, when an isocyanate-based curing agent is used in combination, it is necessary to use a polyester polyol mainly having alcohol terminals.
• the Tg of the polyester used in the present invention is preferably 15°C or higher. If the temperature is lower than this, the resin becomes sticky after the coating operation, and blocking is likely to occur, making it difficult to wind the film after coating. This is because when the Tg is 15° C. or less, it becomes difficult to prevent blocking even when the pressure in the vicinity of the winding core is high, even with the addition of an antiblocking material.
• a more preferable Tg temperature is 18° C. or higher, more preferably 25° C. or higher.
• the polyester used in the present invention is used by polycondensing a polyhydric carboxylic acid component and a polyhydric alcohol component.
• Polyvalent carboxylic acid component The polyvalent carboxylic acid component of the polyester used in the present invention is characterized by containing at least one ortho-oriented aromatic dicarboxylic acid or its anhydride.
• the ortho-orientation improves the solubility in a solvent and enables uniform coating of the resin.
• a uniformly coated protective layer has less variation in barrier performance, and as a result contributes to the suppression of oligo-whitening.
• the ortho-orientation results in a film with excellent flexibility and improved interfacial adhesive strength, so that damage to the resin due to wet heat treatment can be reduced, leading to suppression of oligomer formation.
• aromatic polyvalent carboxylic acid or its anhydride in which the carboxylic acid is substituted at the ortho position examples include orthophthalic acid or its anhydride, naphthalene 2,3-dicarboxylic acid or its anhydride, naphthalene 1,2-dicarboxylic acid or its anhydride. anhydride, anthraquinone 2,3-dicarboxylic acid or its anhydride, 2,3-anthracenecarboxylic acid or its anhydride, and the like. These compounds may have a substituent at any carbon atom of the aromatic ring.
• the substituents include chloro, bromo, methyl, ethyl, i-propyl, hydroxyl, methoxy, ethoxy, phenoxy, methylthio, phenylthio, cyano, nitro, amino, phthalimido group, carboxyl group, carbamoyl group, N-ethylcarbamoyl group, phenyl group, naphthyl group and the like.
• a polyester polyol having a content of 70 to 100 mol% with respect to 100 mol% of the total polycarboxylic acid component has a high effect of improving barrier properties and has excellent solvent solubility, which is essential as a coating material. is particularly preferred from
• aliphatic polycarboxylic acids include succinic acid, adipic acid, azelaic acid, sebacic acid, dodecanedicarboxylic acid, etc.
• unsaturated bond-containing polycarboxylic acids include maleic anhydride, maleic acid, Fumaric acid and the like, 1,3-cyclopentanedicarboxylic acid and 1,4-cyclohexanedicarboxylic acid as alicyclic polycarboxylic acids, and terephthalic acid, isophthalic acid, and pyromellitic acid as aromatic polycarboxylic acids acids, trimellitic acid, 1,4-naphthalenedicarboxylic acid, 2,5-naphthalenedicarboxylic acid, 2,6-naphthalenedicarboxylic acid, naphthalic acid, biphenyldicarboxylic acid, dip
• succinic acid 1,3-cyclopentanedicarboxylic acid, isophthalic acid, 2,6-naphthalenedicarboxylic acid, 1,8-naphthalic acid, and diphenic acid are preferred from the viewpoint of solubility in organic solvents and gas barrier properties.
• the polyhydric alcohol component of the polyester used in the present invention is not particularly limited as long as it is possible to synthesize a polyester exhibiting gas barrier filling performance. It preferably contains a polyhydric alcohol component containing at least one selected from the group consisting of -bishydroxyethylbenzene. Among them, it is presumed that the smaller the number of carbon atoms between the oxygen atoms, the less the molecular chain becomes excessively flexible and the more difficult it is for oxygen to permeate.
• diols include 1,5-pentanediol, 3-methyl-1,5-pentanediol, 1,6-hexanediol, methylpentanediol, dimethylbutanediol, butylethylpropanediol, diethylene glycol, and triethylene.
• Glycol, tetraethylene glycol, dipropylene glycol, and tripropylene glycol, and trihydric or higher alcohols include glycerol, trimethylolpropane, trimethylolethane, tris(2-hydroxyethyl)isocyanurate, and 1,2,4-butane. triol, pentaerythritol, dipentaerythritol and the like.
• polyesters using glycerol and tris(2-hydroxyethyl)isocyanurate in combination have good solubility in organic solvents due to their branched structure and moderately high crosslink density. It also has an excellent barrier function and is particularly preferably used.
• the catalyst used in the reaction to obtain the polyester of the present invention includes tin-based catalysts such as monobutyl tin oxide and dibutyl tin oxide, titanium-based catalysts such as tetra-isopropyl-titanate and tetra-butyl-titanate, and tetra-butyl-zirconate and the like. Acid catalysts such as zirconia catalysts can be mentioned. It is preferable to use a combination of the above titanium-based catalyst such as tetra-isopropyl-titanate, tetra-butyl-titanate, etc. and the above-mentioned zirconia catalyst, which have high activity for the ester reaction.
• tin-based catalysts such as monobutyl tin oxide and dibutyl tin oxide
• titanium-based catalysts such as tetra-isopropyl-titanate and tetra-butyl-titanate, and
• the amount of the catalyst used is 1 to 1000 ppm, more preferably 10 to 100 ppm, based on the total mass of the reactants used. If it is less than 1 ppm, it is difficult to obtain the effect as a catalyst, and if it exceeds 1000 ppm, a problem of inhibiting the urethanization reaction may occur when an isocyanate curing agent is used.
• the coating liquid can be diluted and reused, and in addition, there is no need for a curing process (so-called aging process).
• aging process a curing process
• the terminal of the polyester to be used can be a polyol, a polycarboxylic acid, or a mixture of the two without any problem.
• the resin of the coating layer is linear, there are cases where heat resistance and wear resistance are not sufficient, and there are cases where it is difficult to use for boiling or retort packaging.
• the resin component of the coating material must be polyester polyol.
• an epoxy-based compound when used as a curing agent, it must be a polyester polycarboxylic acid.
• the coating layer becomes a crosslinked system, there is an advantage that heat resistance, wear resistance and rigidity are improved. Therefore, it is easy to use for boiling and retort packaging.
• the polyisocyanate compound used in the present invention reacts at least in part to form a urethane structure, making it highly polar as a resin component and cohesion between polymer chains to further strengthen the gas barrier function. can.
• the resin of the coating material is a straight-chain resin
• cross-linking with a trivalent or higher polyisocyanate can impart heat resistance and abrasion resistance.
• the polyisocyanate compound used in the present invention may be any of diisocyanate, trivalent or higher polyisocyanate, low-molecular-weight compound, and high-molecular-weight compound.
• Gas barrier can be improved by containing an aromatic ring or an aliphatic ring in part of the skeleton.
• aromatic ring-containing isocyanates include toluene diisocyanate, diphenylmethane diisocyanate, xylylene diisocyanate and naphthalene diisocyanate
• aliphatic ring-containing isocyanates include hydrogenated xylylene diisocyanate, hydrogenated toluene diisocyanate, isophorone diisocyanate, and norborne diisocyanate.
• a terminal isocyanate group-containing compound obtained by reacting with a molecularly active hydrogen compound or a polymeric active hydrogen compound such as various polyester polyols, polyether polyols, and polyamides can be used.
• the coating method of the resin composition for the anchor coat layer is not particularly limited as long as it is a method of coating the film surface to form a layer.
• ordinary coating methods such as gravure coating, reverse roll coating, wire bar coating and die coating can be employed.
• the resin composition for the anchor coat layer When forming the anchor coat layer, it is preferable to apply the resin composition for the anchor coat layer and then heat-dry it. More preferably, it is 110 to 160°C. If the drying temperature is lower than 90°C, the anchor coat layer may be insufficiently dried, or film formation of the anchor coat layer may not proceed, resulting in reduced cohesive strength and water-resistant adhesion, resulting in reduced barrier properties and hand tearability. There is a risk of On the other hand, if the drying temperature exceeds 180° C., the film may become brittle due to excessive heat, resulting in reduced puncture strength or shrinkage, resulting in poor workability. In particular, by drying at 100° C. or higher, preferably 110° C. or higher, film formation of the anchor coat layer effectively proceeds, and water-resistant adhesiveness can be improved. In addition to drying, additional heat treatment in the lowest possible temperature range is also effective in advancing the formation of the anchor coat layer.
• the moisture content in the laminated film can be controlled to a predetermined amount.
• Preferred temperature conditions for the heat treatment are 25°C to 80°C, more preferably 30°C to 70°C, still more preferably 35°C to 60°C. If the heat treatment temperature is 20° C. or less, the effect of the heat treatment is small, and it becomes difficult to control the moisture content. On the other hand, if the temperature of the heat treatment exceeds 80° C., the laminate film is subjected to too much heat, which causes poor appearance such as wrinkles.
• the preferred time for the heat treatment varies depending on the amount of the anchor coat layer attached and the temperature, for example, when the treatment is performed at 40° C., it is preferably 24 hours or longer, more preferably 48 hours or longer, and still more preferably 72 hours or longer. .
• the ratio (P1/P2) of (P2) is preferably in the range of 1.0 or more and 10.0 or less. It is preferably in the range of 1.2 to 9.0, more preferably in the range of 1.5 to 8.0.
• a peak at 1250 ⁇ 50 cm ⁇ 1 is a peak derived from a C—O—C structure derived from an aromatic or unsaturated aliphatic skeleton, and serves as an indicator of the degree of cross-linking of the polyester or polyurethane skeleton.
• the peak at 1070 ⁇ 10 cm ⁇ 1 is a peak derived from C—OH, and serves as an index indicating the amount of hydroxyl groups derived from the polyester or polyurethane skeleton in the anchor coat layer.
• P1/P2 represents the ratio of hydroxyl groups in the polyester or polyurethane skeleton, and when this ratio is within the above range, the film becomes highly polar while controlling the water content to a predetermined amount, and the anchor coat layer and the inorganic The adhesion of the thin film layer increases, and as a result, the gas barrier performance and adhesion are maximized even after the wet heat treatment.
• (P1/P2) When (P1/P2) is less than 1.0, the amount of hydroxyl groups in the anchor coat layer is large, and although the bonding strength with the inorganic thin film layer is strengthened, cross-linking in the anchor coat layer does not proceed, resulting in poor film-forming properties.
• the anchor coat layer tends to become brittle, and the moisture content increases due to the presence of many polar groups in the anchor coat layer.
• (P1/P2) exceeds 10.0, the amount of hydroxyl groups in the anchor coat layer is small, the film formation of the inorganic thin film layer becomes sparse, and gas barrier properties and adhesion may be difficult to obtain.
• the above-described materials are used to achieve the above-described predetermined adhesion amount, and furthermore, the compounding ratio of the materials is set within the above-described appropriate range. , must be combined with the drying and heat treatment conditions described above.
• the laminate of the present invention has an inorganic thin film layer.
• the inorganic thin film layer is preferably a metal oxide layer.
• the material for forming the metal oxide layer is not particularly limited as long as it can be made into a thin film. Oxides are preferred.
• the mixing ratio of silicon oxide and aluminum oxide is preferably in the range of 20 to 70% by mass of Al based on the mass ratio of the metal component. If the Al concentration is less than 20% by mass, the water vapor barrier properties may deteriorate. On the other hand, if it exceeds 70% by mass, the metal oxide layer tends to be hardened, and there is a risk that the film will be destroyed after wet heat treatment and the gas barrier property will be lowered.
• silicon oxide means various silicon oxides such as SiO and SiO 2 or mixtures thereof
• aluminum oxide means various aluminum oxides such as AlO and Al 2 O 3 or mixtures thereof.
• the mixing ratio of silicon oxide and aluminum oxide in this mixture can be determined by a monitor that measures the composition using fluorescent X-rays. It irradiates an object to be measured with X-rays, measures the intensity of characteristic X-rays generated from atoms contained in the object, converts it into a composition, and outputs the value. The conversion is based on a calibration curve prepared from the relationship with the fluorescent X-rays obtained by measuring an object to be measured having a known film thickness composition.
• the plastic substrate film contains the same atoms as those contained in the inorganic thin film layer, for example, SiOx as the inorganic thin film layer, and Si atoms are commonly contained when the plastic film contains silica powder as a lubricant.
• a film is prepared in advance by forming an inorganic thin film layer with a different known thickness on a plastic substrate film containing the atoms at the same concentration, and the measurement is performed with the monitor.
• An unknown inorganic thin film layer thickness can be obtained from a calibration curve prepared by obtaining a relational expression between the obtained fluorescent X-ray intensity and the film thickness.
• the film thickness of the inorganic thin film layer is usually 1 to 100 nm, preferably 5 to 50 nm. If the thickness of the inorganic thin film layer is less than 1 nm, it may be difficult to obtain satisfactory gas barrier properties. It is rather disadvantageous in terms of bending resistance and manufacturing cost.
• the method for forming the inorganic thin film layer is not particularly limited, and known vapor deposition methods such as physical vapor deposition (PVD method) such as vacuum vapor deposition, sputtering, and ion plating, or chemical vapor deposition (CVD method). Laws should be adopted accordingly.
• PVD method physical vapor deposition
• CVD method chemical vapor deposition
• a typical method for forming an inorganic thin film layer will be described below using a silicon oxide/aluminum oxide thin film as an example.
• a vacuum deposition method a mixture of SiO 2 and Al 2 O 3 or a mixture of SiO 2 and Al is preferably used as the deposition raw material.
• Particles are usually used as these vapor deposition raw materials, and in this case, the size of each particle is desirably such that the pressure during vapor deposition does not change, and the preferred particle diameter is 1 mm to 7 mm.
• heating methods such as resistance heating, high-frequency induction heating, electron beam heating, and laser heating can be employed. It is also possible to introduce oxygen, nitrogen, hydrogen, argon, carbon dioxide gas, water vapor, etc. as reaction gases, or adopt reactive vapor deposition using means such as addition of ozone and ion assist.
• film formation conditions can be arbitrarily changed, such as applying a bias to the object to be vapor-deposited (laminate to be vapor-deposited), heating or cooling the object to be vapor-deposited.
• Such vapor deposition material, reaction gas, bias of the object to be vapor-deposited, heating/cooling, etc. can be similarly changed when adopting the sputtering method or the CVD method.
• the laminated film of the present invention preferably has a moisture content of 0.20% by mass or less. It is more preferably 0.18% by mass or less, still more preferably 0.15% by mass or less, and particularly preferably 0.12% by mass or less. A preferable lower limit is 0.01% by mass or more. If the water content is more than 0.20% by mass, a large amount of moisture penetrates during the wet heat treatment, and the inorganic thin film tends to crack, resulting in a decrease in gas barrier properties and adhesion. Moreover, the water content here is measured by a heat drying type moisture meter. The detailed measurement method is as described in the examples, but in short, the water content is calculated from the formula (moisture content [g] coming out of the sample) / (sample weight [g]) is.
• a protective layer may be provided on the inorganic thin film layer when further gas barrier performance is required or processing such as printing is required.
• the inorganic thin film layer is not a completely dense film, and is dotted with minute defects.
• the resin in the protective layer resin composition permeates into the defective portions of the inorganic thin film layer, resulting in An effect of stabilizing the gas barrier property is obtained.
• the gas barrier properties of the laminate are greatly improved.
• the provision of the protective layer causes an increase in cost due to an increase in the number of steps and an environmental burden depending on the materials used. It should also be noted that physical properties such as surface roughness change depending on the protective layer.
• a heat-sealing resin called a sealant is used in the laminate of the present invention.
• the heat-sealing resin layer is usually provided on the side of the anchor coat layer or the inorganic thin film layer, but may be provided on the outside of the resin film layer (the surface opposite to the inorganic thin film forming surface). Formation of the heat-sealable resin layer is usually carried out by an extrusion lamination method or a dry lamination method.
• the thermoplastic polymer forming the heat-sealable resin layer may be any polymer that can exhibit sufficient sealant adhesiveness, but polyethylene resins such as olefin-based HDPE, LDPE, and LLDPE, polypropylene resin, and ethylene-acetic acid.
• the thickness of the sealant layer is preferably 20-100 ⁇ m, more preferably 30-90 ⁇ m, more preferably 40-80 ⁇ m. If the thickness is less than 20 ⁇ m, sufficient sealing strength may not be obtained, and handling may be difficult due to lack of stiffness. On the other hand, if the thickness exceeds 100 ⁇ m, the bag will have a strong feeling of elasticity, and the handleability as a bag will deteriorate, and the price may become high.
• the thickness of the entire laminate of the present invention is preferably 9 ⁇ m or more and 200 ⁇ m or less, more preferably 10 ⁇ m or more and 170 ⁇ m or less, even more preferably 12 ⁇ m or more and 150 ⁇ m or less, and particularly preferably 15 ⁇ m or more and 120 ⁇ m or less.
• the haze of the laminate of the present invention is preferably 5% or less, more preferably 0.2% or more and 5.0% or less, further preferably 0.3% or more and 4.5% or less, and 0.4% or more. , 4.0% or less is particularly preferred.
• the laminate of the present invention preferably has an oxygen permeability of 25 cc/m 2 /d/atm or less under conditions of 23° C. and 65% RH. It is more preferably 20 cc/m 2 /d/atm or less, still more preferably 15 cc/m 2 /d/atm or less.
• a preferable lower limit of the oxygen permeability is 0.1 cc/m 2 /d/atm or more.
• the water vapor permeability under the conditions of 40° C. and 90% RH is 3.0 g/m 2 /d or less. It is more preferably 2.5 g/m 2 /d or less, more preferably 2.0 g/m 2 /d or less.
• a preferable lower limit of the water vapor permeability is 0.1 g/m 2 /d or more.
• the barrier value deterioration rate of the laminate of the present invention after wet heat treatment represented by formula (1) is 150% or less. It is more preferably 140% or less, still more preferably 130% or less.
• the laminate of the present invention preferably has a laminate strength of 2.0 N / 15 mm or more, more preferably 2.3 N, in both the dry and wet evaluations described later under the conditions of 23 ° C. and 65% RH. /15 mm or more, more preferably 2.6 N/15 mm or more. If the lamination strength is less than 2.0 N/15 mm, there is a risk that peeling will occur due to the load generated during the wet heat treatment, degrading the barrier properties, or causing the contents to leak out. Furthermore, there is also a possibility that the hand cutting property may deteriorate.
• a general-purpose laminating adhesive can be used.
• Non-)solvent type, water-based type, and hot-melt type adhesives containing a system, a wax system, a casein system, or the like as a main component can be used.
• urethane-based or polyester-based resins are preferable in consideration of heat resistance and flexibility that can follow dimensional changes of each resin.
• Examples of methods for laminating the adhesive layer include direct gravure coating, reverse gravure coating, kiss coating, die coating, roll coating, dip coating, knife coating, spray coating, fontaine coating, and others.
• the coating amount after drying is preferably 1 to 8 g/m 2 in order to exhibit sufficient adhesiveness. More preferably 2 to 7 g/m 2 , still more preferably 3 to 6 g/m 2 . If the coating amount is less than 1 g/m 2 , it becomes difficult to bond over the entire surface, resulting in a decrease in adhesive strength. On the other hand, if it exceeds 8 g/m 2 , it takes time to completely cure the film, unreacted substances tend to remain, and the adhesive strength decreases.
• At least one or more printed layers or other plastic resins and/or paper resins may be laminated between or outside the resin film layer and the heat-sealable resin layer.
• water-based and solvent-based resin-containing printing inks can be preferably used.
• resins used in printing inks include acrylic resins, urethane resins, polyester resins, vinyl chloride resins, vinyl acetate copolymer resins, and mixtures thereof.
• Antistatic agents, light shielding agents, ultraviolet absorbers, plasticizers, lubricants, fillers, colorants, stabilizers, lubricants, antifoaming agents, cross-linking agents, anti-blocking agents, antioxidants, and other known agents are used in printing inks. may contain additives.
• the printing method for forming the printed layer is not particularly limited, and known printing methods such as offset printing, gravure printing, and screen printing can be used.
• a known drying method such as hot air drying, hot roll drying, or infrared drying can be used.
• the present invention it is possible to obtain a laminated film that has excellent oxygen barrier properties and water vapor barrier properties after retort treatment, high interlayer adhesion, and excellent lamination strength.
• the evaluation methods used in the present invention are as follows. (1) Preparation of laminate On the inorganic thin film layer of the laminated film obtained in Examples and Comparative Examples, urethane-based two-liquid curing adhesive ("Takelac A525S” and “Takenate A50” manufactured by Mitsui Chemicals, Inc.) .5:1 ratio), and a 70 ⁇ m thick unstretched polypropylene film (manufactured by Toyobo Co., Ltd., P1146) as a thermal adhesive resin is laminated by a dry lamination method, and aged at 40 ° C. for 4 days. Laminates of Examples 1 to 4 and Comparative Examples 1 and 2 were obtained. The thickness of each adhesive layer was about 4 ⁇ m after drying.
• Thickness The thickness of each layer was measured by cutting out a cross section of a laminate of the present invention solidified with a modified urethane resin with a microtome and observing it with a differential interference microscope.
• each laminate obtained at the stage of laminating the anchor coat layer on the resin film was used as a sample, and a test piece of 100 mm ⁇ 100 mm was cut out from this sample. , the anchor coat layer was wiped off with acetone, and the adhesion amount was calculated from the change in mass of the film before and after wiping.
• each laminate obtained at the stage of laminating the inorganic thin film layer was used as a sample, and a fluorescent X-ray analyzer ("ZSX100e” manufactured by Rigaku Co., Ltd. ”) was used to measure the film thickness composition according to a calibration curve prepared in advance.
• the conditions for the excitation X-ray tube were 50 kV and 70 mA.
• Moisture content The moisture content of the laminate obtained in each example and comparative example was measured using a heat-drying moisture content meter (“MS-70” manufactured by A&D Co., Ltd.). .
• Laminate strength The laminate prepared in (1) above is cut into a width of 15 mm and a length of 200 mm to form a test piece.
• the lamination strength was measured using "Tensilon UMT-II-500 type" manufactured by the company.
• the lamination strength was measured at a tensile speed of 200 mm / min, and the laminate layer and the heat-sealable resin layer of each laminate obtained in Examples and Comparative Examples were peeled at a peel angle of 90 degrees. The strength was measured when water was dropped on the surface with a dropper (wet) and when water was not dropped (dry).
• the laminate prepared above was subjected to retort treatment for 30 minutes by holding it in pressurized hot water at a temperature of 130° C., and immediately after the obtained laminate laminate after retort treatment was treated in the same manner as described above. A test piece was cut out from the laminate, and the lamination strength (after retort treatment) was measured in the same manner as described above.
• Oxygen permeability In the laminate prepared in (1) above, an oxygen permeability measuring device ("OX-TRAN (registered trademark) 1/50" manufactured by MOCON) was used in accordance with JIS-K7126 B method. , a temperature of 23° C. and a humidity of 65% RH. The oxygen permeability was measured in the direction in which oxygen permeates from the surface layer (C) side.
• the laminate for evaluation was subjected to retort treatment in which it was held in pressurized hot water at a temperature of 130° C. for 30 minutes, and then dried at 40° C. for 24 hours. The oxygen permeability (after retort treatment) was measured in the same manner as above.
• Laminate strength deterioration rate A value represented by the following formula (2) was taken as the laminate strength deterioration rate for the value measured in (6) above.
• Laminate strength deterioration rate (%) (laminate strength before retort treatment - laminate strength after retort treatment) / (laminate strength before retort treatment) x 100 Formula (2)
• Tables 1 to 3 show the details of the resin raw materials used in the preparation of the base film below, the film forming conditions, and the raw material mixing ratios.
• the surface layer (B) contains 43.2% by weight of the polypropylene homopolymer PP-2 shown in Table 1, 52.0% by weight of the ethylene copolymerized polypropylene polymer PP-4 shown in Table 1, and antiblocking.
• a mixture containing 4.8% by weight of the agent-containing masterbatch FTX0627G was used.
• the melt flow rate (g/10 minutes) of the polypropylene-based resin composition constituting the surface layer (B) was 5.1.
• the surface layer (C) 93.6% by weight of the polypropylene homopolymer PP-2 shown in Table 1 and 6.4% by weight of the antiblocking agent-containing masterbatch FTX0627G were blended.
• the raw material resin is melted at 250 ° C., and a sheet is formed from a T die. It was co-extruded, cooled and solidified so that the surface layer (B) was in contact with a cooling roll at 30°C, and then stretched 4.5 times in the machine direction (MD) at 125°C.
• both ends of the film in the width direction (TD) are clipped, preheated at 168 ° C., stretched at 155 ° C. in the width direction (TD) 8.2 times, and 6.7% in the width direction (TD).
• the film forming conditions at this time were defined as film forming conditions a.
• a biaxially oriented polypropylene film having a structure of surface layer (B)/base layer (A)/surface layer (C) was obtained.
• the surface of the surface layer (B) of the biaxially oriented polypropylene film was subjected to corona treatment using a corona treatment machine manufactured by Softal Corona & Plasma GmbH under conditions of an applied current value of 0.75 A.
• the thickness of the obtained film was 20 ⁇ m (thickness of surface layer (B)/base layer (A)/surface layer (C) was 1.3 ⁇ m/17.7 ⁇ m/1.0 ⁇ m).
• the polypropylene homopolymer PP-1 shown in Table 1 was used for the base layer (A). Further, the surface layer (B) contains 43.2% by weight of the polypropylene homopolymer PP-2 shown in Table 1, 52.0% by weight of the ethylene copolymerized polypropylene polymer PP-4 shown in Table 1, and antiblocking. A mixture containing 4.8% by weight of the agent-containing masterbatch FTX0627G was used. For the surface layer (C), 93.6% by weight of the polypropylene homopolymer PP-1 shown in Table 1 and 6.4% by weight of the antiblocking agent-containing masterbatch FTX0627G were blended.
• the raw material resin is melted at 250 ° C., and a sheet is formed from a T die. It was co-extruded, cooled and solidified so that the surface layer (B) was in contact with a cooling roll at 30°C, and then stretched 4.5 times in the machine direction (MD) at 135°C. Then, in a tenter, both ends of the film in the width direction (TD) are clipped, preheated at 173 ° C., stretched at 164 ° C.
• a biaxially oriented polypropylene film having a structure of surface layer (B)/base layer (A)/surface layer (C) was obtained.
• the surface of the surface layer (B) of the biaxially oriented polypropylene film was subjected to corona treatment using a corona treatment machine manufactured by Softal Corona & Plasma GmbH under conditions of an applied current value of 0.75 A. After that, it was wound with a winder.
• the thickness of the resulting film was 20 ⁇ m (thickness of surface layer (B)/base layer (A)/surface layer (C) was 1.3 ⁇ m/17.7 ⁇ m/1.0 ⁇ m).
• PET Polyethylene glycol dimethacrylate copolymer
• Toyobo Co., Ltd. and having a thickness of 12 ⁇ m was used.
• the resulting prepared solution was diluted with 69.55 parts by mass of methyl ethyl ketone and 14.03 parts by mass of 1-methoxy-2-propanol (hereinafter PGM), and further polyester resin (manufactured by DIC; DF-COAT GEC-004C: solid content 30%) was added in an amount of 10.62 parts by mass to obtain the desired coating liquid 1.
• PGM 1-methoxy-2-propanol
• the method for producing the inorganic thin film layer used in each example and comparative example is described below.
• a composite oxide layer of silicon dioxide and aluminum oxide was formed on the anchor coat layer by electron beam evaporation.
• As a vapor deposition source particulate SiO 2 (purity 99.9%) and Al 2 O 3 (purity 99.9%) of about 3 mm to 5 mm were used.
• the film thickness of the inorganic thin film layer (SiO 2 /Al 2 O 3 composite oxide layer) in the film (inorganic thin film layer/anchor coat layer-containing film) thus obtained was 13 nm.
• Example 1 OPP-1 was used for the substrate film, and Coating Solution 1 was used for the anchor coat layer, which were applied onto the surface layer (B) of the resin film by a gravure roll coating method and dried at 130° C. for 10 seconds. The adhesion amount of the anchor coat layer at this time was 0.40 g/m 2 . Then, after performing a post-heating treatment at 40° C. for 2 days, an inorganic thin film layer was laminated by the method described above to obtain the target laminated film. (Example 2) A desired laminate film was obtained under the same conditions as in Example 1, except that the resin film was changed to OPP-2.
• Example 3 A desired laminated film was obtained under the same conditions as in Example 1, except that the amount of the anchor coat layer deposited was changed to 0.20 g/m 2 .
• Example 5 A desired laminate film was obtained under the same conditions as in Example 1, except that Coating Solution 2 was used for the anchor coat layer.
• Comparative example 1 A desired laminated film was obtained under the same conditions as in Example 1, except that Coating Solution 3 was used for the anchor coat layer.
• Comparative example 2 A desired laminate film was obtained under the same conditions as in Example 1, except that the base film was changed to PET.
• a laminated film was produced as described above. Further, a laminate was produced from the obtained laminate film as shown in (1) above, and the structure and various evaluations were performed on the laminate film and the laminate, and the results are shown in Table 4.
• the present invention it has become possible to provide a laminated film that has excellent oxygen and water vapor barrier properties even after retorting, and has adhesion that does not cause delamination after retorting.

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• 2021
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