WO2009123200A1 - ガスバリア性フィルムおよびその製造方法 - Google Patents
ガスバリア性フィルムおよびその製造方法 Download PDFInfo
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- WO2009123200A1 WO2009123200A1 PCT/JP2009/056685 JP2009056685W WO2009123200A1 WO 2009123200 A1 WO2009123200 A1 WO 2009123200A1 JP 2009056685 W JP2009056685 W JP 2009056685W WO 2009123200 A1 WO2009123200 A1 WO 2009123200A1
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- gas barrier
- barrier film
- film
- layered silicate
- inorganic layered
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/34—Silicon-containing compounds
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
- C08J7/04—Coating
- C08J7/0427—Coating with only one layer of a composition containing a polymer binder
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
- C08J7/04—Coating
- C08J7/043—Improving the adhesiveness of the coatings per se, e.g. forming primers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
- C08J7/04—Coating
- C08J7/048—Forming gas barrier coatings
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2329/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal, or ketal radical; Hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Derivatives of such polymer
- C08J2329/02—Homopolymers or copolymers of unsaturated alcohols
- C08J2329/04—Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2429/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal, or ketal radical; Hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Derivatives of such polymer
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K2201/00—Specific properties of additives
- C08K2201/008—Additives improving gas barrier properties
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/24—Structurally defined web or sheet [e.g., overall dimension, etc.]
- Y10T428/24628—Nonplanar uniform thickness material
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/25—Web or sheet containing structurally defined element or component and including a second component containing structurally defined particles
- Y10T428/259—Silicic material
Definitions
- the present invention relates to a gas barrier film including a resin composition layer having a high gas barrier function, and a method for producing the barrier film.
- the surface of the resin composition layer in which the swellable layered inorganic silicate is dispersed is likely to have irregularities, and hence the problem of poor appearance, poor printability, or poor adhesion when laminating with other films, etc. It is easy to produce.
- a technique for reducing irregularities on the surface of the resin composition layer by devising a dispersion method and processing conditions of the swellable layered inorganic silicate in the resin has been proposed (for example, Patent Documents). 3).
- Patent Documents 3
- the present invention has been made to solve the above-described problems, and includes a multilayer barrier film including a resin composition layer in which a swellable layered inorganic silicate having extremely excellent gas barrier properties is dispersed, and the resin composition layer
- An object of the present invention is to provide a method for producing a multilayer barrier film having very few surface irregularities.
- the gas barrier film of the present invention that solves the above-mentioned problems is a swellability that satisfies the following formulas (1) and (2) on at least one side of the substrate (D): water-soluble or water-dispersible polymer (A) It has the layer which consists of a resin composition (C) containing an inorganic layered silicate (B), It is characterized by the above-mentioned. 11.0 ⁇ D ⁇ 2.0 ⁇ m (1) ⁇ ⁇ 1.8 ⁇ m (2)
- D and ⁇ are the logarithm average particle size of the swellable inorganic layered silicate (B) measured by the laser diffraction method and the standard deviation of the particle size distribution.
- the compounding ratio of the swellable inorganic layered silicate in the resin composition (C) is preferably 0.5 to 55% by weight.
- the water-soluble or water-dispersible polymer (A) is preferably a polyvinyl alcohol polymer.
- the polyvinyl alcohol polymer is more preferably an ethylene-vinyl alcohol polymer.
- the swellable inorganic layered silicate (B) is preferably a synthetic inorganic layered silicate.
- the swellable inorganic layered silicate (B) is preferably a synthetic smectite.
- the substrate (D) is preferably a film made of at least one polymer selected from the group consisting of a polyamide polymer, a polyester polymer, and a polyvinyl alcohol polymer.
- the substrate (D) is preferably a film made of an ethylene-vinyl alcohol polymer.
- the number of undulations in the range of 25 to 100 ⁇ m in diameter on the layer surface made of the resin composition (C) is less than 1 per 1 mm 2 .
- a solution or water dispersion containing a water-soluble or water-dispersible polymer (A) and a swellable inorganic layered silicate (B) The production method is characterized in that the liquid is applied onto the substrate (D) with a coating facility, smoothed with a smoothing roll, and then dried.
- the smoothing roll preferably has a diameter of 3 mm or more.
- the smoothing roll is preferably a smooth roll in which the number of wires wound around the smoothing roll is No. 75 or less, or no wire is wound.
- the film tension of the smoothing roll portion is preferably 1.0 to 15 Kg / cm.
- the linear velocity to the rotation direction of the smoothing roll surface and the line velocity of a film exist in the range of the following formula
- Vs is the linear velocity in the rotation direction of the smoothing roll surface
- Vf is the line velocity of the film.
- a packaging material obtained by laminating the gas barrier film with another material is also a preferred embodiment of the present invention.
- the present invention provides a gas barrier film including a resin composition layer in which a swellable layered inorganic silicate having extremely excellent gas barrier properties is dispersed, and a method for producing a multilayer barrier film having very few irregularities on the surface of the barrier film. Things will be possible.
- the swellable inorganic layered silicate (B) satisfies the following formulas (1) and (2).
- D and ⁇ are the logarithm average particle diameter of the swellable inorganic layered silicate (B) measured by the laser diffraction method and the standard deviation of the particle size distribution.
- a more preferable range of D is 2.4 ⁇ m to 10 ⁇ m, more preferably 2.8 ⁇ m to 9 ⁇ m, and most preferably 3.2 ⁇ m to 8 ⁇ m.
- a more preferable range of ⁇ is 1.9 ⁇ m or more, more preferably 2.0 ⁇ m or more, and most preferably 2.1 ⁇ m or more.
- the reason why the swellable inorganic layered silicate having a logarithmic average particle size of less than 2.0 ⁇ m does not exhibit sufficient barrier properties is presumed as follows.
- the unit cell in the thickness direction of the swellable inorganic layered silicate crystal is about 1 nm and does not become thinner beyond that.
- the aspect ratio of the particles decreases.
- the aspect ratio of the swellable inorganic layered silicate having a logarithmic average particle size exceeding 11.0 ⁇ m is large, if the particles are too large, the resin composition layer may be broken through and the barrier property will be reduced. It is difficult to orient the swellable inorganic layered silicate with the current film forming technology. The reason is that the resin composition layer in the present invention is formed by applying it on a substrate in the form of a water suspension and then drying it. For this reason, the orientation of the swellable inorganic layered silicate is disturbed when water molecules are vaporized during drying. This is presumed to be the reason why sufficient gas barrier properties are not exhibited in the swellable inorganic layered silicate having a logarithmic average particle size exceeding 11.0 ⁇ m.
- the reason why the standard deviation ⁇ of the particle size distribution is 1.8 ⁇ m or more is that a gas barrier film containing a swellable inorganic layered silicate having the same average particle diameter has a higher standard deviation and a higher gas barrier property is obtained.
- powders with more variation can be packed more densely, the orientation of the swellable inorganic layered silicate is less disturbed during drying, and locally between large swellable inorganic layered silicate particles. This is presumably because the small swellable inorganic layered silicate particles cover the wide gaps that occur.
- the standard deviation ⁇ of the particle size distribution is preferably 11 ⁇ m or less, more preferably 8 ⁇ m or less, and even more preferably 5 ⁇ m or less.
- the basic principle of laser particle size analysis is described below.
- a diffraction phenomenon occurs along the contour of the particles.
- this diffracted light is collected by a lens, a ring of light (diffraction ring) is obtained on the focal plane, and the particle size is determined by the diameter of the ring and the intensity of the light.
- This principle is called Fraunhofer's principle of light diffraction and is the basic principle of laser particle size analysis. Analysis by this diffraction phenomenon can be applied up to a particle diameter several times the wavelength, but 1 ⁇ m is the lower limit. For particle diameters of 1 ⁇ m or less, Mie's light scattering theory is applied, and the size of particles in the submicron range is determined by detecting forward scattered light, back scattered light, and side scattered light.
- the logarithm average particle diameter and the standard deviation of the particle size distribution were measured with a laser diffractometer LMS-30 manufactured by Seishin Enterprise Co., Ltd.
- the logarithmic average particle diameter is an “X50” value calculated by the laser diffractometer.
- the device detects the diffraction ring of laser light with a photodiode array. For forward scattered light, back scattered light, and side scattered light, three forward scattered light, two back scattered light, and one side scattered light detection sensor provided separately from the diffracted light receiving detector. Detect with.
- the mixing ratio of the swellable inorganic layered silicate (B) to the water-soluble or water-dispersible polymer (A) in the resin composition (C) is not particularly limited.
- the amount of the swellable inorganic layered silicate (B) added to the water-soluble or water-dispersible polymer (A) is preferably 0.5 to 55% by weight. When the addition amount is less than 0.5% by weight, sufficient barrier properties cannot be obtained, and when it exceeds 55% by weight, the flexibility of the resin composition (C) is lowered and defects such as cracks are likely to occur.
- a more preferable amount of the swellable inorganic layered silicate (B) is 1 to 40% by weight, more preferably 3 to 30% by weight, and most preferably 5 to 20% by weight.
- the water-soluble or water-dispersible polymer (A) used in the present invention refers to a polymer that can be completely dissolved or finely dispersed in a solvent containing water as a main component at room temperature, and is not necessarily limited.
- a polyvinyl alcohol polymer hereinafter sometimes abbreviated as PVA
- a typical vinyl ester used in the production of the PVA resin is vinyl acetate, but other fatty acid vinyl esters (such as vinyl propionate and vinyl pivalate) can also be used.
- ⁇ - such as ethylene, propylene, butylene, isobutene, 4-methyl-1-pentene, 1-hexene, 1-octene, etc.
- the degree of saponification of the vinyl ester component of PVA used in the present invention is not particularly limited, but is preferably 60 mol% or more.
- the saponification degree of the vinyl ester component is more preferably 70 mol% or more, further preferably 80 mol% or more, and optimally 90 mol% or more. If the saponification degree is less than 60%, the barrier property may be insufficient.
- the barrier property under high humidity conditions can be improved, which is more preferable.
- the ethylene content of the EVOH resin is not particularly limited, but is preferably 1 to 50 mol%. When ethylene content exceeds 50 mol%, there exists a possibility that the barrier property of the resin composition (C) obtained may become inadequate.
- the upper limit of the ethylene content is more preferably 20 mol% or less because when the ethylene content exceeds 20 mol%, it is essential to add alcohols to water as a solvent to obtain a solution. . More preferably, it is 17 mol% or less, Most preferably, it is 14 mol% or less.
- the high humidity barrier property of the resin composition (C) may be insufficient.
- the lower limit of the ethylene content of EVOH is more preferably 2 mol% or more, further preferably 3 mol% or more, and most preferably 4 mol% or more.
- EVOH consists of 2 or more types of EVOH from which ethylene content differs, let the average value calculated from a mixing
- the saponification degree of the PVA resin and the ethylene content of EVOH can be determined by a nuclear magnetic resonance (NMR) method.
- the swellable inorganic layered silicate (B) is preferably a synthetic inorganic layered silicate, and more preferably a synthetic smectite.
- synthetic smectite Na type hectorite, Li type hectorite, etc.
- These can be obtained by a conventionally known internal heat melting method.
- SiO 2 , MgO, Al 2 O 3 , Na 2 CO 3 , Li 2 CO 3 and / or fluorides (NaF, LiF, MgF 2 , Na 2 SiF 6 , Li 2 SiF 6, etc.) are aimed. What is necessary is just to mix and mix according to chemical composition and to melt. Natural minerals such as feldspar, olivine and talc may be used as the Si, Al and Mg sources.
- the obtained synthetic smectite has its average particle size and standard deviation adjusted by a method such as grinding with a ball mill or the like, or centrifugal classification.
- the water dispersion of (B) may be used as a method of mixing the water-soluble or water-dispersible polymer (A) and the swellable inorganic layered silicate (B).
- An appropriate dispersant can be freely added to the dispersion unless the effects of the invention are impaired.
- additives such as surfactants, thickeners, water-soluble polymers, preservatives and the like can be used as necessary as long as the effects of the invention are not impaired.
- the resin composition (C) includes a plasticizer, an antioxidant, a pigment, an ultraviolet absorber, an antistatic agent, a crosslinking agent, a filler, reinforcing agents such as various fibers, It is also possible to add an appropriate amount of etc.
- the resin composition (C) in the present invention can be used alone, but the resin composition (C) exhibits a sufficient barrier property even in a thin layer of 5 ⁇ m or less, and in a thin layer of 5 ⁇ m or less. Since sufficient mechanical strength cannot be obtained, it is preferable to use it laminated with another substrate (D) for use as a barrier packaging material.
- the substrate (D) is not particularly limited, such as paper, metal, cloth, and plastic, but plastic is suitable as the packaging material.
- the polyamide polymer, the polyester polymer, and the polyvinyl alcohol polymer are the polymers themselves. Since it has a good gas barrier property, a film having a high gas barrier property can be obtained by combining with the resin composition (C). Therefore, a film made of at least one polymer selected from the group consisting of these polymers It is preferable that Further, among these polymers, an ethylene-vinyl alcohol polymer which is a polyvinyl alcohol polymer has the highest barrier property and is optimal.
- the thickness of the resin composition (C) when laminated with the substrate (D) is not particularly limited, but is preferably 0.01 to 50 ⁇ m. If it is less than 0.01 ⁇ m, sufficient gas barrier properties may not be obtained, and if it exceeds 50 ⁇ m, the uniformity in the resin composition (C) layer is deteriorated. From this viewpoint, the lower limit of the thickness of the resin composition (C) is more preferably 0.05 ⁇ m or more, further preferably 0.1 ⁇ m or more, and most preferably 0.3 ⁇ m or more. More preferably, it is 30 ⁇ m or less, more preferably 20 ⁇ m or less, and most preferably 10 ⁇ m or less.
- Examples of the method of laminating the resin composition (C) and the substrate (D) include coextrusion molding, extrusion coating, solution or aqueous dispersion coating, and the like, but the water-soluble or water-dispersible polymer (A) And a coating of a solution or an aqueous dispersion containing the swellable inorganic layered silicate (B) are preferable from the viewpoint of workability and laminated film performance.
- Examples of the coating equipment include gravure coating, reverse coating, spray coating, kiss coating, comma coating, die coating, knife coating, air knife coating, and metering bar coating.
- the method for adjusting the coating liquid when coating the solution or water-dispersed liquid is such that the water-dispersible polymer (A) is swellable inorganic layered.
- the method of preparing an aqueous dispersion of the swellable inorganic layered silicate (B) and mixing it with the aqueous dispersion of (A) is a dispersion state of the swellable inorganic layered silicate (B). Is more suitable because it is easy to control.
- water-soluble or water-dispersible polymer (A) is a water-soluble polymer
- (A) and (B) are simultaneously added to a solvent, and then heated and stirred to dissolve (A) and (B)
- a method of simultaneously dispersing, a method of adjusting the solution of (A) and then adding and stirring (B) to disperse (B), adjusting the aqueous dispersion of (B) and adding (A) examples thereof include a method of dissolving (A) by heating and stirring, a method of mixing the solution of (A) and the aqueous dispersion of (B) separately, and the like.
- the method of mixing after separately adjusting the solution of (A) and the aqueous dispersion of (B) is more preferable because the dispersion state of the swellable inorganic layered silicate (B) can be easily controlled. .
- the coating liquid may contain a plasticizer, an antioxidant, a pigment, an ultraviolet absorber, an antistatic agent, a crosslinking agent, a filler, various fibers, etc., as long as the object of the present invention is not impaired. It is also possible to add an appropriate amount of a reinforcing agent or the like. In addition, an additive such as alcohol may be added in order to improve the stability of the coating liquid and the leveling property at the time of application as long as the object of the present invention is not impaired.
- a vapor deposition layer (E) made of a metal and / or a metal oxide on at least one surface of the resin composition (C) layer and / or the substrate (D).
- the vapor deposition layer (E) made of metal and / or metal oxide has a good barrier property without depending on the humidity condition, but has a defect that the barrier property is easily lowered due to deformation or the like, and the barrier property is lowered.
- the resin composition (C) has a high resistance to deformation and the like, although the barrier property does not reach the vapor deposition layer (E), and by combining the two, each drawback can be compensated.
- the vapor deposition layer (E) made of metal and / or metal oxide in the present invention is not particularly limited as a metal, but is preferably stable in the air, such as aluminum whose film surface is oxidized and stabilized after formation of a thin film.
- a metal preferably aluminum whose film surface is oxidized and stabilized after formation of a thin film.
- metal oxide aluminum oxide, silicon oxide, titanium oxide, zinc oxide and the like are preferable, and their oxidation states may be various.
- the thickness of the vapor deposition layer (E) is preferably 1 to 2000 nm. More preferably, it is 10 to 1500 nm, and more preferably 50 to 1000 nm.
- a method for forming the vapor deposition layer (E) is not particularly limited, and a CVD method, a sputtering method, a sol-gel method, or the like is used in addition to a general vacuum vapor deposition method.
- the resin composition (C) layer and the vapor deposition layer (E) each have 1
- the composition of (C) / (E) / (D), in which the vapor deposition layer (E) is provided on the substrate (D) and the resin composition (C) layer is coated thereon is the resin composition.
- the (C) layer is preferable because it can function as a protective layer for the vapor deposition layer (E).
- the number of undulations in the range of 25 to 100 ⁇ m in diameter on the surface of the layer made of the resin composition (C) is less than 1 per 1 mm 2 .
- the number of undulations corresponds to the number of irregularities on the surface. If there are many irregularities on the surface, the surface of the (1) resin composition (C) layer becomes rough and the appearance is poor.
- the resin composition (C ) When printing on the surface of the layer, problems such as ink bleeding at the uneven portions are likely to occur.
- the surface of the resin composition (C) layer And the adhesive layer are poorly adhered, and problems such as a case where sufficient adhesive force may not be obtained are likely to occur.
- the number of swells in the present invention is defined as follows. A low magnification (about 5 times) film surface image obtained by an optical microscope or the like is subjected to image processing using an image analyzer or the like. At this time, image processing is performed so that peaks and valleys existing on the film surface are projected as an image. Each image observed in the image is replaced with an equivalent circle, the number of those whose diameter is in the range of 25 to 100 ⁇ m is counted, and the value converted per 1 mm 2 is defined as the number of waviness.
- a water-soluble or water-dispersible polymer (A) and a swellable inorganic layered form A production method characterized in that a solution containing silicate (B) or an aqueous dispersion is coated on a substrate (D) with a coating facility, smoothed with a smoothing roll, and then dried.
- the coating liquid coated on the substrate (D) has many irregularities on the surface.
- the unevenness is gradually alleviated by the leveling effect of the coating liquid.
- the number of undulations cannot be less than 1 per 1 mm 2 . Therefore, it is possible to reduce the number of undulations to less than 1 per 1 mm 2 by leveling the unevenness of the coating film surface coated on the substrate (D) with a smoothing roll and then putting it into a drying facility. .
- the diameter of the smoothing roll is preferably 3 mm or more. If the thickness is less than 3 mm, it becomes difficult to press the film uniformly against the film due to insufficient rigidity of the smoothing roll. There is a possibility of waking up. From this viewpoint, the diameter of the smoothing roll is more preferably 5 mm or more, further preferably 10 mm or more, and most preferably 15 mm or more. Although depending on the rotational speed of the smoothing roll, if the diameter is too large, the coating liquid may be dried and deposited on the smoothing roll.
- a wire is wound around the surface of the smoothing roll.
- the method for producing the coated film is not necessarily limited, but the wire should be 75 or less or a smooth roll that does not wind the wire.
- the 75th wire means that the winding has a diameter of 75/1000 inches (about 1.9 mm).
- the wire count is more preferably No. 50 or less, more preferably No. 25 or less, and most preferably a smooth roll not wound with a wire.
- the film tension of the smoothing roll portion is 1.0 to 15 kg / cm.
- the film tension of the smoothing roll portion is more preferably 2.0 to 10 kg / cm, and further preferably 3.0 to 8.0 kg / cm.
- the smoothing roll rotates in the opposite direction or the same direction as the flow direction of the substrate in order to uniformly apply the scraped coating liquid to the substrate again.
- the method for producing a coated film of the present invention is not necessarily limited, but the linear velocity on the surface of the smoothing roll and the line velocity of the film are preferably in the range of the following formula (3).
- Vs is the linear velocity of the smoothing roll surface
- Vf is the line velocity of the film.
- the upper limit of Vs / Vf is more preferably 0.1, more preferably 0.05, and the lower limit is more preferably ⁇ 0.5, and still more preferably ⁇ 0.3. is there.
- the drying method of the coated film is not particularly limited, and a hot roll contact method, a heating medium (air, oil, etc.) contact method, an infrared heating method, a microwave heating method, and the like can be used.
- Typical drying conditions for the coating are a drying temperature of 60 to 250 ° C. and a drying time of 1 to 60 seconds. However, depending on the thermal efficiency of the drying equipment, it is necessary to select conditions suitable for the apparatus. .
- a packaging material obtained by laminating the gas barrier film obtained by laminating the resin composition (C) on the base material (D) with at least one layer and other materials is also a preferred embodiment of the present invention.
- the structure of the packaging material can be freely selected as necessary, but a typical example is that a heat-bonding sealant layer is provided on the outermost layer and combined with a polypropylene film or a polyester film depending on other purposes of use.
- a lamination method a known method can be adopted, and dry lamination is generally used, but other methods such as extrusion coating, solution coating, and emulsion coating can be used.
- the gas barrier film of the present invention thus obtained has gas barrier properties superior to those of conventional gas barrier films.
- Example 1 33.75 g of EXCEVAL 3110 manufactured by Kuraray Co., Ltd., which is a polyethylene-vinyl alcohol polymer obtained by saponification of a polyethylene-vinyl acetate polymer, was added to 326. 5 g was stirred for 1 hour while heating to 90 ° C. to obtain an aqueous solution. After the aqueous solution was cooled to room temperature, 64.75 g of a 50% aqueous isopropyl alcohol solution was added to improve the stability of the solution.
- NHT-sol B2 (a synthetic hectorite aqueous dispersion, solid content concentration 5%, average particle size 3.8 ⁇ m, standard deviation 2.2 ⁇ m) was added to this solution to swell EVOH.
- the solid content concentration in the liquid was 7.5%, and the compounding ratio of the swellable inorganic layered silicate in the solid content was 10%.
- Eval EF-XL # 15 thickness 15 ⁇ m
- the thickness of the dried coat layer was 1.5 ⁇ m.
- the coated film obtained as described above was used to evaluate oxygen permeability.
- a part of the sample film was cut out and left in a desiccator adjusted to 20 ° C.-85% RH for one week to adjust the humidity, and then the oxygen permeation measuring device (OX-TRAN-2 / 20, manufactured by Modern Control Co., Ltd.)
- the oxygen transmission rate was calculated by measuring the oxygen transmission rate of 20 ° C.-85% RH.
- the oxygen permeability was 0.9 ml / m 2 ⁇ day ⁇ atm.
- metal aluminum was vapor-deposited on the coating layer surface of the obtained coating film, and the reflected light image (magnification: 5 times) of the film surface was obtained with the optical microscope (Olympus Optical Co., Ltd. BX60).
- the image is taken into an image analyzer and subjected to automatic binarization (P tile method, 10%), and each image observed in the processed image is replaced with an equivalent circle, and the diameter is 25.
- the number of those in the range of ⁇ 100 ⁇ m was measured. This measurement was performed 20 times at different locations, the average value was calculated, and the numerical value converted per mm 2 was taken as the number of undulations. As a result, the number of waviness of the present coated film was 0.6 / mm 2 .
- Example 2 9.6 g of Takelac A-385 and 0.8 g of Takenate A-50, which are adhesives manufactured by Mitsui Takeda Chemical Co., Ltd., were mixed and diluted with 70 g of ethyl acetate to prepare an adhesive solution.
- This adhesive solution is uniformly hand-coated on a 12 ⁇ m film of Lumirror P60, which is a biaxially stretched polyester film manufactured by Toray Industries, Inc., using a No. 8 bar coater, and heated at 60 ° C. for 3 minutes with a hot air dryer Dried.
- the thickness of the adhesive layer after drying was 0.3 ⁇ m.
- Example 1 On this adhesive layer, 500 g of a liquid containing EVOH and the swellable inorganic layered silicate used in Example 1 was coated in the same manner as in Example 1, and oxygen permeability was measured. The result was 2.1 ml / m 2 ⁇ day ⁇ atm. The number of undulations measured in the same manner as in Example 1 was 0.5 / mm 2 .
- Example 3 PVA and swelling were carried out in the same manner as in Example 2 except that PVA-110H (saponification degree: 98 mol% or more), a Kuraray polyvinyl alcohol resin, was used as the water-soluble or water-dispersible polymer (A).
- a film coated with a composition of a porous inorganic layered silicate was prepared. The oxygen permeability of this film was measured in the same manner as in Example 1. As a result, it was 4.1 ml / m 2 ⁇ day ⁇ atm. Moreover, the result of measuring the number of undulations in the same manner as in Example 1 was 0.6 / mm 2 .
- Example 4 As the swellable inorganic layered silicate (B), NHT-sol B5 manufactured by Topy Industries Co., Ltd. (aqueous dispersion of synthetic hectorite, solid content concentration 5%, average particle size 5.2 ⁇ m, standard deviation 2.3 ⁇ m) is used. A film coated with a composition of PVA and a swellable inorganic layered silicate was prepared in the same manner as in Example 3 except that. The oxygen permeability of this film was measured in the same manner as in Example 1. As a result, it was 3.1 ml / m 2 ⁇ day ⁇ atm. Moreover, the result of measuring the number of undulations in the same manner as in Example 1 was 0.7 / mm 2 .
- Example 5 As the swellable inorganic layered silicate (B), NHT-sol B7 manufactured by Topy Industries Co., Ltd. (aqueous dispersion of synthetic hectorite, solid content concentration 5%, average particle size 7.1 ⁇ m, standard deviation 2.4 ⁇ m) is used. A film coated with a composition of PVA and a swellable inorganic layered silicate was prepared in the same manner as in Example 3 except that. The oxygen permeability of this film was measured in the same manner as in Example 1. As a result, it was 4.2 ml / m 2 ⁇ day ⁇ atm. The number of undulations measured in the same manner as in Example 1 was 0.8 / mm 2 .
- Example 6 As a swellable inorganic layered silicate (B), NTS-sol C manufactured by Topy Industries, Ltd. (aqueous dispersion of synthetic sodium tetrasilicon mica, solid content concentration 5%, average particle size 2.8 ⁇ m, standard deviation 2.1 ⁇ m) A film coated with a composition of PVA and a swellable inorganic layered silicate was prepared in the same manner as in Example 3 except that was used. The oxygen permeability of this film was measured in the same manner as in Example 1. As a result, it was 9.7 ml / m 2 ⁇ day ⁇ atm. The number of undulations measured in the same manner as in Example 1 was 0.5 / mm 2 .
- Example 3 A film coated with PVA was prepared in the same manner as in Example 3 except that the aqueous dispersion of the swellable inorganic layered silicate (B) was not added. The oxygen permeability of this film was measured in the same manner as in Example 1. As a result, it was 53 ml / m 2 ⁇ day ⁇ atm.
- Example 7 As the swellable inorganic layered silicate (B), NHT-sol B10 manufactured by Topy Industries, Ltd. (aqueous dispersion of synthetic hectorite, solid content concentration 5%, average particle size 10.4 ⁇ m, standard deviation 2.4 ⁇ m) is used. A film coated with PVA was prepared in the same manner as in Example 3 except that. The oxygen permeability of this film was measured in the same manner as in Example 1. As a result, it was 15 ml / m 2 ⁇ day ⁇ atm. Moreover, the result of measuring the number of undulations in the same manner as in Example 1 was 0.9 / mm 2 .
- Example 4 As a swellable inorganic layered silicate (B), NTS-5 manufactured by Topy Industries Co., Ltd. (aqueous dispersion of synthetic sodium tetrasilicon mica, solid content concentration 6%, average particle size 11.5 ⁇ m, standard deviation 2.4 ⁇ m) A film coated with PVA was produced in the same manner as in Example 3 except that it was used. The oxygen permeability of this film was measured in the same manner as in Example 1. As a result, it was 21 ml / m 2 ⁇ day ⁇ atm.
- Example 5 As a swellable inorganic layered silicate (B), NTS-10 manufactured by Topy Industries Co., Ltd. (aqueous dispersion of synthetic sodium tetrasilicon mica, solid content concentration 10%, average particle size 14.0 ⁇ m, standard deviation 2.5 ⁇ m) A film coated with PVA was produced in the same manner as in Example 3 except that it was used. The oxygen permeability of this film was measured in the same manner as in Example 1. As a result, it was 29 ml / m 2 ⁇ day ⁇ atm.
- Example 6 As the swellable inorganic layered silicate (B), NHT-sol 1 manufactured by Topy Industries, Ltd. (aqueous dispersion of synthetic hectorite, solid content concentration 5%, average particle size 1.1 ⁇ m, standard deviation 2.1 ⁇ m) is used. A film coated with PVA was prepared in the same manner as in Example 3 except that. The oxygen permeability of this film was measured in the same manner as in Example 1. As a result, it was 33 ml / m 2 ⁇ day ⁇ atm.
- Example 7 As the swellable inorganic layered silicate (B), NHT-sol 2 (synthetic hectorite aqueous dispersion, solid content concentration 5%, average particle size 2.2 ⁇ m, standard deviation 1.6 ⁇ m) used by Topy Industries, Ltd. A film coated with PVA was prepared in the same manner as in Example 3 except that. The oxygen permeability of this film was measured in the same manner as in Example 1. As a result, it was 30 ml / m 2 ⁇ day ⁇ atm.
- NHT-sol 2 synthetic hectorite aqueous dispersion, solid content concentration 5%, average particle size 2.2 ⁇ m, standard deviation 1.6 ⁇ m
- Example 8 As the swellable inorganic layered silicate (B), NHT-sol B1 manufactured by Topy Industries, Ltd. (aqueous dispersion of synthetic hectorite, solid content concentration 5%, average particle size 1.1 ⁇ m, standard deviation 1.6 ⁇ m) is used. A film coated with PVA was prepared in the same manner as in Example 3 except that. The oxygen permeability of this film was measured in the same manner as in Example 1. As a result, it was 38 ml / m 2 ⁇ day ⁇ atm.
- Example 11 Same as Example 1 except that the amount of EXCEVAL3110 manufactured by Kuraray Co., Ltd. was changed to 37.39 g, the amount of ion exchange water was changed to 395.61 g, and the amount of NHT-sol B2 manufactured by Topy Industries, Ltd. was changed to 2.25 g. Thus, 500 g of a liquid containing EVOH and a swellable inorganic layered silicate was obtained. The mixing ratio of the swellable inorganic layered silicate in the solid content in the liquid was 0.3%. Using this solution, a film coated with a composition of PVA and a swellable inorganic layered silicate was prepared in the same manner as in Example 1. The oxygen permeability of this film was measured in the same manner as in Example 1. As a result, it was 42 ml / m 2 ⁇ day ⁇ atm.
- Example 2 Using this solution, a film coated with a composition of PVA and a swellable inorganic layered silicate was prepared in the same manner as in Example 1, but cracks occurred on the surface of the coat layer due to slight bending, and the appearance was poor. there were.
- the oxygen permeability of this film was measured in the same manner as in Example 1. As a result, it was 59 ml / m 2 ⁇ day ⁇ atm.
- Example 8 EVOH and swollen in the same manner as in Example 1 except that Kuraray Eval VM-XL # 15 (15 ⁇ m biaxially stretched EVOH film subjected to aluminum vapor deposition) was used as the substrate (D). A film coated with a composition of a porous inorganic layered silicate was prepared, and the oxygen permeability of this film was evaluated. The number of waviness measured in the same manner as in Example 1 was 0.6 / mm 2 . A part of the sample film was cut out and vacuum-dried at 40 ° C.
- the oxygen transmission amount at 100 ° C.-0% RH was measured with an oxygen transmission amount measuring device (GTR-30XFKE, manufactured by GTR Tech Co., Ltd.).
- the oxygen permeability was calculated.
- the oxygen permeability of this film was below the measurement limit (0.1 ml / m 2 ⁇ day ⁇ atm).
- the result of measuring the oxygen permeability of the coated film of Example 1 under the same conditions was 160 ml / m 2 ⁇ day ⁇ atm.
- Example 9 The same procedure as in Example 1 was used, except that the substrate (D) used was Kuraray Co., Ltd. Eval EF-XL # 15 (15 ⁇ m biaxially stretched EVOH film) obtained by depositing silicon oxide by the PVD method. Then, a film coated with a composition of EVOH and a swellable inorganic layered silicate was prepared, and oxygen permeability was evaluated in the same manner as in Example 8. As a result, the oxygen permeability of this film was below the measurement limit (0.1 ml / m 2 ⁇ day ⁇ atm). The number of undulations measured in the same manner as in Example 1 was 0.5 / mm 2 .
- Example 10 50 kg of a coating solution having the same composition as in Example 1 was prepared in the same manner as in Example 1.
- a 110-line gravure roll is set on a gravure coater (two-roll system) of a film processing tester manufactured by Modern Machinery Co., Ltd., and a line speed of 140 m / min is applied to a 600 mm wide film of Kuraray Eval VM-XL # 15.
- This coating solution was coated.
- the smoothing roll was rotated at 30 rpm in the direction opposite to the film flow direction. Therefore, the linear velocity Vs on the smoothing roll surface was ⁇ 5.65 m / min. Further, the tension of the smoothing roll part was 3.3 kg / cm, the drying temperature was 140 ° C., and the drying furnace length was about 9 m.
- the thickness of the composition layer of EVOH and swellable inorganic layered silicate of the obtained coated film was 0.8 ⁇ m.
- the oxygen permeability of this film was evaluated in the same manner as in Example 8, it was below the measurement limit (0.1 ml / m 2 ⁇ day ⁇ atm).
- the result of measuring the number of undulations in the same manner as in Example 1 was 0.3 / mm 2 .
- Example 14 A film coated with a composition of EVOH and a swellable inorganic layered silicate was prepared in the same manner as in Example 10 except that the smoothing roll was not used, and the number of waviness was measured in the same manner as in Example 1. . As a result, the number of undulations of this coated film exceeded 30 / mm 2 even with a large one, and the smoothness was very poor.
- Example 11 A film coated with a composition of EVOH and a swellable inorganic layered silicate was prepared in the same manner as in Example 10 except that a roll wound with No. 32 wire was used as a smoothing roll, and the number of swells was evaluated. . As a result, the number of waviness of the present coated film was 0.7 / mm 2 .
- Example 15 A film coated with a composition of EVOH and a swellable inorganic layered silicate was prepared in the same manner as in Example 10 except that a smooth roll having a diameter of 2 mm was used as the smoothing roll and the roll was not rotated. Since the smoothing roll was bent, the film could not be uniformly adhered to the film. As a result of evaluation of the number of undulations of this coated film, the portion where the smoothing roll hit was at least 0.3 pieces / mm 2 , but the portion where the smoothing roll did not hit exceeded 30 pieces / mm 2 , which was poor. Met.
- Example 13 A film coated with a composition of EVOH and a swellable inorganic layered silicate was prepared in the same manner as in Example 10 except that the rotation direction of the smoothing roll was the forward direction with respect to the film flow direction and was rotated at 30 rpm. Then, the number of swells was evaluated. As a result, the number of waviness of the present coated film was 0.6 / mm 2 .
- Example 15 A film coated with a composition of EVOH and a swellable inorganic layered silicate was prepared in the same manner as in Example 10 except that the line speed was 30 m / min, and the number of swells was evaluated. As a result, the number of waviness of the present coated film was 0.2 / mm 2 .
- Example 18 A film coated with a composition of EVOH and a swellable inorganic layered silicate was prepared in the same manner as in Example 10 except that a roll wound with No. 100 wire was used as a smoothing roll, and the number of swells was evaluated. . As a result, the number of waviness of the present coated film was 4.0 pieces / mm 2 .
- Example 19 A film coated with a composition of EVOH and a swellable inorganic layered silicate was prepared in the same manner as in Example 10 except that the tension of the smoothing roll part was 20 kg / cm. A lot of coating liquid was scraped off by the smoothing roll. As a result, a large amount of the coating liquid was dripped and dropped from the smoothing roll, and stable coating was impossible.
- Example 20 A film coated with a composition of EVOH and a swellable inorganic layered silicate was prepared in the same manner as in Example 10 except that the tension of the smoothing roll part was changed to 0.5 kg / cm. The film could not be uniformly adhered to the roll. As a result of evaluation of the number of undulations of this coated film, the portion where the smoothing roll hit was at least 0.4 pieces / mm 2 , but the portion where the smoothing roll did not hit exceeded 30 pieces / mm 2 , which was poor. Met.
- Comparative Example 11 in which the blending ratio of the swellable inorganic layered silicate (B) is less than 0.5%, only the water-soluble or water-dispersible polymer (A) that does not contain the swellable inorganic layered silicate (B). Compared with Comparative Example 3 coated with No. 1, the improvement in barrier properties is negligible.
- Comparative Example 13 in which the blending ratio of the swellable inorganic layered silicate (B) exceeds 55%, the coat layer is liable to crack, and the water-soluble or water-dispersible property does not contain the swellable inorganic layered silicate (B). Even compared with Comparative Example 3 in which only the polymer (A) was coated, the barrier property was worse.
- Comparative Example 13 in which aluminum was vapor-deposited on an EVOH biaxially stretched film with good barrier properties showed relatively good barrier properties even at high temperatures, but it was water-soluble or water-dispersible polymer (A) and swellable inorganic layered silicate.
- Examples 8 to 9 coated with the resin composition (C) containing (B) exhibit very good barrier properties below the measurement limit even at high temperatures, and are one of the preferred embodiments of the present invention. I understand.
- the gas barrier film containing the resin composition layer in which the swellable layered inorganic silicate of the present invention is dispersed has a very good gas barrier property and can be used for a gas barrier packaging material.
- the gas barrier film production method of the present invention makes it possible to produce a gas barrier film with very little irregularity on the surface of the resin composition layer.
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Abstract
Description
11.0≧D≧2.0μm (1)
σ≧1.8μm (2)
ここで、Dおよびσは、レーザー回折方式により測定した膨潤性無機層状珪酸塩(B)の対数平均粒径およびその粒度分布の標準偏差である。
0.5 ≧ Vs/Vf ≧ -1 (3)
但し、Vsはスムージングロール表面の回転方向への線速度、Vfはフィルムのライン速度である。Vsが負の値をとる場合は、スムージングロールがフィルムの流れ方向に対して逆方向に回転している事を意味する。
11.0≧D≧2.0μm (1)
σ≧1.8μm (2)
ここでDおよびσは、レーザー回折方式により測定した膨潤性無機層状珪酸塩(B)の対数平均粒径およびその粒度分布の標準偏差である。Dのより好適な範囲は2.4μm~10μm、更に好適には2.8μm~9μm、最も好適には3.2μm~8μmである。また、σのより好適な範囲は1.9μm以上、更に好適には2.0μm以上、最も好適には2.1μm以上である。
0.5 ≧ Vs/Vf ≧ -1 (3)
ここで、Vsはスムージングロール表面の線速度、Vfはフィルムのライン速度である。Vs/Vfが0.5を越える場合、あるいは-1を下回る場合は、何れもコート液の液だれや跳ね飛びの問題を生じやすい。この観点より、Vs/Vfの上限は、より好適には0.1、更に好適には0.05であり、下限は、より好適には-0.5、更に好適には-0.3である。
ポリエチレン-酢酸ビニル重合体のケン化により得られたポリエチレン-ビニルアルコール重合体である株式会社クラレ製EXCEVAL3110(エチレン6モル%、ケン化度98モル%以上)33.75gを、イオン交換水326.5gに入れ、90℃に加熱しながら1時間撹拌して、水溶液を得た。この水溶液を室温にまで冷却した後、溶液の安定性向上のため、50%のイソプロピルアルコール水溶液を64.75g添加した。更にこの溶液にトピー工業株式会社製NHT-ゾルB2(合成ヘクトライトの水分散液、固形分濃度5%、平均粒径3.8μm、標準偏差2.2μm)を75g添加して、EVOHと膨潤性無機層状珪酸塩を含む500gの液を得た。液中の固形分濃度は7.5%、固形分中の膨潤性無機層状珪酸塩の配合率は10%であった。
EVOHと膨潤性無機層状珪酸塩の組成物をコートしていない、株式会社クラレ製エバールEF-XL#15の酸素透過度を、実施例1と同様にして測定した。結果は1.8ml/m2・day・atmであった。
三井武田ケミカル株式会社製接着剤である、タケラックA-385を9.6gとタケネートA-50を0.8g混合し、それを酢酸エチル70gで希釈して接着剤液を準備した。この接着剤液を、東レ株式会社製二軸延伸ポリエステルフィルムであるルミラーP60の12μmのフィルムに、8番のバーコーターを用いて均一にハンドコートして、熱風乾燥機にて60℃で3分間乾燥した。乾燥後の接着剤層の厚みは0.3μmであった。この接着剤層の上に、実施例1で使用したEVOHと膨潤性無機層状珪酸塩を含む500gの液を、実施例1と同様にしてコートし、酸素透過度測定を行なった。結果は2.1ml/m2・day・atmであった。また、実施例1と同様にしてうねり数を測定した結果は0.5個/mm2であった。
EVOHと膨潤性無機層状珪酸塩の組成物をコートしていない、東レ株式会社製二軸延伸ポリエステルフィルムであるルミラーP60の12μmフィルムの酸素透過度を、実施例1と同様にして測定した。結果は92ml/m2・day・atmであった。
水溶性または水分散性ポリマー(A)として、株式会社クラレ製ポリビニルアルコール樹脂であるPVA-110H(ケン化度98モル%以上)を用いた以外は、実施例2と同様にして、PVAと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成した。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、4.1ml/m2・day・atmであった。また、実施例1と同様にしてうねり数を測定した結果は0.6個/mm2であった。
膨潤性無機層状珪酸塩(B)として、トピー工業株式会社製NHT-ゾルB5(合成ヘクトライトの水分散液、固形分濃度5%、平均粒径5.2μm、標準偏差2.3μm)を用いた以外は、実施例3と同様にして、PVAと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成した。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、3.1ml/m2・day・atmであった。また、実施例1と同様にしてうねり数を測定した結果は0.7個/mm2であった。
膨潤性無機層状珪酸塩(B)として、トピー工業株式会社製NHT-ゾルB7(合成ヘクトライトの水分散液、固形分濃度5%、平均粒径7.1μm、標準偏差2.4μm)を用いた以外は、実施例3と同様にして、PVAと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成した。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、4.2ml/m2・day・atmであった。また、実施例1と同様にしてうねり数を測定した結果は0.8個/mm2であった。
膨潤性無機層状珪酸塩(B)として、トピー工業株式会社製NTS-ゾルC(合成ナトリウム四ケイ素雲母の水分散液、固形分濃度5%、平均粒径2.8μm、標準偏差2.1μm)を用いた以外は、実施例3と同様にして、PVAと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成した。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、9.7ml/m2・day・atmであった。また、実施例1と同様にしてうねり数を測定した結果は0.5個/mm2であった。
膨潤性無機層状珪酸塩(B)の水分散液を添加しなかった以外は、実施例3と同様にして、PVAをコートしたフィルムを作成した。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、53ml/m2・day・atmであった。
膨潤性無機層状珪酸塩(B)として、トピー工業株式会社製NHT-ゾルB10(合成ヘクトライトの水分散液、固形分濃度5%、平均粒径10.4μm、標準偏差2.4μm)を用いた以外は、実施例3と同様にして、PVAをコートしたフィルムを作成した。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、15ml/m2・day・atmであった。また、実施例1と同様にしてうねり数を測定した結果は0.9個/mm2であった。
膨潤性無機層状珪酸塩(B)として、トピー工業株式会社製NTS-5(合成ナトリウム四ケイ素雲母の水分散液、固形分濃度6%、平均粒径11.5μm、標準偏差2.4μm)を用いた以外は、実施例3と同様にして、PVAをコートしたフィルムを作成した。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、21ml/m2・day・atmであった。
膨潤性無機層状珪酸塩(B)として、トピー工業株式会社製NTS-10(合成ナトリウム四ケイ素雲母の水分散液、固形分濃度10%、平均粒径14.0μm、標準偏差2.5μm)を用いた以外は、実施例3と同様にして、PVAをコートしたフィルムを作成した。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、29ml/m2・day・atmであった。
膨潤性無機層状珪酸塩(B)として、トピー工業株式会社製NHT-ゾル1(合成ヘクトライトの水分散液、固形分濃度5%、平均粒径1.1μm、標準偏差2.1μm)を用いた以外は、実施例3と同様にして、PVAをコートしたフィルムを作成した。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、33ml/m2・day・atmであった。
膨潤性無機層状珪酸塩(B)として、トピー工業株式会社製NHT-ゾル2(合成ヘクトライトの水分散液、固形分濃度5%、平均粒径2.2μm、標準偏差1.6μm)を用いた以外は、実施例3と同様にして、PVAをコートしたフィルムを作成した。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、30ml/m2・day・atmであった。
膨潤性無機層状珪酸塩(B)として、トピー工業株式会社製NHT-ゾルB1(合成ヘクトライトの水分散液、固形分濃度5%、平均粒径1.1μm、標準偏差1.6μm)を用いた以外は、実施例3と同様にして、PVAをコートしたフィルムを作成した。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、38ml/m2・day・atmであった。
膨潤性無機層状珪酸塩(B)として、クニミネ工業株式会社製クニピアF(天然モンモリロナイト、平均粒径1.9μm、標準偏差1.6μm)を脱イオン水に固形分5%になるように添加して、家庭用ミキサーで30分間攪拌して得た水分散液を用いた以外は、実施例3と同様にして、PVAと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成した。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、33ml/m2・day・atmであった。
膨潤性無機層状珪酸塩(B)として、コープケミカル株式会社製シマソフME-100(膨潤性フッ素マイカ系鉱物、平均粒径5.9μm、標準偏差1.6μm)を脱イオン水に固形分5%になるように添加して、家庭用ミキサーで30分間攪拌して得た水分散液を用いた以外は、実施例3と同様にして、PVAと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成した。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、28ml/m2・day・atmであった。
株式会社クラレ製EXCEVAL3110の量を37.39gに、イオン交換水の量を395.61gに、トピー工業株式会社製NHT-ゾルB2の量を2.25gに変更した以外は実施例1と同様にしてEVOHと膨潤性無機層状珪酸塩を含む500gの液を得た。液中の固形分中の膨潤性無機層状珪酸塩の配合率は0.3%であった。この液を用いて、実施例1と同様にして、PVAと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成した。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、42ml/m2・day・atmであった。
トピー工業株式会社製NHT-ゾルB2(固形分濃度5%)450g、イオン交換水2.625g、イソプロピルアルコール32.375gの混合液を調整し、これに株式会社クラレ製EXCEVAL3110を15g添加して90℃に加熱しながら1時間撹拌し、EVOHと膨潤性無機層状珪酸塩を含む500gの液を得た。液中の固形分中の膨潤性無機層状珪酸塩の配合率は60%であった。この液を用いて実施例1と同様にして、PVAと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成したが、わずかな屈曲によりコート層表面にクラックが発生し、外観は不良であった。このフィルムの酸素透過度を、実施例1と同様にして測定した結果、59ml/m2・day・atmであった。
基材(D)として、株式会社クラレ製エバールVM-XL#15(15μmの二軸延伸EVOHフィルムにアルミ蒸着を施した物)を用いた以外は、実施例1と同様にして、EVOHと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成し、このフィルムの酸素透過度の評価を行なった。実施例1と同様にしてうねり数を測定した結果は0.6個/mm2であった。試料フィルムの一部を切り取り、40℃で24時間真空乾燥した後、酸素透過量測定装置(GTRテック株式会社製、GTR-30XFKE)にて、100℃-0%RHの酸素透過量を測定して酸素透過度を算出した。その結果、このフィルムの酸素透過度は測定限界(0.1ml/m2・day・atm)以下であった。この時、同じ条件で実施例1のコートフィルムの酸素透過度を測定した結果は、160ml/m2・day・atmであった。
EVOHと膨潤性無機層状珪酸塩の組成物をコートしていない、株式会社クラレ製エバールVM-XL#15の酸素透過度を、実施例8と同様にして測定した。結果は1.1ml/m2・day・atmであった。
基材(D)として、株式会社クラレ製エバールEF-XL#15(15μmの二軸延伸EVOHフィルム)に、PVD法にて酸化ケイ素を蒸着した物を用いた以外は、実施例1と同様にして、EVOHと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成し、実施例8と同様にして酸素透過度の評価を行なった。その結果、このフィルムの酸素透過度は測定限界(0.1ml/m2・day・atm)以下であった。また、実施例1と同様にしてうねり数を測定した結果は0.5個/mm2であった。
実施例1と同一組成のコート液を、実施例1と同様の方法で50kg準備した。モダンマシナリー株式会社製フィルム加工試験装置のグラビアコーター(ツーロール方式)に110線のグラビアロールをセットし、株式会社クラレ製エバールVM-XL#15の600mm幅のフィルムに、ライン速度は140m/分で本コート液をコートした。フィルムがグラビアロールから離れてから約30cm下流側に設置した、直径60mmの表面を平滑に加工したスムージングロールをフィルムのコート面に押し当て、コート面を均一にした後、乾燥炉に導入して乾燥・巻取りを行なった。この時、スムージングロールはフィルムの流れ方向と逆方向に30rpmで回転させた。従って、スムージングロール表面の線速度Vsは-5.65m/分であった。また、スムージングロール部のテンションは3.3Kg/cm、乾燥温度は140℃、乾燥炉長は約9mであった。
スムージングロールを使用しなかった以外は実施例10と同様にして、EVOHと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成し、実施例1と同様にしてうねり数の測定を行なった。その結果、本コートフィルムのうねり数は大きな物でも30個/mm2を越えており、非常に平滑性は不良であった。
スムージングロールとして32番のワイヤーを巻いたロールを使用した以外は実施例10と同様にして、EVOHと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成し、うねり数の評価を行なった。その結果、本コートフィルムのうねり数は0.7個/mm2であった。
スムージングロールとして直径10mmの平滑ロールを使用して、フィルムの流れ方向に逆方向に30rpmで回転させた(Vs=-0.94m/分)以外は実施例10と同様にして、EVOHと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成し、うねり数の評価を行なった。その結果、本コートフィルムのうねり数は0.5個/mm2であった。
スムージングロールとして直径2mmの平滑ロールを使用し、それを回転させなかった以外は実施例10と同様にして、EVOHと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成した。スムージングロールがたわむため、フィルムに均一に密着させる事ができなかった。このコートフィルムのうねり数の評価結果は、スムージングロールの当たった部分は最低0.3個/mm2であったが、スムージングロールの当たらなかった部分は30個/mm2を越えており、不良であった。
スムージングロールの回転方向を、フィルムの流れ方向に対して順方向として、30rpmで回転させた以外は実施例10と同様にして、EVOHと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成し、うねり数の評価を行なった。その結果、本コートフィルムのうねり数は0.6個/mm2であった。
スムージングロールとして直径120mmの平滑ロールを使用して、フィルムの流れ方向に逆方向に30rpmで回転させた(Vs=-11.3m/分)以外は実施例10と同様にして、EVOHと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成し、うねり数の評価を行なった。その結果、本コートフィルムのうねり数は0.1個/mm2であった。
ライン速度を30m/分にした以外は実施例10と同様にして、EVOHと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成し、うねり数の評価を行なった。その結果、本コートフィルムのうねり数は0.2個/mm2であった。
スムージングロールをフィルムの流れ方向に順方向に90rpmで回転させた(Vs=17.0m/分)以外は実施例15と同様にして、EVOHと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成し、うねり数の評価を行なった。その結果、本コートフィルムのうねり数は2.8個/mm2であった。
スムージングロールをフィルムの流れ方向に逆方向に180rpmで回転させた(Vs=-33.9m/分)以外は実施例15と同様にして、EVOHと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成したところ、スムージングロール上のコート液がはね散って装置のガイドロールなどに付着したため、安定したコーティングが不可能であった。
スムージングロールとして100番のワイヤーを巻いたロールを使用した以外は実施例10と同様にして、EVOHと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成し、うねり数の評価を行なった。その結果、本コートフィルムのうねり数は4.0個/mm2であった。
スムージングロール部のテンションを20Kg/cmとした以外は実施例10と同様にして、EVOHと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成したところ、スムージングロールによりコート液が多くかき取られすぎて、多量のコート液がスムージングロールからしたたり落ちる状態となり、安定したコーティングが不可能であった。
スムージングロール部のテンションを0.5Kg/cmとした以外は実施例10と同様にして、EVOHと膨潤性無機層状珪酸塩の組成物をコートしたフィルムを作成したところ、フィルムのシワのため、スムージングロールにフィルムに均一に密着させる事ができなかった。このコートフィルムのうねり数の評価結果は、スムージングロールの当たった部分は最低0.4個/mm2であったが、スムージングロールの当たらなかった部分は30個/mm2を越えており、不良であった。
Claims (16)
- 基材(D)上の少なくとも片面に、水溶性または水分散性ポリマー(A)と下式(1)、(2)を満足する膨潤性無機層状珪酸塩(B)を含有する樹脂組成物(C)からなる層を有することを特徴とするガスバリア性フィルム。
11.0≧D≧2.0μm (1)
σ≧1.8μm (2)
但し、Dおよびσは、レーザー回折方式により測定した膨潤性無機層状珪酸塩(B)の対数平均粒径およびその粒度分布の標準偏差。 - 請求項1記載の樹脂組成物(C)において、膨潤性無機層状珪酸塩(B)の配合率が0.5~55重量%である事を特徴とする請求項1に記載のガスバリア性フィルム。
- 水溶性または水分散性ポリマー(A)が、ポリビニルアルコール系ポリマーである事を特徴とする請求項1~2のいずれか一項に記載のガスバリア性フィルム。
- ポリビニルアルコール系ポリマーが、エチレン-ビニルアルコール系ポリマーである事を特徴とする請求項3に記載のガスバリア性フィルム。
- 膨潤性無機層状珪酸塩(B)が合成無機層状珪酸塩である事を特徴とする請求項1~4のいずれか一項に記載のガスバリア性フィルム。
- 膨潤性無機層状珪酸塩(B)が合成スメクタイトである事を特徴とする請求項5に記載のガスバリア性フィルム。
- 膨潤性無機層状珪酸塩(B)および、水溶性または水分散性ポリマー(A)を含有する樹脂組成物層(C)および/または基材(D)の少なくとも片面に、金属および/または金属酸化物からなる蒸着層(E)を有する事を特徴とする請求項1~6のいずれか一項に記載のガスバリア性フィルム。
- 基材(D)が、ポリアミド系ポリマー、ポリエステル系ポリマー、ポリビニルアルコール系ポリマーからなる群より選ばれる、少なくとも1種のポリマーからなるフィルムである請求項1~7のいずれかに記載のガスバリア性フィルム。
- 基材(D)が、エチレン-ビニルアルコール系ポリマーからなるフィルムである、請求項8に記載のガスバリア性フィルム。
- 樹脂組成物(C)からなる層表面の、直径25~100μmの範囲内のうねり数が1mm2あたり1個未満である事を特徴とする、請求項1~9のいずれか一項に記載のガスバリア性フィルム。
- 膨潤性無機層状珪酸塩(B)、および水溶性または水分散性ポリマー(A)を含む溶液または水分散液をコート設備で基材(D)上に塗布し、スムージングロールにより平滑にした後、乾燥する事を特徴とする請求項10に記載のガスバリア性フィルムの製造方法。
- スムージングロールの直径が3mm以上である事を特徴とする、請求項11に記載のガスバリア性フィルムの製造方法。
- スムージングロールが、スムージングロールに巻くワイヤーが75番以下のものである、またはワイヤーを巻かない平滑ロールである事を特徴とする請求項11または12のいずれか一項に記載のガスバリア性フィルムの製造方法。
- スムージングロール部のフィルムテンションが、1.0~15Kg/cmである事を特徴とする、請求項11~13のいずれか一項に記載のガスバリア性フィルムの製造方法。
- スムージングロール表面の線速度と、フィルムのライン速度が、以下の式(3)の範囲にある事を特徴とする、請求項11~14のいずれか一項に記載のガスバリア性フィルムの製造方法。
0.5 ≧ Vs/Vf ≧ -1 (3)
但し、Vsはスムージングロール表面の線速度、Vfはフィルムのライン速度。 - 請求項1~10のいずれか一項に記載のガスバリア性フィルムを少なくとも1層以上有する事を特徴とする包装材料。
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- 2009-03-31 WO PCT/JP2009/056685 patent/WO2009123200A1/ja active Application Filing
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- 2009-03-31 US US12/935,717 patent/US20110045251A1/en not_active Abandoned
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Cited By (14)
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JP2016530124A (ja) * | 2013-07-12 | 2016-09-29 | クラレイ ユーロップ ゲゼルシャフト ミット ベシュレンクテル ハフツングKuraray Europe GmbH | 改善された耐湿性を達成するためのガスバリアコーティングを有するプラスチック容器をコーティングする方法 |
WO2015152069A1 (ja) * | 2014-03-31 | 2015-10-08 | 大日本印刷株式会社 | ガスバリア性フィルム及びその製造方法 |
JP2015193194A (ja) * | 2014-03-31 | 2015-11-05 | 大日本印刷株式会社 | ガスバリア性フィルムとその製造方法 |
JP2015193193A (ja) * | 2014-03-31 | 2015-11-05 | 大日本印刷株式会社 | ガスバリア性フィルムとその製造方法 |
US10030113B2 (en) | 2014-03-31 | 2018-07-24 | Dai Nippon Printing Co., Ltd. | Gas barrier film and method for producing it |
JP2017171381A (ja) * | 2016-03-25 | 2017-09-28 | 昭和電工パッケージング株式会社 | 内容物付着防止蓋材の製造方法 |
JP2020196259A (ja) * | 2019-05-28 | 2020-12-10 | 王子ホールディングス株式会社 | バリア性積層体およびその製造方法 |
JP7439641B2 (ja) | 2019-05-28 | 2024-02-28 | 王子ホールディングス株式会社 | バリア性積層体およびその製造方法 |
JP2021020357A (ja) * | 2019-07-26 | 2021-02-18 | 凸版印刷株式会社 | ガスバリア性フィルム |
JP7363162B2 (ja) | 2019-07-26 | 2023-10-18 | Toppanホールディングス株式会社 | ガスバリア性フィルム |
JP7521669B2 (ja) | 2019-07-26 | 2024-07-24 | Toppanホールディングス株式会社 | ガスバリア性フィルム |
WO2021029156A1 (ja) * | 2019-08-09 | 2021-02-18 | 凸版印刷株式会社 | バリアフィルム及びバリア性包装材料 |
CN114206604A (zh) * | 2019-08-09 | 2022-03-18 | 凸版印刷株式会社 | 阻隔膜及阻隔性包装材料 |
US12083774B2 (en) | 2019-08-09 | 2024-09-10 | Toppan Inc. | Barrier film and barrier packaging material |
Also Published As
Publication number | Publication date |
---|---|
EP2263869A4 (en) | 2011-03-23 |
EP2263869A1 (en) | 2010-12-22 |
US20110045251A1 (en) | 2011-02-24 |
CN102046376B (zh) | 2014-08-20 |
EP2263869B1 (en) | 2016-06-01 |
JPWO2009123200A1 (ja) | 2011-07-28 |
CN102046376A (zh) | 2011-05-04 |
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