WO2012128136A1 - 積層フィルムおよびその製造方法 - Google Patents
積層フィルムおよびその製造方法 Download PDFInfo
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- WO2012128136A1 WO2012128136A1 PCT/JP2012/056501 JP2012056501W WO2012128136A1 WO 2012128136 A1 WO2012128136 A1 WO 2012128136A1 JP 2012056501 W JP2012056501 W JP 2012056501W WO 2012128136 A1 WO2012128136 A1 WO 2012128136A1
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- 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
- B32B27/28—Layered products comprising a layer of synthetic resin comprising synthetic resins not wholly covered by any one of the sub-groups B32B27/30 - B32B27/42
- B32B27/285—Layered products comprising a layer of synthetic resin comprising synthetic resins not wholly covered by any one of the sub-groups B32B27/30 - B32B27/42 comprising polyethers
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- G—PHYSICS
- G02—OPTICS
- G02B—OPTICAL ELEMENTS, SYSTEMS OR APPARATUS
- G02B5/00—Optical elements other than lenses
- G02B5/02—Diffusing elements; Afocal elements
- G02B5/0205—Diffusing elements; Afocal elements characterised by the diffusing properties
- G02B5/021—Diffusing elements; Afocal elements characterised by the diffusing properties the diffusion taking place at the element's surface, e.g. by means of surface roughening or microprismatic structures
- G02B5/0226—Diffusing elements; Afocal elements characterised by the diffusing properties the diffusion taking place at the element's surface, e.g. by means of surface roughening or microprismatic structures having particles on the surface
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
- B29C55/005—Shaping by stretching, e.g. drawing through a die; Apparatus therefor characterised by the choice of materials
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
- B29C55/02—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
- B29C55/023—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets using multilayered plates or sheets
- B29C55/026—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets using multilayered plates or sheets of preformed plates or sheets coated with a solution, a dispersion or a melt of thermoplastic material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
- B29C55/02—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
- B29C55/10—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial
- B29C55/12—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
- B29C55/02—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
- B29C55/10—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial
- B29C55/12—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial
- B29C55/14—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial successively
- B29C55/143—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial successively firstly parallel to the direction of feed and then transversely thereto
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- 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
- B32B27/14—Layered products comprising a layer of synthetic resin next to a particulate layer
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- 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
- B32B38/00—Ancillary operations in connection with laminating processes
- B32B38/0036—Heat treatment
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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
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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
- C08J7/043—Improving the adhesiveness of the coatings per se, e.g. forming primers
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- 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
- C08J7/08—Heat treatment
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D133/00—Coating compositions based on 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 only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Coating compositions based on derivatives of such polymers
- C09D133/04—Homopolymers or copolymers of esters
- C09D133/06—Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, the oxygen atom being present only as part of the carboxyl radical
- C09D133/062—Copolymers with monomers not covered by C09D133/06
- C09D133/066—Copolymers with monomers not covered by C09D133/06 containing -OH groups
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D133/00—Coating compositions based on 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 only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Coating compositions based on derivatives of such polymers
- C09D133/04—Homopolymers or copolymers of esters
- C09D133/14—Homopolymers or copolymers of esters of esters containing halogen, nitrogen, sulfur or oxygen atoms in addition to the carboxy oxygen
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- G—PHYSICS
- G02—OPTICS
- G02B—OPTICAL ELEMENTS, SYSTEMS OR APPARATUS
- G02B5/00—Optical elements other than lenses
- G02B5/02—Diffusing elements; Afocal elements
- G02B5/0205—Diffusing elements; Afocal elements characterised by the diffusing properties
- G02B5/021—Diffusing elements; Afocal elements characterised by the diffusing properties the diffusion taking place at the element's surface, e.g. by means of surface roughening or microprismatic structures
- G02B5/0221—Diffusing elements; Afocal elements characterised by the diffusing properties the diffusion taking place at the element's surface, e.g. by means of surface roughening or microprismatic structures the surface having an irregular structure
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- G—PHYSICS
- G02—OPTICS
- G02B—OPTICAL ELEMENTS, SYSTEMS OR APPARATUS
- G02B5/00—Optical elements other than lenses
- G02B5/02—Diffusing elements; Afocal elements
- G02B5/0273—Diffusing elements; Afocal elements characterized by the use
- G02B5/0284—Diffusing elements; Afocal elements characterized by the use used in reflection
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- 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
- B32B38/00—Ancillary operations in connection with laminating processes
- B32B38/0012—Mechanical treatment, e.g. roughening, deforming, stretching
- B32B2038/0028—Stretching, elongating
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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
- C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
- C08J2367/02—Polyesters derived from dicarboxylic acids and dihydroxy 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
- C08J2371/00—Characterised by the use of polyethers obtained by reactions forming an ether link in the main chain; Derivatives of such polymers
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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
- C08J2433/00—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 only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers
- C08J2433/04—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 only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers esters
- C08J2433/06—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 only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers esters of esters containing only carbon, hydrogen, and oxygen, the oxygen atom being present only as part of the carboxyl radical
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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
- C08J2467/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
- C08J2467/02—Polyesters derived from dicarboxylic acids and dihydroxy 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
- C08J2475/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
- C08J2475/04—Polyurethanes
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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
- C08K2201/00—Specific properties of additives
- C08K2201/002—Physical properties
- C08K2201/003—Additives being defined by their diameter
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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.]
- Y10T428/24355—Continuous and nonuniform or irregular surface on layer or component [e.g., roofing, etc.]
- Y10T428/24372—Particulate matter
- Y10T428/24405—Polymer or resin [e.g., natural or synthetic rubber, etc.]
Definitions
- the present invention relates to a laminated film having a coating layer laminated on the surface and a method for producing the same. More specifically, the present invention relates to a laminated film in which a coating layer containing organic particles is laminated on the surface and a method for producing the same.
- the backlight has a structure of a surface light source called a side light type or a direct type in order to uniformly irradiate the entire screen, not just irradiating light.
- sidelight-type backlights using CCFLs or LEDs as the light source are applied to TVs, monitors, and thin liquid crystal displays that are used in notebook computers, where thinning and energy saving are desired. Yes.
- CCFL or LED is used as an illumination light source, and the entire liquid crystal display is uniformly irradiated from the edge of the light guide plate that propagates and diffuses light uniformly. Is adopted.
- a reflection plate is provided on the back surface of the light guide plate to efficiently reflect light diffused from the light guide plate toward the liquid crystal screen.
- the unevenness printed on the surface of the light guide plate may be scraped off, or there may be a problem in that a white spot is partially generated in the liquid crystal display during lighting.
- a technology has been provided in which the reflector has a surface roughness of several microns or more by applying a coating liquid containing organic particles (plastic beads) or inorganic particles to the surface (patent) Reference 1 to 4).
- JP 2002-162511 A Japanese Patent Laid-Open No. 2003-92018 JP 2003-107216 A JP 2004-85633 A JP 2011-13402 A JP 2004-195673 A JP-A-4-288217
- the laminated film and the manufacturing method thereof according to the present invention have the following configurations.
- a coating layer containing organic particles is provided on the surface of the base film, and the ratio (SRz / d) of the surface roughness (SRz) to the coating thickness (d) of the coating layer surface is 12.5.
- the organic particles are made of a thermoplastic resin containing an ether bond, and the coating layer contains at least one selected from a sulfonic acid group, a carboxylic acid group and a hydroxyl group, and a salt thereof.
- a laminated film comprising a binder resin contained therein.
- a coating layer containing organic particles is provided on the surface of the base film, and the ratio (R / d) of the number average particle diameter (R) and coating thickness (d) of the particles on the coating layer surface is 10.5 or more, wherein the organic particles are made of a thermoplastic resin containing an ether bond, and the coating layer is at least selected from sulfonic acid groups, carboxylic acid groups and hydroxyl groups, and salts thereof
- a laminated film comprising a binder resin containing one kind.
- a laminated film in which a coating layer containing organic particles is provided on the surface of the base film can be provided at a low cost without dropping off the organic particles.
- the laminated film is composed of a base film and a coating layer containing a binder resin and organic particles provided on at least one surface thereof.
- the coating thickness of the coating layer (d: the distance from the surface of the base film where the organic particles are not included to the coating layer surface) is preferably 1100 nm or less. More preferably, it is 800 nm or less, More preferably, it is 400 nm or less.
- the coating thickness is preferably 50 nm. If the coating thickness is less than 50 nm, the organic particles may fall off.
- a section including particles is cut and observed with a scanning electron microscope (SEM) or a transmission electron microscope (TEM) to determine the coating thickness of the coating layer.
- SEM scanning electron microscope
- TEM transmission electron microscope
- Examples of the method for setting the coating thickness of the coating layer in the above range include a method achieved by adjusting the binder resin concentration of the coating liquid and the coating thickness of the coating liquid.
- the surface roughness (SRz; three-dimensional ten-point average roughness) of the coating layer surface is preferably 5 ⁇ m or more and 60 ⁇ m or less. More preferably, they are 10 micrometers or more and 30 micrometers or less. If it is less than 5 ⁇ m, white spots may occur when the laminated film coated on the white film is incorporated as a reflector in a liquid crystal display, and if it is more than 60 ⁇ m, particles may fall off.
- Examples of the method of adjusting the surface roughness so as to be included in the above range include a method of adjusting the particle size of the organic particles, the binder resin concentration of the coating liquid, and the coating thickness of the coating liquid.
- the ratio (SRz / d) of the surface roughness (SRz) of the coating layer surface to the coating thickness (d) is 12.5 or more, more preferably 25 or more, and further preferably 50 or more.
- This ratio (SRz / d) is preferably 300 or less, more preferably less than 300, still more preferably 250 or less, and particularly preferably less than 250. If the ratio (SRz / d) is outside the above range, the organic resin may not be sufficiently covered with the binder resin, and the organic particles may fall off. Therefore, it may not be preferable from the viewpoint of coating appearance.
- (SRz / d) when (SRz / d) is less than 12.5, the coating thickness tends to be thick, and the coating appearance such as coating unevenness may be deteriorated.
- Examples of the method of adjusting the ratio (SRz / d) within the above range include a method of adjusting the particle diameter of the organic particles, the binder resin concentration of the coating liquid, and the coating thickness of the coating liquid.
- the ratio (SRz / d) between the surface roughness (SRz) of the coating layer surface and the coating thickness (d) is obtained by a method described later.
- the ratio (R / d) of the number average particle diameter (R) of the particles on the coating layer surface to the coating layer thickness (d) is preferably 10.5 or more. More preferably, it is 20 or more, More preferably, it is 45 or more.
- the ratio (R / d) is preferably 250 or less, more preferably 200 or less.
- (R / d) when (R / d) is less than 10.5, the coating thickness tends to increase, and the coating appearance such as coating unevenness may be deteriorated.
- Examples of the method for adjusting the ratio (R / d) within the above range include adjusting the particle diameter of the organic particles, the binder resin concentration of the coating liquid, and the coating thickness of the coating liquid.
- the ratio (R / d) of the number average particle diameter (R) and the coating thickness (d) of the particles is determined by a method described later.
- the binder resin is made of a water-soluble resin.
- the water-soluble resin as used herein refers to a resin containing at least one functional group selected from sulfonic acid groups, carboxylic acid groups, hydroxyl groups, and salts thereof.
- the water-soluble resin is preferably a resin in which a monomer having a functional group such as a sulfonic acid group, a sulfonic acid group, a carboxylic acid group, or a carboxylic acid group is copolymerized, and more preferably a carboxylic acid group and / or a carboxylic acid group.
- a resin in which a monomer having a salt is copolymerized.
- the binder resin is a water-soluble resin, it can be used in a coating state in which the binder resin and organic particles are dissolved and dispersed in water.
- a binder resin and organic particles previously dissolved or dispersed separately in water may be arbitrarily mixed and used.
- the water-soluble resin is preferably formed from at least one selected from the group consisting of a polyester resin, an acrylic resin, and a polyurethane resin, and more preferably a polyester resin or an acrylic resin.
- the binder resin has good adhesion to the base film and is preferably transparent, and the resin can satisfy these characteristics.
- the product name Watersol (registered trademark) manufactured by DIC Corporation, pesresin of Takamatsu Yushi Co., Ltd., and the like are available.
- additives can be added to the binder resin forming the coating layer as long as the effects of the invention are not impaired.
- an antioxidant for example, an antioxidant, a crosslinking agent, a fluorescent brightening agent, an antistatic agent, a coupling agent and the like can be used.
- the adhesion to the base film can be further improved, and at the same time, the organic particles can be further prevented from falling off.
- the crosslinking agent include an isocyanate crosslinking agent, a silicone crosslinking agent, a polyolefin crosslinking agent, and the like, and an isocyanate crosslinking agent that undergoes addition polymerization with a compound having a hydroxyl group to form a urethane bond is preferably used.
- isocyanate crosslinking agent examples include, but are not limited to, 2,4-tolylene diisocyanate, 2,6-tolylene diisocyanate, hexamethylene diisocyanate, diphenylmethane diisocyanate, and the like.
- the content of the crosslinking agent in the coating layer is preferably 5% by weight or less, more preferably 0.1 to 4% by weight, and further within the range of 0.5 to 3% by weight. Most preferably it is. If the content of the crosslinking agent is within such a preferable range, the effect can be sufficiently obtained, and the film can be prevented from curling after the coating layer is provided.
- an antistatic agent By adding an antistatic agent, it is possible to prevent foreign matters such as dust from adhering to the film.
- the antistatic agent include, but are not limited to, a surfactant, an ionic conductive polymer, an electron conductive polymer, a conductive metal oxide, and metals.
- Specific examples of the surfactant and the ionic conductive polymer include the following.
- Surfactants include cationic surfactants such as sulfonated compounds, N-acyl amino acids or salts thereof, anionic surfactants such as alkyl ether carboxylates, aliphatic amine salts, and aliphatic quaternary ammonium salts. , Amphoteric surfactants such as carboxybetaine, imidazolinium betaine, and aminocarboxylate.
- sulfonated compounds are preferably applied, specifically sodium dodecylbenzenesulfonate, sodium stearylbenzenesulfonate, sodium octylbenzenesulfonate, potassium dodecylbenzenesulfonate, lithium dodecylbenzenesulfonate, lithium octylnaphthalenesulfonate, Sodium oxylnaphthalene sulfonate, sodium dodecyl naphthalene sulfonate, potassium dodecyl naphthalene sulfonate, sodium butyl sulfonate, sodium pentyl sulfonate, sodium hexyl sulfonate, sodium heptyl sulfonate, sodium octyl sulfonate, sodium nonyl sulfonate, decyl sulfone Acid sodium, sodium undecyl s
- ionic conductive polymer examples include polystyrene sulfonates and their low molecular weight compounds represented by polystyrene sulfonates such as alkali metal salts and ammonium salts thereof, alkyl phosphate ester salts and alkyl ether phosphate ester salts. Examples thereof include a phosphoric acid polymer compound copolymerized as a monomer and a polyacrylic acid ester having an ionic functional group.
- the organic particles are made of a thermoplastic resin containing an ether bond.
- a thermoplastic resin containing an ether bond By being a thermoplastic resin containing an ether bond, it is possible to increase the affinity between the organic particles and the binder resin and to prevent dropping. When organic particles are formed with a thermosetting resin, the particles may fall off. The details of the drop-off prevention mechanism are unknown, but it has good chemical affinity between the ether bond and hydrophilic substituents such as the sulfonic acid group, carboxylic acid group and hydroxyl group of the binder resin, forming a strong bond. It is thought that it is because. Further, it is considered that the organic particles are made of a thermoplastic resin, thereby forming an intermediate layer at the interface with the binder resin and forming a stronger bond.
- thermoplastic resin containing an ether bond examples include polyether resins and resins formed by copolymerization of polyethers with other resins. Specifically, polyoxymethylene, formal resin, polyphenylene oxide, polyether ketone, polyether ether ketone, polyether ketone ketone, polyether sulfone, polyphenyl sulfone, polyether imide, polyether ester, polyether ester amide, Polyesters containing polyetheramide and spiroglycol can be mentioned, and polyesters containing polyetherester and spiroglycol are preferably used from the viewpoint of transparency and reproducibility. Particularly preferred is a polyether ester whose elastic modulus can be adjusted by the copolymerization ratio.
- polyether ester examples include various trade names such as “HYTREL” (registered trademark) manufactured by DuPont, “RITEFLEX” (registered trademark) manufactured by Ticona, and There are “ARNITEL” (registered trademark) manufactured by DSM, and the like are sold by many companies.
- the thermoplastic resin constituting the organic particles preferably has a flexural modulus of 500 MPa to 3000 MPa. More preferably, it is 1000 MPa or more and 2000 MPa or less.
- the flexural modulus in the present invention refers to a value measured according to ASTM-D790-98.
- the thermoplastic resin (pellet) constituting the organic particles was dried with hot air at 90 ° C. for 3 hours or more, and the dried pellet was used with an injection molding machine (NEX-1000 manufactured by Nissei Plastic Industries).
- NEX-1000 manufactured by Nissei Plastic Industries
- the flexural modulus is smaller than the above range, white spots may occur when applied on a white film and incorporated in a liquid crystal display as a reflector. If the flexural modulus is larger than the above range, the light guide plate may be damaged when the light guide plate and the reflection plate rub against each other.
- a long-chain polyalkylene glycol can be copolymerized with the resin.
- Hytrel 7247 and Hytrel 8238 achieve a flexural modulus within the above range as a thermoplastic resin containing an ether bond.
- the organic particles can be produced by heating and melting and then spraying from a nozzle to obtain spherical particles (Japanese Patent Publication No. 2-12975), or by dissolving in a heating solvent and cooling to precipitate spherical particles.
- a method for obtaining spherical particles by forcibly dispersing a heat-melted resin in an incompatible heated polysiloxane Japanese Patent Laid-Open No. 2001-213970
- Examples of applicable methods include phase separation of a polymer solution, formation of an emulsion, and addition of a poor solvent to obtain fine particles (International Publication No. 2009/142231, Japanese Patent Application No. 2010-217158). It is done.
- the polymer solution is phase-separated to form an emulsion, and the poor solvent A method of obtaining fine particles by adding is preferably used.
- the temperature at which the emulsion formation and micronization steps are performed is 100 ° C. or higher.
- the upper limit is the temperature at which dissolution and phase separation occur, and there is no particular limitation as long as the desired fine particles can be obtained, but it is usually in the range of 100 ° C. to 300 ° C., preferably 100 ° C. to 280 ° C., More preferably, it is 120 ° C. to 260 ° C., further preferably 120 ° C. to 240 ° C., particularly preferably 120 ° C. to 220 ° C., and most preferably in the range of 120 ° C. to 200 ° C.
- the temperature it may be easy to obtain fine particles having a small particle size distribution.
- the shape of the particles may become porous, but by controlling as follows, the particle size distribution can be further reduced and the particle shape can be made into a true sphere. preferable. That is, by carrying out emulsification and micronization at a temperature higher than the temperature lowering crystallization temperature, which is the thermal characteristic of a thermoplastic resin having an ether bond, it is possible to obtain spherical microparticles with a small particle size distribution.
- the temperature-falling crystallization temperature refers to a crystallization temperature measured by a differential scanning calorimetry (DSC method), and a temperature range from 30 ° C. to a temperature exceeding 30 ° C. above the melting point of the polymer. It means the peak top of the exothermic peak that is observed when the temperature is raised once at a rate of temperature rise of 20 ° C./minute, held for 1 minute, and then lowered to 0 ° C. at 20 ° C./minute.
- DSC method differential scanning calorimetry
- the fine particles made of the thermoplastic resin having an ether bond of the present invention preferably have a particle size distribution index of 1 to 3. More preferably, it is 1 to 2, and most preferably 1 to 1.5.
- the particle size distribution index is within the above range, only a part of the particles having a large particle size are in close contact with the light guide plate and deformed when the reflector is pressed against the light guide plate. It can be prevented from becoming easy.
- the particle distribution index is larger than the above range (that is, when coarse particles are included), Mayer bar particle clogging may occur in the coating process, and coating stripes may occur, which is not preferable from the viewpoint of coating appearance. is there.
- the temperature at which the emulsion formation and fine particle formation steps are performed is 100 ° C. or higher. Can be preferably used.
- the number average particle diameter of the organic particles is preferably 3 ⁇ m or more and 60 ⁇ m or less, more preferably 4 ⁇ m or more and 20 ⁇ m or less, and further preferably 5 ⁇ m or more and 15 ⁇ m or less. If it is less than 3 ⁇ m, white spots may occur when it is applied on a reflective film and incorporated in a liquid crystal display, and if it is greater than 60 ⁇ m, particles may fall off.
- a known method can be used as a method of adjusting the particle diameter within the above range. Specific examples include the methods described in Japanese Patent Application Laid-Open No. 2001-213970 and International Publication No. 2009/142231.
- the organic particles are preferably covered with a binder resin.
- a binder resin By covering the organic particles with the binder resin, it can be made difficult to fall off.
- the organic particles are preferably a thermoplastic resin containing an ether bond, and the binder resin contained in the coating liquid is preferably a water-soluble resin.
- it is also an effective method to make SRz / d less than 300, More preferably, it is 250 or less.
- a coating state it can confirm by SEM or TEM of a particle cross section. At this time, it can be confirmed more clearly by using ruthenium staining or the like. *
- the laminated film of the present invention it is preferred particle density of the organic particles in the coating layer surface is 5 pieces / mm 2 or more 100,000 / mm 2 or less. More preferably, they are 400 pieces / mm ⁇ 2 > or more and 100,000 pieces / mm ⁇ 2 > or less, More preferably, they are 1000 pieces / mm ⁇ 2 > or more and 100,000 pieces / mm ⁇ 2 > or less.
- a laminated film having a particle density within the above numerical range is used as a reflection plate or a light diffusion film of a liquid crystal display, an appropriate light diffusibility can be obtained.
- the amount of particles in the coating liquid, the thickness of the coating film, and when coating during film formation, by adjusting the stretching ratio in the stretching step after coating can be achieved.
- the base film of the laminated film is not particularly limited, and may be transparent or opaque.
- the transparent film include a polyester film, a polyolefin film, a polystyrene film, and a polyamide film, and a polyester film is preferably used from the viewpoint of ease of molding.
- the opaque film include white films exemplified in JP-A-4-239540 and JP-A-2004-330727, and polyphenylene sulfide films exemplified in JP-A-6-305019.
- the base film is a white film.
- a white film made of a polyester resin is preferably used from the viewpoints of moldability and cost.
- a method for forming the coating layer in addition to a method of applying the coating liquid to the base film after biaxial stretching (offline coating method), a method of stretching and heat-treating the film after coating the coating liquid ( In-line coating method). From the viewpoint of adhesion between the coating layer and the base film and cost saving, an in-line coating method is preferable.
- the in-line coating method a method in which a coating liquid is applied to the surface of an unstretched film and then stretched in a biaxial direction, or a direction (for example, uniaxial) that intersects the previous uniaxial stretching direction after a coating liquid is applied to the surface of a uniaxially stretched film.
- stretching direction etc. is mentioned, the latter is preferable.
- thermoplastic resin raw material is supplied to an extrusion device, melt extrusion is performed at a temperature equal to or higher than the melting point of the thermoplastic resin, and extruded as a molten sheet from a slit-shaped die onto a rotating cooling drum, and a glass transition is performed on the surface of the rotating cooling drum. Rapidly solidify to a temperature below the temperature to obtain an unstretched sheet in an amorphous state.
- an electrostatic application adhesion method is preferably employed.
- the ratio of the surface roughness (SRz) of the coating layer surface after drying to the coating thickness (d) is adjusted by adjusting the particle size of the organic particles, the binder resin concentration of the coating solution, and the coating thickness of the coating solution. ) Is 12.5 or more.
- the ratio (SRz / d) can be increased by lowering the solid content concentration of the coating liquid, reducing the coating thickness of the coating liquid, and increasing the particle diameter of the organic particles.
- the number average particle diameter R ′ of the organic particles contained in the coating liquid is preferably 5 ⁇ m or more.
- the particle size distribution index of the organic particles contained in the coating liquid is preferably 1 to 3.
- the flexural modulus of the organic particles contained in the coating liquid is preferably 500 MPa to 3000 MPa.
- the bending elastic modulus of the organic particles contained in the coating layer can be efficiently set to 500 MPa to 3000 MPa.
- the stretching temperature is usually in the range of (the glass transition temperature of the thermoplastic resin constituting the base film ⁇ 5 ° C.) to (the glass transition temperature of the thermoplastic resin constituting the base film + 25 ° C.), and the stretching ratio is usually 3 to 6 Double the range. Stretching can be performed in one step or in two or more steps.
- a coating solution is applied to at least one surface of the film.
- a coating method of the coating liquid for example, a wire bar coater, a reverse roll coater, a gravure coater, a rod coater, an air doctor coater, or any other coating device can be used.
- the coating layer may be formed on only one side of the film or on both sides.
- the coated film is preheated to a temperature range of 90 to 150 ° C. in the preheating zone of the tenter and appropriately dried, and then stretched in the width direction (direction perpendicular to the longitudinal direction).
- the stretching temperature is usually in the range of (the glass transition temperature of the thermoplastic resin constituting the base film ⁇ 5 ° C.) to (the glass transition temperature of the thermoplastic resin constituting the base film + 40 ° C.), and the stretching ratio is usually The range is 3 to 6 times, preferably 3.2 to 4.5 times.
- the film Prior to the preheating, the film may be once cooled below the glass transition point.
- heat treatment is performed for 1 second to 5 minutes under 20% elongation, contraction or constant length.
- relaxation treatment is usually performed within 10%, preferably within 5% in the longitudinal direction and / or the width direction during or after the heat treatment step. You may do.
- the heat treatment temperature varies depending on the stretching conditions, but is usually in the range of 180 to 250 ° C., preferably 190 to 230 ° C. When the heat treatment temperature exceeds 250 ° C., the orientation of the film tends to decrease, and a part of the coating layer may be thermally decomposed. On the other hand, when the heat treatment temperature is lower than 180 ° C., the thermal shrinkage rate of the film may become too large.
- the film of the present invention can be suitably used as a light reflecting plate.
- it can be suitably used as a light reflecting plate for a backlight.
- it can be suitably used as a light reflecting plate for a sidelight type backlight.
- the sidelight-type backlight has at least a light source, a light guide plate, and a reflection plate, but may include a housing or the like.
- the type of the light source is not particularly limited, but a particularly great effect can be obtained when CCFL or LED is used as the light source.
- the light source is located at an edge portion of the light guide plate.
- Measurement / evaluation method (5.1) Measurement method of surface roughness (SRz) and ratio of surface roughness to coating thickness (d) (SRz / d) Measured according to JIS-B-0601 (2001) Carried out.
- SRz surface roughness
- d coating thickness
- the coating state in the coating film of an organic particle was confirmed with the obtained cross-sectional photograph, and it determined as follows.
- A When the coating film covers 80% or more of the particles: B
- B When the particle coating is 40% or more: C
- D When the particle coating is less than 40%: D
- the glossiness before and after the scraping test was compared.
- the glossiness was measured according to JIS Z-8741 (1997) from the coating layer side of the laminated film using a digital variable glossiness meter UGV-5B (manufactured by Suga Test Instruments Co., Ltd.).
- a surface SEM photograph was taken to observe dropout marks, and 100 points were observed in total (number of particles + dropout marks), and evaluated based on the following criteria. When there is no drop mark: A When there are 5 or less drop marks: B When there are 10 or less drop marks: C When there are 30 or less drop marks: D If there are more than 30 dropout marks: E
- the used backlight is a side light type backlight, has a light guide plate and a light source (LED), and a light source is located in the edge part of a light guide plate.
- a white spot evaluation method for example, as shown in FIG. 3 as an example of white spot evaluation, a white spot does not occur (FIG. 3A) and a white spot occurs (FIG. 3B). Can be clearly distinguished.
- glossiness (85 °) is less than 30: A When glossiness (85 °) is 30 or more and less than 80: B When the glossiness (85 °) is 80 or more and less than 100: C When glossiness (85 °) is 100 or more: D
- Cyclic olefin copolymer resin As an incompatible component, a cyclic olefin resin “TOPAS” (registered trademark, polyplastics) having a glass transition temperature of 178 ° C. and an MVR (260 ° C./2.16 kg) of 4.5 ml / 10 min. Used).
- TOPAS cyclic olefin resin
- Polyester binder resin (Material A-1) Pesresin A-215E (manufactured by Takamatsu Yushi Co., Ltd., 30 wt% solution: containing a carboxylic acid group and a hydroxyl group) was diluted with purified water to prepare a 25 wt% solution.
- Polyester binder resin (Material A-2) 28.3 parts by weight of dimethyl terephthalate, 23.3 parts by weight of dimethyl isophthalate, 12.7 parts by weight of dimethyl adipate, 7.5 parts by weight of dimethyl 5-sodium sulfoisophthalate, 37.3 parts by weight of ethylene glycol, 17 parts of diethylene glycol 17 0.5 part by weight, 0.035 part by weight of magnesium acetate and 0.3 part by weight of lithium acetate were added and subjected to a transesterification according to a conventional method. 0.035 parts by weight of ethyl acetate was added.
- the obtained fine particles were mixed with purified water to prepare a 40 mass% aqueous dispersion, and this was used as material C. Observation with a scanning electron microscope revealed true spherical fine particles. The melting point of this polyether ester was 218 ° C., and the temperature-falling crystallization temperature of this polyether ester was 157 ° C.
- PVA-1500 weight average molecular weight 29,000: acetic acid by washing with methanol After adding 14 g of the product whose sodium content was reduced to 0.05% by mass and replacing with nitrogen, the mixture was heated to 180 ° C. and stirred for 4 hours until the polymer was dissolved. Thereafter, 350 g of ion-exchanged water as a poor solvent was dropped at a speed of 2.92 g / min via a liquid feed pump. After the entire amount of water has been added, the temperature is lowered while stirring, and the resulting suspension is filtered, washed with 700 g of ion exchange water and reslurried, and the filtered product is vacuum dried at 80 ° C. for 10 hours. 25.5 g of a white solid was obtained.
- the polyether ester fine particles had a number average particle size of 7.0 ⁇ m, a volume average particle size of 8.6 ⁇ m, and a particle size distribution index of 1.23. It was.
- the obtained fine particles were mixed with purified water to prepare a 40 mass% aqueous dispersion, and this was used as material D.
- Observation with a scanning electron microscope revealed true spherical fine particles.
- the melting point of this polyether ester was 218 ° C., and the temperature-falling crystallization temperature of this polyether ester was 157 ° C.
- the polyether ester fine particles had a number average molecular diameter of 9.8 ⁇ m, a volume average particle diameter of 12.5 ⁇ m, and a particle diameter distribution index of 1.28. there were.
- the obtained fine particles were mixed with purified water to prepare a 40 mass% aqueous dispersion, and this was used as material E.
- Observation with a scanning electron microscope revealed true spherical fine particles.
- the melting point of this polyether ester was 218 ° C., and the temperature-falling crystallization temperature of this polyether ester was 157 ° C.
- the obtained powder When the obtained powder was observed with a scanning electron microscope, it was a spherical fine particle, a polyether ester fine particle having a number average particle size of 12.0 ⁇ m, a volume average particle size of 14.7 ⁇ m, and a particle size distribution index of 1.23. Met. Observation with a scanning electron microscope revealed true spherical fine particles. The melting point of this polyether ester was 224 ° C., and the temperature-falling crystallization temperature of this polyether ester was 161 ° C. The obtained particles were mixed with purified water to prepare a 40 mass% aqueous dispersion, and this was used as material G.
- the generated aqueous dispersion of particles is filtered through a cellulose acetate membrane filter having a pore size of 0.45 ⁇ m, and the particles recovered by the membrane filter are dispersed again in 10 times the amount of pure water and washed with stirring for about 30 minutes. And filtered again. Such a washing operation was repeated twice.
- the sample washed twice was dried overnight in a 45 ° C. oven to obtain fine particles (C1).
- the number average particle diameter of the obtained particles (C1) was 70 ⁇ m.
- the powder of the material H was observed with a scanning electron microscope, it was a spherical fine particle, and polyether ester fine particles having a number average particle size of 14.2 ⁇ m, a volume average particle size of 64.5 ⁇ m, and a particle size distribution index of 4.54. Met.
- the obtained fine particles were mixed with purified water to prepare a 40 mass% aqueous dispersion, and this was used as material H.
- the obtained powder When the obtained powder was observed with a scanning electron microscope, it was a true spherical fine particle, a polyether ester fine particle having a number average particle size of 13.2 ⁇ m, a volume average particle size of 15.4 ⁇ m, and a particle size distribution index of 1.17. Met. Observation with a scanning electron microscope revealed true spherical fine particles.
- the obtained fine particles were mixed with purified water to prepare a 40 mass% aqueous dispersion, and this was used as material I.
- the generated aqueous dispersion of particles is filtered through a cellulose acetate membrane filter having a pore size of 0.45 ⁇ m, and the particles recovered by the membrane filter are dispersed again in 10 times the amount of pure water and washed with stirring for about 30 minutes. And filtered again. Such a washing operation was repeated twice.
- the sample washed twice was dried overnight in a 45 ° C. oven to obtain fine particles (C1).
- the number average particle diameter of the obtained particles (C1) was 70 ⁇ m.
- the powder of the material H When the powder of the material H is observed with a scanning electron microscope, it is a spherical fine particle, and polyether ester fine particles having a number average particle size of 11.4 ⁇ m, a volume average particle size of 34.2 ⁇ m, and a particle size distribution index of 3.00. Met.
- the obtained fine particles were mixed with purified water to prepare a 40 mass% aqueous dispersion, and this was designated as material J.
- Organic particles (material K) Synthesis of aliphatic polyether ester (D1) 48.0 parts of terephthalic acid, 42.0 parts of 1,4-butanediol and 10.0 parts of polytetramethylene glycol having a weight average molecular weight of about 3000 Then, 0.01 part of titanium tetrabutoxide and 0.005 part of mono-n-butyl-monohydroxytin oxide were charged into a reaction vessel equipped with a helical ribbon type stirring blade, and heated at 190 to 225 ° C. for 3 hours to give reaction water. The esterification reaction was carried out while distilling out of the system.
- D1 48.0 parts of terephthalic acid, 42.0 parts of 1,4-butanediol and 10.0 parts of polytetramethylene glycol having a weight average molecular weight of about 3000 Then, 0.01 part of titanium tetrabutoxide and 0.005 part of mono-n-butyl-monohydroxytin oxide were charged into
- the obtained powder When the obtained powder was observed with a scanning electron microscope, it was a spherical fine particle, a polyether ester fine particle having a number average particle size of 12.0 ⁇ m, a volume average particle size of 14.7 ⁇ m, and a particle size distribution index of 1.23. Met. Observation with a scanning electron microscope revealed true spherical fine particles.
- the obtained fine particles were mixed with purified water to prepare a 40% by mass aqueous dispersion, which was designated as material K.
- the obtained powder When the obtained powder was observed with a scanning electron microscope, it was a spherical fine particle, and polyether ester fine particles having a number average particle size of 1.5 ⁇ m, a volume average particle size of 1.8 ⁇ m, and a particle size distribution index of 1.20. Met.
- the obtained fine particles were mixed with purified water to prepare a 40 mass% aqueous dispersion, and this was used as material L.
- the obtained powder When the obtained powder was observed with a scanning electron microscope, it was a spherical fine particle, and polyether ester fine particles having a number average particle size of 2.2 ⁇ m, a volume average particle size of 2.7 ⁇ m, and a particle size distribution index of 1.23. Met.
- the obtained fine particles were mixed with purified water to prepare a 40 mass% aqueous dispersion, and this was used as material M.
- the obtained powder When the obtained powder was observed with a scanning electron microscope, it was a spherical fine particle, and polyether ester fine particles having a number average particle size of 4.3 ⁇ m, a volume average particle size of 5.4 ⁇ m, and a particle size distribution index of 1.26. Met.
- the obtained fine particles were mixed with purified water to prepare a 40 mass% aqueous dispersion, and this was used as material N.
- the obtained powder When the obtained powder was observed with a scanning electron microscope, it was a spherical fine particle, a polyether ester fine particle having a number average particle size of 12.0 ⁇ m, a volume average particle size of 14.7 ⁇ m, and a particle size distribution index of 1.23. Met. Observation with a scanning electron microscope revealed true spherical fine particles.
- the obtained fine particles were mixed with purified water to prepare a 40 mass% aqueous dispersion, and this was used as material O.
- Example 1 (1) Preparation of coating liquid The raw materials of the coating liquid were prepared in the order of 1) to 4), and the coating liquid was prepared by stirring for 10 minutes with a universal stirrer. 1) Purified water: 67.3 parts by weight 2) Material A-1: 17.1 parts by weight 3) Material B: 0.6 parts by weight 4) Material D: 15.0 parts by weight
- a melt-laminated sheet is formed by extrusion into a sheet form from the inside of the T die die, and the melt-laminated sheet is closely cooled and solidified by an electrostatic application method on a drum maintained at a surface temperature of 25 ° C.
- a film was obtained.
- the film surface in contact with the drum was defined as the back surface, and the surface in contact with the air was defined as the “front” surface.
- the unstretched laminated film is preheated with a roll (preheated roll) group heated to a temperature of 80 ° C., and then stretched 3.5 times using the difference in peripheral speed of the roll in the longitudinal direction, and 25 ° C.
- a uniaxially stretched film was obtained by cooling with a roll group at a temperature of 5 ° C.
- the “front” surface of the uniaxially stretched film was subjected to corona discharge treatment in the air, and the coating layer forming coating solution was applied to the treated surface by a bar coating method using a wire bar.
- FIG. 1 shows a schematic cross section of a laminated film 31 obtained in this example.
- FIG. 2 shows a result of observing a cross section in the vicinity of the organic particles 12 included in the coating layer 22 of the laminated film 31 with an SEM.
- the laminated film 31 includes a base film 21 and a coating layer 22 formed on the surface thereof.
- the coating layer 22 includes the binder resin 11 and the organic particles 12. Since the organic particles 12 are covered with the binder resin 11, the organic particles 12 are not exposed on the surface of the coating layer 22 and are embedded in the binder resin 11.
- Example 2 to 16 Except that the composition of the coating layer-forming coating solution is as shown in Table 1 and the thickness of the coating layer is as shown in Table 2, film formation is performed under the same conditions as in Example 1, and the thickness is 188 ⁇ m. A laminated white film was obtained. Various properties of the film are shown in Table 2. In all cases, the coating appearance was good, and there was little dropout of particles.
- Example 17 PET was vacuum-dried at a temperature of 180 ° C. for 3 hours, then supplied to the extruder A, melt-extruded at a temperature of 280 ° C., and introduced into a T die die. Next, a melt-laminated sheet is formed by extrusion into a sheet form from the inside of the T die die, and the melt-laminated sheet is closely cooled and solidified by an electrostatic application method on a drum maintained at a surface temperature of 25 ° C. A film was obtained. At this time, the film surface in contact with the drum was defined as the back surface, and the surface in contact with the air was defined as the “front” surface.
- the unstretched laminated film was preheated with a roll (preheated roll) group heated to a temperature of 80 ° C., and then stretched 3.0 times using the difference in peripheral speed of the roll in the longitudinal direction, and 25 ° C.
- a uniaxially stretched film was obtained by cooling with a roll group at a temperature of 5 ° C.
- the “front” surface of the uniaxially stretched film was subjected to corona discharge treatment in the air, and the coating layer forming coating solution was applied to the treated surface by a bar coating method using a wire bar.
- the composition of the coating layer forming coating solution was prepared in the same manner as in Example 3.
- the obtained laminated film has a number average particle size of 4.9 ⁇ m, a particle distribution index of 1.10, a particle covering state of A, a surface roughness SRz of 5 ⁇ m, a coating layer thickness d of 400 nm, and SRz / d of 12. 0.5, R / d was 12.3, and the coating appearance was A.
- the laminated film was excellent in light diffusibility.
- Comparative Example 1 Except that the composition of the coating layer-forming coating solution is as shown in Table 1 and the thickness of the coating layer is as shown in Table 2, film formation is performed under the same conditions as in Example 1, and the thickness is 188 ⁇ m. A laminated white film was obtained. Various properties of the film are shown in Table 2. Particles dropped from the film of Comparative Example 1.
- Example 2-3 A film was formed under the same conditions as in Example 1 except that the composition of the coating layer forming coating solution was set as shown in Table 1 and the thickness of the coating layer was set as shown in Table 2. A layer having a thickness of 188 ⁇ m A white film was obtained. Various properties of the film are shown in Table 2. There were places where the applicability was poor and not partially applied.
- the laminated film of the present invention can be suitably used as a reflector by providing a coating layer on a white substrate film, and can be suitably used as a diffusion plate by providing a coating layer on a transparent substrate film. be able to.
- Binder resin 12 Organic particle 21 Base film 22 Coating layer 31 Laminated film
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Abstract
Description
積層フィルムは、基材フィルムと少なくともその一方の表面に設けられたバインダー樹脂および有機粒子を含有する塗布層とからなる。
(2.1)バインダー樹脂
バインダー樹脂は水溶性樹脂からなる。ここでいう水溶性樹脂とは、スルホン酸基、カルボン酸基、水酸基およびそれらの塩から選ばれた少なくとも1種の官能基を含有する樹脂を示す。水溶性樹脂は、好ましくはスルホン酸基、スルホン酸塩基、カルボン酸基、カルボン酸塩基等の官能基を有するモノマーが共重合された樹脂であり、さらに好ましくはカルボン酸基および/またはカルボン酸基塩を有するモノマーが共重合された樹脂である。水溶性であることによって、基材フィルムおよび有機粒子との親和性がよく、表面粗さ(SRz)と塗布厚み(d)との比(SRz/d)が12.5以上であっても有機粒子の脱落が少ない塗布層を形成することができる。また、バインダー樹脂が水溶性樹脂であることにより、バインダー樹脂および有機粒子を水に溶解および分散させた塗液状態にして使用することができる。もちろん、バインダー樹脂と有機粒子を予め別々に水に溶解または分散させたものを任意に混合して使用してもよい。水を用いた塗液を用いることによって、インラインコーティング法において塗布が可能となるため省コストの観点からも好ましい。バインダー樹脂に上記の官能基を有するモノマーを共重合する方法は公知の方法をとることができる。水溶性樹脂はポリエステル樹脂、アクリル樹脂、ポリウレタン樹脂からなる群より選ばれる少なくとも一種から形成されることが好ましく、ポリエステル樹脂またはアクリル樹脂であることがより好ましい。バインダー樹脂は、基材フィルムとの密着性がよく、また透明であることが好ましく、上記樹脂はこれらの特性を満たすことができる。これら水溶性樹脂としては、DIC(株)製の製品名ウォーターゾール(登録商標)や高松油脂(株)のペスレジン等が入手可能である。
有機粒子は、エーテル結合を含む熱可塑性樹脂からなる。エーテル結合を含む熱可塑性樹脂であることによって、有機粒子とバインダー樹脂との親和性を増し脱落を防ぐことができる。熱硬化性樹脂で有機粒子を形成した場合には粒子が脱落する恐れがある。脱落防止機構の詳細は不明であるが、エーテル結合と、バインダー樹脂が有するスルホン酸基、カルボン酸基および水酸基などの親水性の置換基との化学的親和性が良く、強い結合を形成しているためと考えられる。また、有機粒子が熱可塑性樹脂からなることによってバインダー樹脂との界面に中間層を形成し、さらに強固な結合を形成しているためであると考えられる。
NEX-1000)を用いて、シリンダー温度240℃、金型温度50℃の成形条件で成形して得られる、127×12.7×6.4mmの曲げ試験片を測定サンプルとして使用するものとする。曲げ弾性率が上記範囲より小さいと、白色フィルム上に塗布し反射板として液晶ディスプレイに組み込んだ時に白点が生じる場合がある。曲げ弾性率が上記範囲より大きいと、導光板と反射板がこすれ合った時に導光板に傷が生じる場合がある。熱可塑性樹脂の曲げ弾性率を上記範囲内に調整するためには、例えば、上記樹脂に長鎖のポリアルキレングリコールを共重合させることができる。また、デュポン社製の「ハイトレル(HYTREL)」ではハイトレル7247やハイトレル8238がエーテル結合を含有する熱可塑性樹脂として上記範囲内の曲げ弾性率を達成する。
積層フィルムの基材フィルムは特に限定されず、透明であっても不透明であっても良い。透明なフィルムとしてはポリエステルフィルム、ポリオレフィンフィルム、ポリスチレンフィルム、ポリアミドフィルムなどが挙げられるが、成形のしやすさの観点からポリエステルフィルムが好ましく用いられる。また、不透明なフィルムとしては特開平4-239540号公報、特開2004-330727号公報などに例示される白色フィルムや、特開平6-305019号公報などに例示されるポリフェニレンスルフィドフィルムなどが挙げられる。積層フィルムを液晶ディスプレイの反射板として用いる場合は基材フィルムを白色フィルムとすることが好ましい。特にポリエステル樹脂からなる白色フィルムは、成形性およびコストの観点から好ましく用いられる。
塗布層の形成方法としては、二軸延伸後の基材フィルムに塗液を塗布する方法(オフラインコーティング法)のほか、塗液の塗布後にフィルムを延伸して熱処理する方法(インラインコーティング法)がある。塗布層と基材フィルムとの密着性および省コストの観点からは、インラインコーティング法が好ましい。インラインコーティング法としては、未延伸フィルム表面に塗液を塗布した後に二軸方向に延伸する方法、または、一軸延伸フィルム表面に塗液を塗布した後に先の一軸延伸方向と交差する方向(例えば一軸延伸方向と直交する方向)にさらに延伸する方法などが挙げられるが、後者が好ましい。
(5.1)表面粗さ(SRz)および表面粗さと塗布厚み(d)との比(SRz/d)の測定方法
JIS-B-0601(2001)に準じて測定を実施した。測定器としては、小坂研究所製、表面粗さ計(型番:SE3500)を用いた。測定条件は下記の通りである。
・送り速度:0.1mm/s
・Xピッチ:1.00μm
・Yピッチ:5.0μm
・Z測定倍率:20000
・低域カット:0.25mm
また、上記により求めたSRz(単位:μm)および(5.2)により求めたd(単位:nm)から、下記式によりSRz/dを求めた。
(SRz/d)=(SRz(単位:μm))÷(d(単位:nm))×1000
積層フィルムを断面方向にミクロトームにて70~100nmの厚みの切片を切り出し、四酸化ルテニウムで染色した。染色した切片を透過型電子顕微鏡”TEM2010”(日本電子(株)製)を用いて500~10,000倍に拡大観察して撮影した断面写真より、有機粒子の無い部分の塗布層の厚みを計測して求めた。無作為に選んだ10ヶ所で計測を行い、その平均値を塗布層の厚みとした。
粒子の全部を塗膜が被覆している場合:A
粒子の8割以上塗膜が被覆している場合:B
粒子の塗膜による被覆が4割以上の場合:C
粒子の塗膜による被覆が4割未満の場合:D
底面4cm×4cmのSUSブロック(重さ300g)の底面に市販のトレシーMKクロス(登録商標、東レ(株)製)を両面テープで貼り付けた。積層フィルムの塗布面上を、上記SUSブロックを10回滑らせ、削れテストとした。
脱落痕のない場合:A
5点以下の脱落痕がある場合:B
10点以下の脱落痕がある場合:C
30以下の脱落痕がある場合:D
30点より多い脱落痕がある場合:E
走査型電子顕微鏡(日本電子社製走査型電子顕微鏡JSM-6301NF)にて、積層フィルムの表面に設けられた塗布層の粒子を観察し、粒子径を測定した。なお、粒子が真円でない場合には、長径をその粒子径として測定した。また、数平均粒子径R(Dn)および体積平均粒子径(Dv)は、無作為に選んだ100個の粒子について測定した上記粒子径の値から求めた。
粒子径分布指数(PDI)は、下記数式(1)に従い、算出した。
PDI=Dv/Dn ・・・(1)
尚、Dn:数平均粒子径、Dv:体積平均粒子径、PDI:粒子径分布指数とする。
走査型電子顕微鏡(日本電子社製走査型電子顕微鏡JSM-6301NF)にて、粒子を観察し、粒子径を測定した。なお、粒子が真円でない場合には、長径をその粒子径として測定した。また、数平均粒子径R’(Dn)および体積平均粒子径(Dv)は、無作為に選んだ100個の粒子について測定した上記粒子径の値から求めた。
粒子径分布指数(PDI)は、下記数式(1)に従い、算出した。
PDI=Dv/Dn ・・・(1)
尚、Dn:数平均粒子径、Dv:体積平均粒子径、PDI:粒子径分布指数とする。
実施例あるいは比較例にて得られた積層フィルムについて、蛍光灯反射光にて外観観察を行った。評価基準は以下の通りである。
A:塗布ムラ、塗布抜けが観察されない。
B:塗布ムラ、塗布抜けが一部観察されるが、AUO社製LEDディスプレイ(T240HW01)のバックライトユニットに積層フィルムを組み込み画面が水平になるように設置し点灯したときに、ムラが観察されない。
C:塗布ムラ、塗布抜けが観察され、AUO社製LEDディスプレイ(T240HW01)のバックライトユニットに積層フィルムを組み込み画面が水平になるように設置し点灯したときに、ムラがわずかに観察される。
D:塗布ムラ、塗布抜けにより外観が著しく損なわれている。
なお、塗布外観の評価としては、A~Bを良好、Dを不可とした。
AUO社製LEDディスプレイ(T240HW01)のバックライトユニットに積層フィルムを組み込み画面が水平になるように設置し点灯する。所定の重さの重りで画面中央を押さえた時の状態について、以下の基準で評価を行った。
重りなしで白点が発生する場合:F
0.5kgの重りで白点が発生する場合:E
1.0kgの重りで白点が発生する場合:D
1.5kgの重りで白点が発生する場合:C
2.0kgの重りで白点が発生する場合:B
2.0kgの重りで白点が発生しない場合:A
なお、用いたバックライトは、サイドライト型バックライトであり、導光板および光源(LED)を有し、光源が導光板のエッジ部に位置するものである。この白点評価方法においては、例えば図3に白点の評価例を示すように、白点が発生しない場合(図3(A))と白点が発生する場合(図3(B))とを明確に区別できる。
(5.4.1)の数平均粒子径(Dn)(μm)と(5.2)の厚み(d)(nm)から次式により求めた。
R/d=Dn(μm)/d(nm)×1000
積層フィルムの表面を走査型電子顕微鏡(日本電子社製走査型電子顕微鏡JSM-6301NF)にて観察し、250μm×400μmの10視野において粒子の個数を数えその数Nを有機粒子の粒子密度(個/mm2)とした。
積層フィルムから有機粒子を抽出し、127mm×12.7mm×3.2mmのサイズに成形(Molding)し、ASTM-D790-98に準拠して、曲げ弾性率を測定した。
積層フィルムから抽出する方法は、下記のいずれかの方法を用い、有機粒子以外の成分が5重量%以下になるように採取した。
(1)積層フィルム表面の塗布層からエタノール等の溶剤を用いて有機粒子を抽出し、溶媒を乾燥した。
(2)積層フィルム表面から片刃等を用いて有機粒子を削り取り、有機粒子を採取した。
有機粒子を、127mm×12.7mm×3.2mmのサイズに成形(Molding)し、ASTM-D790-98に準拠して、曲げ弾性率を測定した。
積層フィルムの光沢度をデジタル変角光沢度計UGV-5B(スガ試験機(株)製)を用いて、積層フィルムのコーティング層側よりJIS Z-8741(1997)に準じて測定した。なお、測定条件は入射角=85゜、受光角=85゜とした。サンプル数はn=5とし、それぞれの光沢度を測定して、その平均値を算出した。特にサイドライト型のバックライトシステムでは反射フィルムおよび拡散フィルム共に入射角85°の光沢度が低い方が好ましい場合があることから、以下のように、光沢度に基づいて拡散性の評価を行った。
光沢度(85°)が30未満の場合:A
光沢度(85°)が30以上80未満の場合:B
光沢度(85°)が80以上100未満の場合:C
光沢度(85°)が100以上の場合:D
(1)基材フィルムとしての白色フィルム
・PET(ポリエチレンテレフタレート)
酸成分としてテレフタル酸を、グリコール成分としてエチレングリコールを用い、三酸化アンチモン(重合触媒)を得られるポリエステルペレットに対してアンチモン原子換算で300ppmとなるように添加し、重縮合反応を行い、極限粘度0.63dl/gのポリエチレンテレフタレートペレット(PET)を得た。得られたPETのガラス転移温度は80℃であった。
非相溶性成分として、ガラス転移温度が178℃、MVR(260℃/2.16kg)が4.5ml/10minである環状オレフィン樹脂「TOPAS」(登録商標、ポリプラスチックス社製)を用いた。
・ポリエステル系バインダー樹脂(材料A-1)
ペスレジン A-215E(高松油脂(株)製、30重量%溶液:カルボン酸基および水酸基を含有する。)を精製水で希釈し、25重量%溶液を調製した。
テレフタル酸ジメチル28.3重量部、イソフタル酸ジメチル23.3重量部、アジピン酸ジメチル12.7重量部、5-ナトリウムスルホイソフタル酸ジメチル7.5重量部、エチレングリコール37.3重量部、ジエチレングリコール17.5重量部および酢酸マグネシウム0.035重量部、酢酸リチウム0.3重量部を加え、常法に従いエステル交換反応せしめたのち、チタン化合物(触媒A)をTi元素としてポリマーに対し10ppm、ジエチルホスホノ酢酸エチル0.035重量部を添加した。次いで徐々に昇温、減圧にし、最終的に280℃、1mmHg以下で重縮合反応を行い、共重合ポリエステル(スルホン酸基塩(スルホン酸ナトリウム)および水酸基を含有する。)を得た。得られた共重合ポリエステルを蒸留水に溶かし、25重量%溶液とした。
「ノベック」(登録商標)FC-4430(菱江化学(株)製、5重量%溶液)を用いた。
1000mlの耐圧ガラスオートクレーブ(耐圧硝子工業(株)製、ハイパーグラスターTEM-V1000N)の中に、ポリエーテルエステル(“ハイトレル”(登録商標)7247、東レ・デュポン株式会社製、重量平均分子量29,000、曲げ弾性率600MPa)28g、N-メチル-2-ピロリドン(関東化学株式会社製)304.5g、ポリビニルアルコール(和光純薬工業株式会社製、PVA-1500、重量平均分子量29,000:メタノールでの洗浄により、酢酸ナトリウム含量を0.05質量%に低減したもの)17.5gを加え、窒素置換を行った後、180℃に加熱し、ポリマーが溶解するまで4時間攪拌を行った。その後、貧溶媒として350gのイオン交換水を、送液ポンプを経由して、2.92g/分のスピードで滴下した。全量の水を入れ終わった後、攪拌したまま降温させ、得られた懸濁液をろ過し、イオン交換水700gを加えてリスラリー洗浄し、濾別したものを、80℃で10時間真空乾燥させ、白色固体26.5gを得た。この白色固体をレーザー粒度分布計(島津製作所社製、SALD-2100)にて分析した結果、数平均粒子径が4.9μm、体積平均粒子径が5.5μm、粒子径分布指数が1.12のポリエーテルエステル微粒子であった。得られた微粒子を精製水に混合し、40質量%の水分散液を作成しこれを材料Cとした。走査型電子顕微鏡により観察を行ったところ、真球状微粒子であった。このポリエーテルエステルの融点は、218℃であり、このポリエーテルエステルの降温結晶化温度は、157℃であった。
1000mlの耐圧ガラスオートクレーブ(耐圧硝子工業(株)ハイパーグラスターTEM-V1000N)の中に、ポリエーテルエステル(“ハイトレル”(登録商標)7247、東レ・デュポン株式会社製、重量平均分子量29,000、曲げ弾性率600MPa)28g、N-メチル-2-ピロリドン(関東化学株式会社製)308g、ポリビニルアルコール(和光純薬工業株式会社製 PVA-1500、重量平均分子量29,000:メタノールでの洗浄により、酢酸ナトリウム含量を0.05質量%に低減したもの)14gを加え、窒素置換を行った後、180℃に加熱し、ポリマーが溶解するまで4時間攪拌を行った。その後、貧溶媒として350gのイオン交換水を、送液ポンプを経由して、2.92g/分のスピードで滴下した。全量の水を入れ終わった後、攪拌したまま降温させ、得られた懸濁液をろ過し、イオン交換水700gを加えてリスラリー洗浄し、濾別したものを、80℃で10時間真空乾燥させ、白色固体25.5gを得た。レーザー粒度分布計(島津製作所社製、SALD-2100)にて分析した結果、数平均粒子径7.0μm、体積平均粒子径8.6μm、粒子径分布指数1.23のポリエーテルエステル微粒子であった。得られた微粒子を精製水に混合し、40質量%の水分散液を作成しこれを材料Dとした。走査型電子顕微鏡により観察を行ったところ、真球状微粒子であった。このポリエーテルエステルの融点は、218℃であり、このポリエーテルエステルの降温結晶化温度は、157℃であった。
1000mlの耐圧ガラスオートクレーブ(耐圧硝子工業(株)製、ハイパーグラスターTEM-V1000N)の中に、ポリエーテルエステル(“ハイトレル”(登録商標)7247、東レ・デュポン株式会社製、重量平均分子量29,000、曲げ弾性率600MPa)28g、N-メチル-2-ピロリドン(関東化学株式会社製)301g、ポリビニルアルコール(和光純薬工業株式会社製、PVA-1500、重量平均分子量29,000:メタノールでの洗浄により、酢酸ナトリウム含量を0.05質量%に低減したもの)10.5gを加え、窒素置換を行った後、180℃に加熱し、ポリマーが溶解するまで4時間攪拌を行った。その後、貧溶媒として350gのイオン交換水を、送液ポンプを経由して、2.92g/分のスピードで滴下した。全量の水を入れ終わった後、攪拌したまま降温させ、得られた懸濁液をろ過し、イオン交換水700gを加えてリスラリー洗浄し、濾別したものを、80℃で10時間真空乾燥させ、白色固体26.0gを得た。レーザー粒度分布計(島津製作所社製、SALD-2100)にて分析した結果、数平均分子径が9.8μm、体積平均粒子径12.5μm、粒子径分布指数1.28のポリエーテルエステル微粒子であった。得られた微粒子を精製水に混合し、40質量%の水分散液を作成しこれを材料Eとした。走査型電子顕微鏡により観察を行ったところ、真球状微粒子であった。このポリエーテルエステルの融点は、218℃であり、このポリエーテルエステルの降温結晶化温度は、157℃であった。
テクポリマーMBX-8(架橋PMMA粒子、数平均粒子径8μm、体積平均粒子径11.7μm、粒子径分布指数1.46)(積水化成品工業(株)社製)を精製水に混合した40重量%溶液の水分散体を作成しこれを材料Fとした。なお、この材料Fは、粒子内にエーテル結合を含まない。
1000mlの耐圧ガラスオートクレーブ(耐圧硝子工業(株)製、ハイパーグラスターTEM-V1000N)の中に、ポリエーテルエステル(“ハイトレル”(登録商標)8238、デュポン株式会社製、重量平均分子量27,000、曲げ弾性率1100MPa)33.25g、N-メチルー2-ピロリドン299.25g、ポリビニルアルコール(和光純薬工業株式会社製、PVA-1500、重量平均分子量29,000:メタノールでの洗浄により、酢酸ナトリウム含量を0.05質量%に低減したもの)17.5gを加え、窒素置換を行った後、180℃に加熱し、ポリマーが溶解するまで4時間攪拌を行った。その後、貧溶媒として350gのイオン交換水を、送液ポンプを経由して、2.92g/分のスピードで滴下した。全量の水を入れ終わった後、攪拌したまま降温させ、得られた懸濁液をろ過し、イオン交換水700gを加えてリスラリー洗浄し、濾別したものを、80℃で10時間真空乾燥させ、白色固体28.3gを得た。得られた粉体を走査型電子顕微鏡にて観察したところ真球状の微粒子であり、数平均粒子径12.0μm、体積平均粒子径14.7μm、粒子径分布指数1.23のポリエーテルエステル微粒子であった。走査型電子顕微鏡により観察を行ったところ、真球状微粒子であった。このポリエーテルエステルの融点は、224℃であり、このポリエーテルエステルの降温結晶化温度は、161℃であった。得られた粒子を精製水に混合し、40質量%の水分散液を作成しこれを材料Gとした。
ラボプラストミルを用いて、(A1)水溶性多糖類(日本食品化工株式会社製、クラスターデキストリン)、(A2)水溶性可塑化成分
糖アルコール ソルビトール(東和化成工業株式会社製、ソルビット、融点103℃)および(B1)ポリエーテルエステル(“ハイトレル”(登録商標)8238、デュポン株式会社製、重量平均分子量27,000、曲げ弾性率1100MPa)を(A1):(A2):(B1)=55:15:30の比率で混合し、240℃、50rpmで10分間混練し、混練物を得た。さらに得られた混練物を取り出し後、冷却し、10倍(重量)の純水に浸漬することにより、マトリックス成分を溶解した。生成した粒子分散水溶液を、孔径0.45μmの酢酸セルロース製メンブレンフィルターにてろ過し、メンブレンフィルターにより回収された粒子を、再度10倍量の純水に分散させ、30分程度攪拌下で洗浄後、再びろ過した。このような洗浄操作は二回繰り返した。2回洗浄した試料を45℃のオーブン中で一昼夜乾燥させ、微粒子(C1)を得た。
得られた粒子(C1)の数平均粒径は70μmであった。得られた粒子(C1)および前記粒子(材料G)を(C1):(材料G)=2:98の重量比で混ぜ合わせ材料Hを得た。材料Hの粉体を走査型電子顕微鏡にて観察したところ真球状の微粒子であり、数平均粒子径14.2μm、体積平均粒子径64.5μm、粒子径分布指数4.54のポリエーテルエステル微粒子であった。得られた微粒子を精製水に混合し、40質量%の水分散液を作成しこれを材料Hとした。
100mlの4口フラスコの中に、ポリエーテルエステル(“ハイトレル”(登録商標)3046、東レ・デュポン株式会社製、重量平均分子量23,000、曲げ弾性率20MPa)3.5g、有機溶媒としてN-メチル-2-ピロリドン43g、ポリビニルアルコール(日本合成化学工業株式会社製、‘ゴーセノール(登録商標)’ GL-05)3.5gを加え、90℃に加熱し、ポリマーが溶解するまで攪拌を行った。系の温度を80℃に戻した後に、450rpmで攪拌しながら、貧溶媒として50gのイオン交換水を、送液ポンプを経由し、0.41g/分のスピードで滴下を行った。全量の水を入れ終わった後に、30分間攪拌し、得られた懸濁液を、ろ過し、イオン交換水 100gで洗浄し、80℃ 10時間真空乾燥を行い、白色固体3.1gを得た。得られた粉体を走査型電子顕微鏡にて観察したところ真球状の微粒子であり、数平均粒子径13.2μm、体積平均粒子径15.4μm、粒子径分布指数1.17のポリエーテルエステル微粒子であった。走査型電子顕微鏡により観察を行ったところ、真球状微粒子であった。得られた微粒子を精製水に混合し、40質量%の水分散液を作成しこれを材料Iをした。
ラボプラストミルを用いて、(A1)水溶性多糖類(日本食品化工株式会社製、クラスターデキストリン)、(A2)水溶性可塑化成分
糖アルコール ソルビトール(東和化成工業株式会社製、ソルビット、融点103℃)および(B1)ポリエーテルエステル(“ハイトレル”(登録商標)8238、デュポン株式会社製、重量平均分子量27,000、曲げ弾性率1100MPa)を(A1):(A2):(B1)=55:15:30の比率で混合し、240℃、50rpmで10分間混練し、混練物を得た。さらに得られた混練物を取り出し後、冷却し、10倍(重量)の純水に浸漬することにより、マトリックス成分を溶解した。生成した粒子分散水溶液を、孔径0.45μmの酢酸セルロース製メンブレンフィルターにてろ過し、メンブレンフィルターにより回収された粒子を、再度10倍量の純水に分散させ、30分程度攪拌下で洗浄後、再びろ過した。このような洗浄操作は二回繰り返した。2回洗浄した試料を45℃のオーブン中で一昼夜乾燥させ、微粒子(C1)を得た。
得られた粒子(C1)の数平均粒径は70μmであった。得られた粒子(C1)および前記粒子(材料G)を(C1):(材料G)=0.3:99.7の重量比で混ぜ合わせ材料Hを得た。材料Hの粉体を走査型電子顕微鏡にて観察したところ真球状の微粒子であり、数平均粒子径11.4μm、体積平均粒子径34.2μm、粒子径分布指数3.00のポリエーテルエステル微粒子であった。得られた微粒子を精製水に混合し、40質量%の水分散液を作成しこれを材料Jとした。
テレフタル酸48.0部、1,4-ブタンジオール42.0部および重量平均分子量約3000のポリテトラメチレングリコール10.0部を、チタンテトラブトキシド0.01部とモノ-n-ブチル-モノヒドロキシスズオキサイド0.005部をヘリカルリボン型撹拌翼を備えた反応容器に仕込み、190~225℃で3時間加熱して反応水を系外に留出しながらエステル化反応を行なった。反応混合物にテトラ-n-ブチルチタネート0.06部を追添加し、“イルガノックス”1098(チバ・ジャパン(株)製、ヒンダードフェノール系酸化防止剤)0.02部を添加した後、245℃に昇温し、次いで50分かけて系内の圧力を30Paの減圧とし、その条件下で2時間50分重合を行わせて、脂肪族ポリエーテルエステル(D1)を得た。融点は、226℃であり、重量平均分子量は、28,000、曲げ弾性率は1800MPaであった。
1000mlの耐圧ガラスオートクレーブ(耐圧硝子工業(株)製、ハイパーグラスターTEM-V1000N)の中に、ポリエーテルエステル(“ハイトレル”(登録商標)8238、デュポン株式会社製、重量平均分子量27,000、曲げ弾性率1100MPa)14.6g、N-メチルー2-ピロリドン300g、ポリビニルアルコール(和光純薬工業株式会社製、PVA-1500、重量平均分子量29,000:メタノールでの洗浄により、酢酸ナトリウム含量を0.05質量%に低減したもの)17.5gを加え、窒素置換を行った後、180℃に加熱し、ポリマーが溶解するまで4時間攪拌を行った。その後、貧溶媒として350gのイオン交換水を、送液ポンプを経由して、2.92g/分のスピードで滴下した。全量の水を入れ終わった後、攪拌したまま降温させ、得られた懸濁液をろ過し、イオン交換水700gを加えてリスラリー洗浄し、濾別したものを、80℃で10時間真空乾燥させ、白色固体12.4gを得た。得られた粉体を走査型電子顕微鏡にて観察したところ真球状の微粒子であり、数平均粒子径1.5μm、体積平均粒子径1.8μm、粒子径分布指数1.20のポリエーテルエステル微粒子であった。得られた微粒子を精製水に混合し、40質量%の水分散液を作成しこれを材料Lとした。
1000mlの耐圧ガラスオートクレーブ(耐圧硝子工業(株)製、ハイパーグラスターTEM-V1000N)の中に、ポリエーテルエステル(“ハイトレル”(登録商標)8238、デュポン株式会社製、重量平均分子量27,000、曲げ弾性率1100MPa)15.2g、N-メチルー2-ピロリドン300g、ポリビニルアルコール(和光純薬工業株式会社製、PVA-1500、重量平均分子量29,000:メタノールでの洗浄により、酢酸ナトリウム含量を0.05質量%に低減したもの)17.5gを加え、窒素置換を行った後、180℃に加熱し、ポリマーが溶解するまで4時間攪拌を行った。その後、貧溶媒として350gのイオン交換水を、送液ポンプを経由して、2.92g/分のスピードで滴下した。全量の水を入れ終わった後、攪拌したまま降温させ、得られた懸濁液をろ過し、イオン交換水700gを加えてリスラリー洗浄し、濾別したものを、80℃で10時間真空乾燥させ、白色固体12.9gを得た。得られた粉体を走査型電子顕微鏡にて観察したところ真球状の微粒子であり、数平均粒子径2.2μm、体積平均粒子径2.7μm、粒子径分布指数1.23のポリエーテルエステル微粒子であった。得られた微粒子を精製水に混合し、40質量%の水分散液を作成しこれを材料Mとした。
1000mlの耐圧ガラスオートクレーブ(耐圧硝子工業(株)製、ハイパーグラスターTEM-V1000N)の中に、ポリエーテルエステル(“ハイトレル”(登録商標)8238、デュポン株式会社製、重量平均分子量27,000、曲げ弾性率1100MPa)17.5g、N-メチルー2-ピロリドン315g、ポリビニルアルコール(和光純薬工業株式会社製、PVA-1500、重量平均分子量29,000:メタノールでの洗浄により、酢酸ナトリウム含量を0.05質量%に低減したもの)17.5gを加え、窒素置換を行った後、180℃に加熱し、ポリマーが溶解するまで4時間攪拌を行った。その後、貧溶媒として350gのイオン交換水を、送液ポンプを経由して、2.92g/分のスピードで滴下した。全量の水を入れ終わった後、攪拌したまま降温させ、得られた懸濁液をろ過し、イオン交換水700gを加えてリスラリー洗浄し、濾別したものを、80℃で10時間真空乾燥させ、白色固体14.9gを得た。得られた粉体を走査型電子顕微鏡にて観察したところ真球状の微粒子であり、数平均粒子径4.3μm、体積平均粒子径5.4μm、粒子径分布指数1.26のポリエーテルエステル微粒子であった。得られた微粒子を精製水に混合し、40質量%の水分散液を作成しこれを材料Nとした。
テレフタル酸26.7部、1,4-ブタンジオール23.3部および重量平均分子量約3000のポリテトラメチレングリコール50.0部を、チタンテトラブトキシド0.01部とモノ-n-ブチル-モノヒドロキシスズオキサイド0.005部をヘリカルリボン型撹拌翼を備えた反応容器に仕込み、190~225℃で3時間加熱して反応水を系外に留出しながらエステル化反応を行なった。反応混合物にテトラ-n-ブチルチタネート0.06部を追添加し、“イルガノックス”1098(チバ・ジャパン(株)製、ヒンダードフェノール系酸化防止剤)0.02部を添加した後、245℃に昇温し、次いで50分かけて系内の圧力を30Paの減圧とし、その条件下で2時間50分重合を行わせて、脂肪族ポリエーテルエステル(D2)を得た。融点は、210℃であり、重量平均分子量は、28,000、曲げ弾性率は450MPaであった。
(1)塗液の調製
下記材料を、1)から4)の順番にて塗液の原料を調合し、万能攪拌機にて10分間攪拌して塗液を調製した。
1)精製水:67.3重量部
2)材料A-1:17.1重量部
3)材料B: 0.6重量部
4)材料D:15.0重量部
PET80重量部と環状オレフィン共重合体樹脂20重量部との混合物を180℃の温度で3時間真空乾燥した後に押出機Aに供給し、280℃の温度で溶融押出した。また、PET100重量部を180℃の温度で3時間真空乾燥した後に押出機Bに供給し280℃の温度で溶融押出した。それぞれの押出機A、Bからの樹脂を厚み方向にB/A/Bの順に積層するように合流させた後、Tダイ口金に導入した。
塗布層形成塗液の組成を表1に示した条件とし、塗布層の厚みを表2に示した条件とした以外は、実施例1と同様の条件にて製膜を行い、厚さ188μmの積層の白色フィルムを得た。フィルムの各種特性を表2に示す。いずれも塗布外観よく、また粒子の脱落も少なかった。
次いで、Tダイ口金内より、シート状に押出して溶融積層シートを形成し、該溶融積層シートを、表面温度25℃に保たれたドラム上に静電印加法で密着冷却固化させて未延伸積層フィルムを得た。このとき、ドラムに接しているフィルム面を裏面、空気に接している面を「おもて」面とした。続いて、該未延伸積層フィルムを80℃の温度に加熱したロール(予熱ロール)群で予熱した後、長手方向にロールの周速差を利用して、3.0倍延伸を行い、25℃の温度のロール群で冷却して一軸延伸フィルムを得た。
さらに続いて一軸延伸フィルムの「おもて」面に空気中でコロナ放電処理を施し、その処理面に上記塗布層形成塗液をワイヤーバーを用いたバーコート方式にて塗布した。
上記の塗布層形成塗液が塗布された一軸延伸フィルムの両端をクリップで把持しながらテンター内の100℃の予熱ゾーンに導き乾燥後、引き続き連続的に100℃の加熱ゾーンで長手方向に垂直な方向(横方向)に3.5倍延伸した。さらに引き続いて、テンター内の熱処理ゾーンで190℃ の熱処理を施し、さらに190℃で2%横方向に弛緩処理を行った後、次いで均一に徐冷後に巻き取って、厚み188μmの透明フィルム上に、厚み300nmの塗布層が設けられた積層フィルムを得た。上記の塗布層形成塗液の組成は実施例3と同様に調合した。得られた積層フィルムの数平均粒子径は4.9μm、粒子分布指数は1.10、粒子の被覆状態はA、表面粗さSRzは5μm、塗布層の厚みdは400nm、SRz/dは12.5、R/dは12.3であり、塗布外観はAであった。また、積層フィルムは光拡散性に優れていた。
塗布層形成塗液の組成を表1に示した条件とし、塗布層の厚みを表2に示した条件とした以外は、実施例1と同様の条件にて製膜を行い、厚さ188μmの積層白色フィルムを得た。フィルムの各種特性を表2に示す。比較例1のフィルムからは粒子が脱落した。
塗布層形成塗液の組成を表1に示した条件とし、塗布層の厚みを表2に示した条件とした以外は、実施例1と同様の条件で製膜を行い、厚さ188μmの積層白色フィルムを得た。フィルムの各種特性を表2に示す。塗布性が悪く部分的に塗布されていない箇所が存在した。
12 有機粒子
21 基材フィルム
22 塗布層
31 積層フィルム
Claims (13)
- 基材フィルムの表面に有機粒子を含む塗布層が設けられており、該塗布層表面の表面粗さ(SRz)と塗布厚み(d)との比(SRz/d)が12.5以上である積層フィルムであって、前記有機粒子がエーテル結合を含む熱可塑性樹脂からなり、前記塗布層が、スルホン酸基、カルボン酸基および水酸基、ならびにそれらの塩から選ばれた少なくとも1種を含有するバインダー樹脂からなることを特徴とする積層フィルム。
- 基材フィルムの表面に有機粒子を含む塗布層が設けられており、該塗布層表面の粒子の数平均粒子径(R)と塗布厚み(d)との比(R/d)が10.5以上である積層フィルムであって、前記有機粒子がエーテル結合を含む熱可塑性樹脂からなり、前記塗布層が、スルホン酸基、カルボン酸基および水酸基、ならびにそれらの塩から選ばれた少なくとも1種を含有するバインダー樹脂からなることを特徴とする積層フィルム。
- 前記有機粒子が前記バインダー樹脂によって被覆されている、請求項1または2に記載の積層フィルム。
- 前記表面粗さ(SRz)が5μm以上である、請求項1~3のいずれかに記載の積層フィルム。
- 前記塗布厚み(d)が1100nm以下である、請求項1~4のいずれかに記載の積層フィルム。
- 前記有機粒子の曲げ弾性率が500MPa~3000MPaである、請求項1~5のいずれかに記載の積層フィルム。
- 前記有機粒子の粒子径分布指数が1~3である、請求項1~6のいずれかに記載の積層フィルム。
- 前記塗布層表面における、前記有機粒子の粒子密度が5個/mm2~100000個/mm2である、請求項1~7のいずれかに記載の積層フィルム。
- 前記基材フィルムが白色フィルムからなる、請求項1~8のいずれかに記載の積層フィルム。
- 請求項1~9のいずれかに記載の積層フィルムを製造する方法であって、一軸延伸フィルムからなる基材フィルムの表面に、有機粒子と、スルホン酸基、カルボン酸基および水酸基、ならびにそれらの塩から選ばれた少なくとも1種を含有するバインダー樹脂とを含む塗液を塗布した後に、該塗液が塗布された基材フィルムを、前記基材フィルムの一軸延伸方向と交差する方向にさらに延伸し、熱処理することを特徴とする積層フィルムの製造方法。
- 前記塗液に含まれる有機粒子の平均粒径R’が5μm以上である、請求項10に記載の積層フィルムの製造方法。
- 前記塗液に含まれる有機粒子の粒子径分布指数が1~3である、請求項10または11に記載の積層フィルム。
- 前記塗液に含まれる有機粒子の曲げ弾性率が500MPa~3000MPaである、請求項10~12のいずれかに記載の積層フィルム。
Priority Applications (5)
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| US14/005,660 US20140004305A1 (en) | 2011-03-18 | 2012-03-14 | Laminated film and method for manufacturing same |
| KR1020137023736A KR101922458B1 (ko) | 2011-03-18 | 2012-03-14 | 적층 필름 및 그 제조 방법 |
| JP2012517978A JP5915524B2 (ja) | 2011-03-18 | 2012-03-14 | 積層フィルムおよびその製造方法 |
| CN201280014285.3A CN103443174B (zh) | 2011-03-18 | 2012-03-14 | 层合膜及其制造方法 |
| EP12761406.3A EP2687558A4 (en) | 2011-03-18 | 2012-03-14 | COATING FILM AND METHOD FOR THE PRODUCTION THEREOF |
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| JP2011-060298 | 2011-03-18 | ||
| JP2011060298 | 2011-03-18 | ||
| JP2011-210279 | 2011-09-27 | ||
| JP2011210279 | 2011-09-27 |
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| WO2012128136A1 true WO2012128136A1 (ja) | 2012-09-27 |
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| US (1) | US20140004305A1 (ja) |
| EP (1) | EP2687558A4 (ja) |
| JP (1) | JP5915524B2 (ja) |
| KR (1) | KR101922458B1 (ja) |
| CN (1) | CN103443174B (ja) |
| MY (1) | MY177968A (ja) |
| TW (1) | TWI538814B (ja) |
| WO (1) | WO2012128136A1 (ja) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015106029A (ja) * | 2013-11-29 | 2015-06-08 | 帝人デュポンフィルム株式会社 | 白色反射フィルム |
| KR102004088B1 (ko) * | 2018-03-06 | 2019-07-25 | 도레이첨단소재 주식회사 | 백색 폴리에스테르 반사필름 및 이를 이용한 반사 시트 및 이의 제조방법 |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106133560B (zh) * | 2014-03-27 | 2019-11-19 | 东丽株式会社 | 层叠膜 |
| KR20170039618A (ko) * | 2014-07-31 | 2017-04-11 | 도레이 카부시키가이샤 | 폴리에스테르 필름 |
| WO2019172384A1 (ja) * | 2018-03-07 | 2019-09-12 | 凸版印刷株式会社 | 光学フィルム、光学バリアフィルム、及びバックライトユニット |
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| KR102004088B1 (ko) * | 2018-03-06 | 2019-07-25 | 도레이첨단소재 주식회사 | 백색 폴리에스테르 반사필름 및 이를 이용한 반사 시트 및 이의 제조방법 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103443174B (zh) | 2015-05-13 |
| EP2687558A4 (en) | 2014-11-19 |
| JP5915524B2 (ja) | 2016-05-11 |
| TWI538814B (zh) | 2016-06-21 |
| KR101922458B1 (ko) | 2018-11-27 |
| US20140004305A1 (en) | 2014-01-02 |
| CN103443174A (zh) | 2013-12-11 |
| JPWO2012128136A1 (ja) | 2014-07-24 |
| TW201302482A (zh) | 2013-01-16 |
| KR20140050588A (ko) | 2014-04-29 |
| MY177968A (en) | 2020-09-28 |
| EP2687558A1 (en) | 2014-01-22 |
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