WO2015115359A1 - Film maître permettant la production de film optique - Google Patents

Film maître permettant la production de film optique Download PDF

Info

Publication number
WO2015115359A1
WO2015115359A1 PCT/JP2015/052002 JP2015052002W WO2015115359A1 WO 2015115359 A1 WO2015115359 A1 WO 2015115359A1 JP 2015052002 W JP2015052002 W JP 2015052002W WO 2015115359 A1 WO2015115359 A1 WO 2015115359A1
Authority
WO
WIPO (PCT)
Prior art keywords
film
producing
optical film
optical
raw
Prior art date
Application number
PCT/JP2015/052002
Other languages
English (en)
Japanese (ja)
Inventor
勝啓 高藤
磯▲ざき▼　孝徳
加藤　雅己
Original Assignee
株式会社クラレ
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 株式会社クラレ filed Critical 株式会社クラレ
Priority to JP2015527725A priority Critical patent/JP6408989B2/ja
Priority to CN201580006076.8A priority patent/CN105917256B/zh
Priority to KR1020167018581A priority patent/KR102232980B1/ko
Publication of WO2015115359A1 publication Critical patent/WO2015115359A1/fr

Links

Classifications

    • G—PHYSICS
    • G02—OPTICS
    • G02B—OPTICAL ELEMENTS, SYSTEMS OR APPARATUS
    • G02B5/00—Optical elements other than lenses
    • G02B5/30—Polarising elements
    • 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
    • B29C55/04—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets uniaxial, e.g. oblique
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F216/00—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
    • C08F216/02—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 by an alcohol radical
    • C08F216/04—Acyclic compounds
    • C08F216/06—Polyvinyl alcohol ; Vinyl alcohol
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F218/00—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 acyloxy radical of a saturated carboxylic acid, of carbonic acid or of a haloformic acid
    • C08F218/02—Esters of monocarboxylic acids
    • C08F218/04—Vinyl esters
    • C08F218/08—Vinyl acetate
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00—Chemical modification by after-treatment
    • C08F8/12—Hydrolysis
    • 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
    • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18—Manufacture of films or sheets
    • G—PHYSICS
    • G02—OPTICS
    • G02B—OPTICAL ELEMENTS, SYSTEMS OR APPARATUS
    • G02B5/00—Optical elements other than lenses
    • G02B5/30—Polarising elements
    • G02B5/3025—Polarisers, i.e. arrangements capable of producing a definite output polarisation state from an unpolarised input state
    • G02B5/3033—Polarisers, i.e. arrangements capable of producing a definite output polarisation state from an unpolarised input state in the form of a thin sheet or foil, e.g. Polaroid
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2800/00—Copolymer characterised by the proportions of the comonomers expressed
    • C08F2800/10—Copolymer characterised by the proportions of the comonomers expressed as molar percentages
    • 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
    • C08J2300/00—Characterised by the use of unspecified polymers
    • C08J2300/10—Polymers characterised by the presence of specified groups, e.g. terminal or pendant functional groups
    • C08J2300/104—Polymers characterised by the presence of specified groups, e.g. terminal or pendant functional groups containing oxygen atoms
    • 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

Definitions

  • the present invention relates to a raw film for producing an optical film such as a polarizing film containing a specific hydroxymethyl group-containing vinyl alcohol polymer and a method for producing an optical film using the same.
  • a polarizing plate having a light transmission and shielding function is a basic component of a liquid crystal display (LCD) together with a liquid crystal that changes a polarization state of light.
  • LCD liquid crystal display
  • Many polarizing plates have a structure in which a protective film such as a cellulose triacetate (TAC) film is bonded to the surface of a polarizing film.
  • TAC cellulose triacetate
  • a polarizing film a vinyl alcohol polymer film (hereinafter referred to as “vinyl alcohol-based heavy film”) is used.
  • iodine based dye coalescing the may be referred to as" PVA ) in a matrix formed by uniaxial stretching (I 3 - and I 5 -, etc.) or a dichroic dye such as dichroic organic dyes which are adsorbed Has become the mainstream.
  • LCDs have come to be used in a wide range of small devices such as calculators and watches, mobile phones, notebook computers, liquid crystal monitors, liquid crystal color projectors, liquid crystal televisions, in-vehicle navigation systems, and measurement devices used indoors and outdoors.
  • polarizing film there has been a demand for higher display quality.
  • high performance is also demanded for the polarizing film, and specifically, there is a demand for a polarizing film that has a high degree of polarization and transparency, excellent optical properties, and excellent hue.
  • high durability is also required for the polarizing film.
  • a polyvinyl alcohol film for a polarizing film made of a specific PVA containing 0.01 to 1 mol% of a hydrophilic functional group such as a carboxylic acid group or an ⁇ -hydroxy- ⁇ -olefin group is stretched and oriented. It is known that the processability and the adsorption processability of the dichroic substance are excellent (see Patent Document 1). In addition, it is known that a specific optical PVA film containing PVA containing a 1,2-glycol bond in the side chain is excellent in optical properties and stretchability (see Patent Document 2).
  • the present invention provides a raw film for producing an optical film that can easily produce an optical film with low shrinkage stress that is excellent in all of optical properties, hue, and durability, and a method for producing an optical film using the same.
  • the purpose is to provide.
  • a raw film for producing an optical film comprising a hydroxymethyl group-containing PVA having a structural unit content represented by the following formula (1) of 0.1 to 1.9 mol%;
  • R 1 represents an alkyl group having 1 to 3 carbon atoms.
  • [2] The raw film for producing an optical film according to [1], wherein the degree of polymerization of the hydroxymethyl group-containing PVA exceeds 2,000; [3] The raw film for producing an optical film according to [1] or [2], wherein the saponification degree of the hydroxymethyl group-containing PVA is 95 mol% or more; [4] The raw film for producing an optical film according to any one of [1] to [3], wherein the 1,2-glycol bond amount of the hydroxymethyl group-containing PVA is 1.5 mol% or less; [5] The raw film for producing an optical film according to any one of [1] to [4], wherein R 1 of the structural unit represented by the formula (1) is a methyl group; [6] The raw film for producing an optical film according to any one of [1] to [5], having a thickness of 60 ⁇ m or less; [7] The original film for producing an optical film according to any one of [1] to [1
  • the raw film for optical film manufacture which can manufacture easily the optical film with the low shrinkage stress which is excellent in all of an optical characteristic, a hue, and durability, and the manufacturing method of an optical film using the same Is provided.
  • the raw film for producing an optical film of the present invention contains a hydroxymethyl group-containing PVA in which the content of the structural unit represented by the following formula (1) is 0.1 to 1.9 mol%.
  • R 1 represents an alkyl group having 1 to 3 carbon atoms.
  • the raw film for producing an optical film of the present invention includes any one of optical properties, hues, and durability because the hydroxymethyl group-containing PVA contained therein contains the structural unit represented by the above formula (1) with a specific content. In addition, it is possible to easily produce an optical film having a low shrinkage stress.
  • the present invention is not limited in any way, the reason why the above-described advantages are obtained is that there is an influence of the crystallinity reduction based on the methylene group of the hydroxymethyl group in the structural unit represented by the formula (1), and the hydroxy group. This may be due to the high hydrogen bonding force based on the hydroxyl group of the methyl group.
  • R 1 represents an alkyl group having 1 to 3 carbon atoms.
  • the alkyl group having 1 to 3 carbon atoms include a methyl group, an ethyl group, an n-propyl group, and an isopropyl group.
  • R 1 is preferably a methyl group or an ethyl group, preferably a methyl group, since the hue of the optical film produced therefrom is improved as the crystallinity of the resulting optical film for producing an optical film decreases. Is particularly preferred.
  • the content of the structural unit represented by the formula (1) in the hydroxymethyl group-containing PVA is 0.1 to 1.9 mol%, where the number of moles of all the structural units constituting the hydroxymethyl group-containing PVA is 100 mol%. It is necessary to be within the range, and the content is preferably 0.2 mol% or more, more preferably 0.3 mol% or more, and further preferably 0.4 mol% or more. Preferably, it is preferably 1.8 mol% or less, more preferably 1.7 mol% or less, for example, 1.2 mol% or less, or 1.1 mol% or less.
  • the hue of the optical film manufactured from the raw film for optical film manufacture obtained by the said content rate being 0.1 mol% or more improves.
  • the structural unit refers to a repeating unit constituting a polymer.
  • the degree of polymerization degree of hydroxymethyl group containing PVA preferably exceeds 2,000, more preferably exceeds 2,100, and more preferably exceeds 2,200.
  • the upper limit of the degree of polymerization is not particularly limited, but the degree of polymerization is preferably 6,000 or less from the viewpoints of production cost and process passability during film formation.
  • the polymerization degree of the hydroxymethyl group-containing PVA in the present specification means an average polymerization degree measured according to the description of JIS K6726-1994.
  • the degree of saponification of the hydroxymethyl group-containing PVA is preferably 95 mol% or more, preferably 96 mol% or more, from the viewpoint of the water resistance of an optical film such as a polarizing film produced from the resulting optical film production raw film. More preferably, it is 98 mol% or more, for example, it may be 99 mol% or more, 99.7 mol% or more, or 99.8 mol% or more.
  • the degree of saponification of hydroxymethyl group-containing PVA is a structural unit (typical) of hydroxymethyl group-containing PVA that can be converted into vinyl alcohol units (—CH 2 —CH (OH) —) by saponification.
  • the degree of saponification can be measured according to the description of JIS K6726-1994, taking into consideration the amount of the structural unit represented by formula (1) and its derivatives.
  • the method for producing the hydroxymethyl group-containing PVA is not particularly limited.
  • a vinyl ester copolymer obtained by copolymerizing a vinyl ester monomer and an unsaturated monomer copolymerizable therewith and convertible to the structural unit represented by the formula (1) A method of converting a vinyl ester unit of the above into a vinyl alcohol unit, and further converting a structural unit derived from an unsaturated monomer that can be converted into a structural unit represented by the formula (1) into a structural unit represented by the formula (1) Is mentioned.
  • a specific example of the unsaturated monomer that can be converted into the structural unit represented by the formula (1) is shown in the following formula (2).
  • R 1 represents an alkyl group having 1 to 3 carbon atoms
  • R 2 represents an alkyl group having 1 to 10 carbon atoms.
  • R 2 is not particularly limited, and may be a linear alkyl group, or may partially have a branched or cyclic structure. Moreover, a part may be substituted with other functional groups.
  • R 2 is preferably an alkyl group having 1 to 5 carbon atoms. Examples of the alkyl group include a methyl group, an ethyl group, an n-propyl group, an isopropyl group, an n-butyl group, an isobutyl group, and a tert-butyl group. And a linear or branched alkyl group such as a pentyl group.
  • Examples of the unsaturated monomer represented by the formula (2) include 2-methyl-2-propenyl acetate (methallyl acetate), 2-ethyl-2-propenyl acetate and the like. Of these, 2-methyl-2-propenyl acetate (methallyl acetate) is preferably used in terms of safety and ease of production.
  • the vinyl ester monomer used for the production of the hydroxymethyl group-containing PVA is not particularly limited.
  • vinyl acidate, vinyl caprylate, vinyl caprate, vinyl laurate, vinyl palmitate, vinyl stearate, vinyl oleate, and vinyl benzoate from the economical viewpoint, vinyl acetate is preferred.
  • the polymerization method for copolymerizing the unsaturated monomer represented by formula (2) and the vinyl ester monomer may be any method such as batch polymerization, semi-batch polymerization, continuous polymerization, and semi-continuous polymerization.
  • the polymerization method known methods such as a bulk polymerization method, a solution polymerization method, a suspension polymerization method, and an emulsion polymerization method can be applied.
  • a bulk polymerization method or a solution polymerization method in which polymerization proceeds in a solvent-free or solvent such as alcohol is usually employed.
  • an emulsion polymerization method is also preferred.
  • the solvent of the solution polymerization method is not particularly limited, for example, alcohol.
  • the alcohol used as the solvent for the solution polymerization method is, for example, a lower alcohol such as methanol, ethanol, or propanol.
  • the amount of solvent used in the polymerization system may be selected in consideration of the chain transfer of the solvent in accordance with the degree of polymerization of the target hydroxymethyl group-containing PVA. For example, when the solvent is methanol, it is included in the solvent and the polymerization system.
  • the polymerization initiator used for copolymerization of the unsaturated monomer represented by the formula (2) and the vinyl ester monomer is a known polymerization initiator such as an azo initiator or a peroxide initiator.
  • the redox initiator may be selected according to the polymerization method.
  • Examples of the azo initiator include 2,2′-azobisisobutyronitrile, 2,2′-azobis (2,4-dimethylvaleronitrile), 2,2′-azobis (4-methoxy-2,4- Dimethylvaleronitrile).
  • peroxide initiator examples include percarbonate compounds such as diisopropyl peroxydicarbonate, di-2-ethylhexyl peroxydicarbonate, and diethoxyethyl peroxydicarbonate; t-butyl peroxyneodecanate, ⁇ - Perester compounds such as cumylperoxyneodecanate; acetylcyclohexylsulfonyl peroxide; 2,4,4-trimethylpentyl-2-peroxyphenoxyacetate; acetyl peroxide. Potassium persulfate, ammonium persulfate, hydrogen peroxide, or the like may be combined with the above initiator to form a polymerization initiator.
  • percarbonate compounds such as diisopropyl peroxydicarbonate, di-2-ethylhexyl peroxydicarbonate, and diethoxyethyl peroxydicarbonate
  • the redox initiator is, for example, a polymerization initiator in which the peroxide initiator is combined with a reducing agent such as sodium hydrogen sulfite, sodium hydrogen carbonate, tartaric acid, L-ascorbic acid, or longalite.
  • a reducing agent such as sodium hydrogen sulfite, sodium hydrogen carbonate, tartaric acid, L-ascorbic acid, or longalite.
  • the amount of the polymerization initiator used varies depending on the type of the polymerization initiator and cannot be determined unconditionally, but may be selected according to the polymerization rate. For example, when 2,2′-azobisisobutyronitrile or acetyl peroxide is used as the polymerization initiator, 0.01 to 0.2 mol% is preferable with respect to the vinyl ester monomer, and 0.02 to 0 More preferred is 15 mol%.
  • the copolymerization of the unsaturated monomer represented by the formula (2) and the vinyl ester monomer may be performed in the presence of a chain transfer agent.
  • the chain transfer agent include aldehydes such as acetaldehyde and propionaldehyde; ketones such as acetone and methyl ethyl ketone; mercaptans such as 2-hydroxyethanethiol; and phosphinic acid salts such as sodium phosphinate monohydrate. Of these, aldehydes and ketones are preferably used.
  • the amount of chain transfer agent used can be determined according to the chain transfer coefficient of the chain transfer agent to be used and the degree of polymerization of the target hydroxymethyl group-containing PVA. The amount is preferably 0.1 to 10 parts by mass.
  • the above hydroxymethyl group-containing PVA can be obtained by saponifying a vinyl ester copolymer obtained by copolymerization of an unsaturated monomer represented by formula (2) and a vinyl ester monomer. .
  • the vinyl ester unit in the vinyl ester copolymer is converted to a vinyl alcohol unit.
  • the ester bond of the structural unit derived from the unsaturated monomer represented by the formula (2) is also saponified and converted to the structural unit represented by the formula (1). Therefore, the hydroxymethyl group-containing PVA can be produced without further reaction such as hydrolysis after saponification.
  • the saponification of the vinyl ester copolymer can be performed in a state where the vinyl ester copolymer is dissolved in, for example, alcohol or hydrous alcohol.
  • the alcohol used for saponification include lower alcohols such as methanol and ethanol, preferably methanol.
  • the alcohol used for saponification may contain other solvents such as acetone, methyl acetate, ethyl acetate, and benzene at a ratio of 40% by mass or less of the mass, for example.
  • the catalyst used for saponification is, for example, an alkali metal hydroxide such as potassium hydroxide or sodium hydroxide, an alkali catalyst such as sodium methylate, or an acid catalyst such as mineral acid.
  • the temperature at which saponification is performed is not limited, but is preferably within the range of 20 to 60 ° C.
  • the product is pulverized, washed and dried to obtain a hydroxymethyl group-containing PVA.
  • the saponification method is not limited to the method described above, and a known method can be applied.
  • the hydroxymethyl group-containing PVA can further include other structural units other than the structural unit represented by the formula (1), the vinyl alcohol unit, and the vinyl ester unit.
  • the other structural unit include a structural unit derived from an ethylenically unsaturated monomer copolymerizable with a vinyl ester monomer.
  • the proportion of the total of the structural unit represented by the formula (1), the vinyl alcohol unit and the vinyl ester unit is 100 mol% of the number of moles of all the structural units constituting the hydroxymethyl group-containing PVA. 80 mol% or more, preferably 90 mol% or more, more preferably 95 mol% or more, particularly preferably 99 mol% or more, and 100 mol%. Also good.
  • ethylenically unsaturated monomer examples include ⁇ -olefins such as ethylene, propylene, n-butene, isobutylene and 1-hexene; acrylic acid and salts thereof; unsaturated monomer having an acrylate group.
  • Body methacrylic acid and salts thereof; unsaturated monomer having methacrylic ester group; acrylamide; N-methylacrylamide, N-ethylacrylamide, N, N-dimethylacrylamide, diacetoneacrylamide, acrylamidepropanesulfonic acid and salts thereof Acrylamide derivatives such as acrylamidepropyldimethylamine and salts thereof (for example, quaternary salts); methacrylamide; N-methyl methacrylamide, N-ethyl methacrylamide, methacrylamide propane sulfonic acid and salts thereof, methacrylamide propylene Methacrylamide derivatives such as dimethylamine and its salts (eg quaternary salts); methyl vinyl ether, ethyl vinyl ether, n-propyl vinyl ether, i-propyl vinyl ether, n-butyl vinyl ether, i-butyl vinyl ether, t-butyl vinyl ether, dodecyl vinyl ether , Vinyl
  • the arrangement order of the structural unit represented by the formula (1) in the hydroxymethyl group-containing PVA, the vinyl alcohol unit, and other arbitrary structural units is not particularly limited, and may be any of random, block, alternating, and the like.
  • the 1,2-glycol bond amount of the hydroxymethyl group-containing PVA is preferably 1.5 mol% or less, more preferably 1.4 mol% or less, and 1.2 mol% or less. Further preferred. When the 1,2-glycol bond amount of the hydroxymethyl group-containing PVA is within the above range, the durability of the optical film produced from the resulting optical film production raw film is improved.
  • a hydroxymethyl group-containing PVA having a 1,2-glycol bond content of 1.5 mol% or less is a raw material of a vinyl ester copolymer obtained by polymerizing a vinyl ester monomer at a temperature of 40 ° C. or less. Can be manufactured as.
  • the industrially possible lower limit of the polymerization temperature is about ⁇ 50 ° C.
  • the lower limit of the 1,2-glycol bond amount of the hydroxymethyl group-containing PVA is 0. Often about 5 mol% is the limit.
  • the 1,2-glycol bond amount is the number of moles of bonds between adjacent vinyl alcohol units bonded by 1,2-glycol bonds to the total number of moles of bonds between adjacent vinyl alcohol units.
  • the ratio (mol%) is referred to and can be determined by NMR measurement.
  • the raw film for producing an optical film of the present invention can contain a plasticizer in addition to the hydroxymethyl group-containing PVA.
  • Preferred plasticizers include polyhydric alcohols, and specific examples include ethylene glycol, glycerin, propylene glycol, diethylene glycol, diglycerin, triethylene glycol, tetraethylene glycol, trimethylolpropane, and the like.
  • the raw film for producing an optical film of the present invention can contain one or more of these plasticizers. Among these, glycerin is preferable in terms of the effect of improving stretchability.
  • the plasticizer content in the raw film for producing an optical film of the present invention is preferably in the range of 1 to 20 parts by mass with respect to 100 parts by mass of the hydroxymethyl group-containing PVA contained therein. More preferably, it is within the range of 5 parts by weight, and even more preferably within the range of 5 to 15 parts by weight.
  • the content is 1 part by mass or more, the stretchability of the film is further improved.
  • the content is 20 parts by mass or less, it is possible to prevent the film from becoming too flexible and handling properties from being lowered.
  • the raw film for producing an optical film of the present invention further includes a filler, a processing stabilizer such as a copper compound, a weather resistance stabilizer, a colorant, an ultraviolet absorber, a light stabilizer, an antioxidant, an antistatic agent, Flame retardants, other thermoplastic resins, lubricants, fragrances, defoamers, deodorants, extenders, release agents, mold release agents, reinforcing agents, cross-linking agents, fungicides, preservatives, crystallization rate retarders Additives such as can be blended as needed.
  • a processing stabilizer such as a copper compound, a weather resistance stabilizer, a colorant, an ultraviolet absorber, a light stabilizer, an antioxidant, an antistatic agent, Flame retardants, other thermoplastic resins, lubricants, fragrances, defoamers, deodorants, extenders, release agents, mold release agents, reinforcing agents, cross-linking agents, fungicides, preservatives, crystallization rate retarders
  • the proportion of the total of the hydroxymethyl group-containing PVA and the plasticizer in the raw film for producing an optical film of the present invention is preferably 80% by mass or more based on the mass of the original film for producing an optical film, 90 More preferably, it is more than 95 mass%, and it is still more preferable that it is 95 mass% or more.
  • the degree of swelling of the original film for producing an optical film of the present invention is preferably in the range of 160 to 240%, more preferably in the range of 170 to 230%, and in the range of 180 to 220%. It is particularly preferred.
  • the swelling degree is 160% or more, the film can be stably stretched to a higher magnification.
  • the degree of swelling is 240% or less, dissolution during stretching is suppressed, and stretching is possible even under higher temperature conditions.
  • the degree of swelling of the optical film-producing original film refers to the mass when the optical film-producing original film is immersed in distilled water at 30 ° C. for 30 minutes, and is dried at 105 ° C. for 16 hours after immersion.
  • the degree of swelling can be adjusted, for example, by changing the conditions for heat treatment, and the degree of swelling can usually be lowered by increasing the heat treatment temperature and lengthening the heat treatment time.
  • an optical film having excellent shrinkage stress and excellent optical characteristics, hue and durability can be easily produced. It can be used particularly effectively in a raw film for production.
  • the thickness of the raw film for producing an optical film is preferably 60 ⁇ m or less, more preferably 55 ⁇ m or less, further preferably 50 ⁇ m or less, particularly preferably 40 ⁇ m or less, and 35 ⁇ m or less. Is most preferable, and may be 25 ⁇ m or less, and further 20 ⁇ m or less. When the thickness is too thick, stretch spots tend to occur during uniaxial stretching for producing an optical film.
  • the thickness is preferably 1 ⁇ m or more because there is a tendency that stretching breakage is likely to occur during uniaxial stretching treatment for producing an optical film such as a polarizing film, More preferably, it is 5 ⁇ m or more, and further preferably 10 ⁇ m or more.
  • the width of the original film for producing an optical film of the present invention is not particularly limited, and can be determined according to the use of the produced optical film. In recent years, since the enlargement of screens of liquid crystal televisions and liquid crystal monitors has progressed, it is preferable for these applications to have a width of the original film for producing optical films of 3 m or more. On the other hand, if the width of the raw film for producing an optical film is too large, it is difficult to uniformly carry out uniaxial stretching itself when producing an optical film with an apparatus that has been put into practical use.
  • the width of the anti-film is preferably 7 m or less.
  • the production method of the raw film for producing an optical film of the present invention is not particularly limited, and a production method in which the thickness and width of the film after film formation are more uniform can be preferably employed.
  • Film formation in which one or two or more of the above-mentioned hydroxymethyl group-containing PVA constituting the anti-film and the above-described plasticizer, additive and surfactant described later are dissolved in a liquid medium as necessary.
  • the film-forming stock solution contains at least one of a plasticizer, an additive, and a surfactant, it is preferable that these components are uniformly mixed.
  • liquid medium used for the preparation of the membrane forming stock solution examples include water, dimethyl sulfoxide, dimethylformamide, dimethylacetamide, N-methylpyrrolidone, ethylene glycol, glycerin, propylene glycol, diethylene glycol, triethylene glycol, and tetraethylene glycol. , Trimethylolpropane, ethylenediamine, diethylenetriamine and the like, and one or more of them can be used. Among these, water is preferable from the viewpoint of environmental load and recoverability.
  • the volatile fraction of the film-forming stock solution (content ratio in the film-forming stock solution of volatile components such as liquid media removed by volatilization or evaporation during film formation) varies depending on the film-forming method, film-forming conditions, etc. Specifically, it is preferably in the range of 50 to 95% by mass, more preferably in the range of 55 to 90% by mass, and still more preferably in the range of 60 to 85% by mass.
  • the film-forming stock solution has a volatile content of 50% by mass or more, so that the viscosity of the film-forming stock solution does not become too high, and filtration and defoaming are smoothly performed during the preparation of the film-forming stock solution, and there are few foreign substances and defects. Is easy to manufacture.
  • the volatile fraction of the film-forming stock solution is 95% by mass or less, the concentration of the film-forming stock solution does not become too low, and industrial film production is facilitated.
  • the film forming stock solution preferably contains a surfactant.
  • a surfactant By including the surfactant, the film-forming property is improved and the occurrence of uneven thickness of the film is suppressed, and the film is easily peeled off from the metal roll or belt used for film formation.
  • the film may contain a surfactant.
  • the kind of said surfactant is not specifically limited, From a viewpoint of the peelability from a metal roll or a belt, an anionic surfactant or a nonionic surfactant is preferable.
  • anionic surfactant for example, a carboxylic acid type such as potassium laurate; a sulfuric acid ester type such as polyoxyethylene lauryl ether sulfate and octyl sulfate; and a sulfonic acid type such as dodecylbenzene sulfonate are suitable.
  • a carboxylic acid type such as potassium laurate
  • a sulfuric acid ester type such as polyoxyethylene lauryl ether sulfate and octyl sulfate
  • a sulfonic acid type such as dodecylbenzene sulfonate
  • Nonionic surfactants include, for example, alkyl ether types such as polyoxyethylene oleyl ether; alkylphenyl ether types such as polyoxyethylene octylphenyl ether; alkyl ester types such as polyoxyethylene laurate; polyoxyethylene laurylamino Alkylamine type such as ether; alkylamide type such as polyoxyethylene lauric acid amide; polypropylene glycol ether type such as polyoxyethylene polyoxypropylene ether; alkanolamide type such as lauric acid diethanolamide and oleic acid diethanolamide; polyoxy An allyl phenyl ether type such as alkylene allyl phenyl ether is preferred.
  • surfactants can be used alone or in combination of two or more.
  • the content thereof is preferably in the range of 0.01 to 0.5 parts by weight with respect to 100 parts by weight of the hydroxymethyl group-containing PVA contained in the film-forming stock solution.
  • the content is more preferably in the range of 0.02 to 0.3 parts by mass, and particularly preferably in the range of 0.05 to 0.1 parts by mass.
  • the content is 0.01 mass part or more, film forming property and peelability improve more.
  • the content is 0.5 parts by mass or less, it is possible to suppress that the surfactant bleeds out to the surface of the optical film-producing raw film, resulting in blocking and deterioration in handling properties. it can.
  • Examples of the film forming method for forming an optical film manufacturing raw film using the above film forming stock solution include a cast film forming method, an extrusion film forming method, a wet film forming method, and a gel film forming method. Can be mentioned. These film forming methods may be used alone or in combination of two or more. Among these film forming methods, the cast film forming method and the extrusion film forming method are preferable because a raw film for producing an optical film having a uniform thickness and width and good physical properties can be obtained. The formed film can be dried or heat-treated as necessary.
  • a method for producing a raw film for producing an optical film of the present invention for example, using the T-type slit die, hopper plate, I-die, lip coater die, etc.
  • the film discharged or cast uniformly on the peripheral surface of the rotating heated first roll (or belt) located on the upstream side and discharged or cast on the peripheral surface of the first roll (or belt) Volatile components are evaporated and dried from one side, and then further dried on the peripheral surface of one or more rotating heated rolls arranged downstream thereof, or in a hot air dryer
  • the method of winding with a winding device can be preferably employed industrially. Drying with a heated roll and drying with a hot air dryer may be performed in an appropriate combination.
  • the original film for producing an optical film of the present invention is used as an original film for producing an optical film.
  • Examples of such an optical film include a polarizing film and a retardation film, and a polarizing film is preferable.
  • Such an optical film can be produced, for example, by a method using the raw film for producing an optical film of the present invention, and a method having a uniaxial stretching process. Specifically, the optical film of the present invention is produced.
  • Film or the film derived from the original film for producing an optical film of the present invention hereinafter referred to as “the original film for producing an optical film of the present invention”).
  • the “films derived from the raw film for producing an optical film of the present invention” may be collectively referred to as “films according to the present invention”), and may be produced by a method having a step of uniaxially stretching.
  • the method for producing a polarizing film using the original film for producing an optical film of the present invention is not particularly limited, and any conventionally employed method may be adopted. Examples of such a method include a method in which a film based on the present invention is dyed and uniaxially stretched, or a film based on the present invention containing a dye is uniaxially stretched.
  • the film based on the present invention is subjected to swelling, dyeing, uniaxial stretching, and, if necessary, crosslinking treatment, fixing treatment, drying, heat treatment, etc.
  • a method is mentioned.
  • the order of each treatment such as swelling, dyeing, crosslinking treatment, uniaxial stretching, and fixing treatment is not particularly limited, and one or two or more treatments can be performed simultaneously. Also, one or more of each process can be performed twice or more.
  • Swelling can be performed by immersing the film according to the present invention in water.
  • the temperature of the water when immersed in water is preferably in the range of 20 to 40 ° C., more preferably in the range of 22 to 38 ° C., and preferably in the range of 25 to 35 ° C. Further preferred.
  • the time for immersion in water is preferably in the range of 0.1 to 5 minutes, for example, and more preferably in the range of 0.5 to 3 minutes.
  • the water at the time of immersing in water is not limited to pure water, The aqueous solution in which various components melt
  • Dyeing can be performed by bringing a dichroic dye into contact with the film according to the present invention.
  • the dichroic dye an iodine dye is generally used.
  • the dyeing time may be any stage before uniaxial stretching, during uniaxial stretching, or after uniaxial stretching.
  • Dyeing is generally performed by immersing the PVA film in a solution (particularly an aqueous solution) containing iodine-potassium iodide which is a dyeing bath, and such a dyeing method is also suitably employed in the present invention.
  • the iodine concentration in the dyeing bath is preferably in the range of 0.01 to 0.5% by mass, and the potassium iodide concentration is preferably in the range of 0.01 to 10% by mass.
  • the temperature of the dyeing bath is preferably 20 to 50 ° C., particularly 25 to 40 ° C.
  • the crosslinking treatment is preferably performed after the treatment for bringing the dichroic dye into contact and before the uniaxial stretching.
  • the crosslinking treatment can be performed by immersing the film according to the present invention in an aqueous solution containing a crosslinking agent.
  • a crosslinking agent one or more of boron compounds such as boric acid and borate such as borax can be used.
  • the concentration of the crosslinking agent in the aqueous solution containing the crosslinking agent is preferably in the range of 1 to 15% by mass, more preferably in the range of 2 to 7% by mass, and in the range of 3 to 6% by mass. More preferably. Sufficient stretchability can be maintained when the concentration of the crosslinking agent is in the range of 1 to 15% by mass.
  • the aqueous solution containing a crosslinking agent may contain potassium iodide and the like.
  • the temperature of the aqueous solution containing the crosslinking agent is preferably in the range of 20 to 50 ° C., particularly in the range of 25 to 40 ° C. By setting the temperature within the range of 20 to 50 ° C., crosslinking can be performed efficiently.
  • Uniaxial stretching of the film according to the present invention may be performed by either a wet stretching method or a dry stretching method.
  • the wet stretching method it can be carried out in an aqueous solution containing boric acid, or can be carried out in the dyeing bath described above or in a fixing treatment bath described later.
  • the stretching may be performed at room temperature, may be performed while heating, or may be performed in the air using the film based on the present invention after water absorption.
  • the wet stretching method is preferable because it can be uniformly stretched in the width direction, and uniaxial stretching is more preferable in an aqueous solution containing boric acid.
  • the concentration of boric acid in the boric acid aqueous solution is preferably within the range of 0.5 to 6.0% by mass, more preferably within the range of 1.0 to 5.0% by mass, It is particularly preferably within the range of ⁇ 4.0% by mass.
  • the aqueous boric acid solution may contain potassium iodide, and the concentration of potassium iodide is preferably in the range of 0.01 to 10% by mass.
  • the stretching temperature in the uniaxial stretching is preferably in the range of 30 to 90 ° C, more preferably in the range of 40 to 80 ° C, and particularly preferably in the range of 50 to 70 ° C.
  • the draw ratio in uniaxial stretching is preferably 6.6 times or more, more preferably 6.8 times or more, and 7.0 times or more from the viewpoint of the polarizing performance of the obtained polarizing film. Is particularly preferred.
  • the upper limit of the draw ratio is not particularly limited, but the draw ratio is preferably 8 times or less.
  • uniaxial stretching in the case of uniaxially stretching a long film according to the present invention there is no particular limitation on the direction of uniaxial stretching in the case of uniaxially stretching a long film according to the present invention, and uniaxial stretching or lateral uniaxial stretching in the long direction can be adopted. Since it is obtained, uniaxial stretching in the longitudinal direction is preferable. Uniaxial stretching in the longitudinal direction can be performed by changing the peripheral speed between the rolls using a stretching apparatus including a plurality of rolls parallel to each other. On the other hand, lateral uniaxial stretching can be performed using a tenter type stretching machine.
  • the fixing treatment bath used for the fixing treatment an aqueous solution containing one or more of boron compounds such as boric acid and borax can be used. Moreover, you may add an iodine compound and a metal compound in a fixed treatment bath as needed.
  • the concentration of the boron compound in the fixing treatment bath is generally about 2 to 15% by mass, particularly about 3 to 10% by mass. By setting the concentration within the range of 2 to 15% by mass, the adsorption of the dichroic dye can be further strengthened.
  • the temperature of the fixing treatment bath is preferably 15 to 60 ° C., particularly 25 to 40 ° C.
  • Drying conditions are not particularly limited, but it is preferable to perform the drying at a temperature within the range of 30 to 150 ° C, particularly within the range of 50 to 130 ° C.
  • a polarizing film excellent in dimensional stability can be easily obtained by drying at a temperature in the range of 30 to 150 ° C.
  • the contraction stress of the obtained polarizing film is 3 as the contraction stress in the length direction (stretching direction at the time of manufacturing the polarizing film) in the polarizing film after the humidity control is performed under the conditions of a temperature of 20 ° C. and a relative humidity of 20%. It is preferably 5 N / mm 2 or less. When the shrinkage stress is 3.5 N / mm 2 or less, the polarizing film is less likely to warp the LCD.
  • the shrinkage stress is more preferably 3.2 N / mm 2 or less, still more preferably 3N / mm 2 or less, particularly not less 2.7 N / mm 2 or less preferable.
  • the shrinkage stress for example 1N / mm 2 or more, or even at 2N / mm 2 or more.
  • the shrinkage stress can be measured as follows. That is, a humidity control process is first performed on a polarizing film sample (length 12 cm ⁇ width 1.5 cm) to be measured under conditions of a temperature of 20 ° C. and a relative humidity of 20%. Here, the humidity control process is performed to measure the shrinkage stress. When the humidity control process is not performed, the value of the contraction stress usually increases, but by performing this process, the value of the contraction stress can be decreased and a more accurate value can be obtained. . After performing the humidity control treatment, the length direction of this sample was fixed at 5 cm between chucks, and then stretched in the length direction under conditions of a temperature of 40 ° C. and a relative humidity of 5%, and the tension reached 2N.
  • the stretching is sometimes stopped and held, and in that state, the shrinkage stress (N / mm 2 ) in the length direction when the temperature is raised to 80 ° C. and 4 hours elapses is obtained. More specifically, the shrinkage stress can be measured by the method described later in the examples.
  • the polarizing film obtained as described above is usually used as a polarizing plate by attaching an optically transparent protective film having mechanical strength to both sides or one side.
  • an optically transparent protective film having mechanical strength to both sides or one side.
  • a cellulose triacetate (TAC) film, a cycloolefin polymer (COP) film, an acetic acid / cellulose butyrate (CAB) film, an acrylic film, a polyester film, or the like is used.
  • the adhesive for bonding include PVA adhesives, urethane adhesives, acrylate ultraviolet curable adhesives, and the like.
  • the polarizing plate obtained as described above can be used as an LCD component after being coated with an acrylic adhesive or the like and bonded to a glass substrate. At the same time, it may be bonded to a retardation film, a viewing angle improving film, a brightness improving film, or the like.
  • PVA Primary structure of PVA
  • the width of the width 5 cm ⁇ length 5 cm is uniaxially stretched.
  • a 5 cm ⁇ 8 cm long sample was cut. This sample was uniaxially stretched in the length direction by a factor of 1.5 while being immersed in pure water at 30 ° C. Subsequently, while being immersed in an aqueous solution (dyeing bath) (temperature 30 ° C.) containing 0.03% by mass of iodine and 3.0% by mass of potassium iodide for 60 seconds, the ratio is 1.6 times (2.4 in total). Uniaxially stretching in the length direction to adsorb iodine.
  • the length was 1.1 times (2.6 times in total) while being immersed in an aqueous solution (crosslinking bath) (temperature 30 ° C.) containing 3% by weight of boric acid and 3% by weight of potassium iodide. Uniaxially stretched in the direction. Further, while being immersed in an aqueous solution (stretching bath) containing 4% by mass of boric acid and 6% by mass of potassium iodide, the film is uniaxially stretched in the length direction until it is cut, and the raw film for producing an optical film before stretching.
  • the ratio of the length at the time of cutting with respect to the length of the film was defined as the limit stretch ratio.
  • the temperature of the stretching bath was changed by 1 ° C. from an appropriate temperature, the limiting stretching ratio was measured, and the temperature at which the limiting stretching ratio was the highest was selected.
  • Optical properties of polarizing film (dichroic ratio) (1) Measurement of transmittance Ts From the central part of the polarizing film obtained in the following examples or comparative examples, two 2 cm samples were taken in the length direction of the polarizing film, and a spectrophotometer with an integrating sphere (Japan) Using “V7100” manufactured by Spectroscopic Co., Ltd., in accordance with JIS Z 8722 (measuring method of object color), the visibility of the visible light region of the C light source and 2 ° field of view is corrected.
  • the transmittance Ts (%) and the degree of polarization V (%) were determined by the method described above, and the transmittance Ts (%) was plotted on the horizontal axis and the degree of polarization for each example and comparative example.
  • V (%) as the vertical axis, a total of 5 points including one point based on the transmittance Ts (%) and the degree of polarization V (%) of the polarizing film obtained in each example or comparative example are plotted on a graph.
  • V (%) as the vertical axis
  • a total of 5 points including one point based on the transmittance Ts (%) and the degree of polarization V (%) of the polarizing film obtained in each example or comparative example are plotted on a graph.
  • an approximate curve was obtained, and from the approximate curve, the degree of polarization V 44 (%) when the transmittance Ts (%) was 44% was obtained.
  • the dichroic ratio at a transmittance of 44% was determined by the following formula (6) and used as an index of polarization performance.
  • the higher the dichroic ratio the better the optical properties of the polarizing film.
  • Dichroic ratio when the transmittance 44% log (44 / 100-44 / 100 ⁇ V 44/100) / log (44/100 + 44/100 ⁇ V 44/100) (6)
  • the four polarizing films produced in the above-mentioned “Optical characteristics of the polarizing film (dichroic ratio)” with different amounts of adsorption of the dichroic dye, and each example or comparative example were obtained.
  • the absorbance (orthogonal absorbance) at a wavelength of 610 nm obtained when the transmittance was in the range of 44 to 45% and the transmittance T ⁇ (%) was measured out of the total of five polarizing films obtained.
  • One polarizing film of 2.95 to 3.05 was selected. The polarizing film was exposed for 4 hours in an environment of 60 ° C.
  • the residual rate of orthogonal absorbance (absorbance residual rate) D (%) determined by 7) was evaluated as the durability of the polarizing film. The higher the residual absorbance rate, the better the durability of the polarizing film. When the residual absorbance rate is 33% or more, it is judged as “ ⁇ ” (good), and when it is less than 33%, “x” (bad). It was determined. D (%) 100 ⁇ A 4h / A 0h (7)
  • the film was stretched in the length direction at a speed, and when the tension reached 2N, the stretching was stopped and held, and in that state, the temperature was raised to 80 ° C., and the tension after 4 hours was measured.
  • the contraction stress (contraction stress in the length direction) of the polarizing film was determined.
  • a case where the shrinkage stress was 3.5 N / mm 2 or less was determined as “ ⁇ ” (good), and a case where the shrinkage stress exceeded 3.5 N / mm 2 was determined as “x” (defective).
  • Example 1 100 parts by mass of a hydroxymethyl group-containing PVA shown in Table 1 obtained by saponifying a copolymer of vinyl acetate and 2-methyl-2-propenyl acetate as a modified PVA, 10 parts by mass of glycerin as a plasticizer, And an aqueous solution containing 0.1 part by mass of polyoxyethylene lauryl ether sodium sulfate as a surfactant and having a modified PVA content of 10% by mass as a film-forming stock solution, and drying it on a metal roll at 80 ° C.
  • the degree of swelling was adjusted to 200% by subjecting the obtained film to a heat treatment at a predetermined temperature for 1 minute in a hot air dryer to produce an original film for producing an optical film having a thickness of 30 ⁇ m.
  • the stretchability was evaluated by the above-described method using the obtained optical film for optical film production. The results are shown in Table 1.
  • the length was 1.1 times (2.6 times in total) while being immersed in an aqueous solution (crosslinking bath) (temperature 30 ° C.) containing 3% by weight of boric acid and 3% by weight of potassium iodide. Uniaxially stretched in the direction. Further, an aqueous solution (stretching bath) containing 4% by mass of boric acid and 6% by mass of potassium iodide (a temperature at which the limit stretching ratio determined in the above “stretchability of the raw film for producing optical film” becomes the highest) ) was uniaxially stretched in the length direction to a magnification 0.2 times lower than the limit draw ratio.
  • Example 2 In Example 1, hydroxymethyl group-containing PVA (Examples 2 to 5) shown in Table 1 obtained by saponifying a copolymer of vinyl acetate and 2-methyl-2-propenyl acetate as a modified PVA was used. Except for the above, a raw film for producing an optical film and a polarizing film were produced in the same manner as in Example 1, and each measurement or evaluation was performed. The results are shown in Table 1.
  • Example 1 unmodified PVA shown in Table 1 obtained by saponifying a homopolymer of vinyl acetate instead of modified PVA (Comparative Example 1); vinyl acetate and 2-methyl-2-acetate as modified PVA Hydroxymethyl group-containing PVA shown in Table 1 obtained by saponifying a copolymer with propenyl (Comparative Example 2); As a modified PVA, a copolymer of vinyl acetate and 3,4-diacetoxy-1-butene was used.
  • Modified PVA shown in Table 1 obtained by saponification (Comparative Example 3); Modified PVA shown in Table 1 obtained by saponifying a copolymer of vinyl acetate and itaconic acid as modified PVA (Comparative Example 4) Or modified PVA shown in Table 1 obtained by saponifying a copolymer of vinyl acetate and 7-acetoxy-1-heptene as modified PVA (Reference Example 1) Except for the use respectively, to produce a raw film and polarizing film for an optical film prepared in the same manner as in Example 1 were each measured or evaluated. The results are shown in Table 1.
  • the optical film having a low shrinkage stress which is excellent in all of optical characteristics, hue and durability. It can be seen that can be easily manufactured.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Organic Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Medicinal Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Physics & Mathematics (AREA)
  • Materials Engineering (AREA)
  • Optics & Photonics (AREA)
  • General Physics & Mathematics (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Polarising Elements (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)

Abstract

Le problème décrit par la présente invention est de procurer un film maître permettant la production d'un film optique, qui permet une production facile d'un film optique présentant d'excellentes caractéristiques optiques, teinte et durabilité, tout en ayant une faible contrainte de contraction ; et un procédé de production d'un film optique, qui utilise ce film maître. La solution selon l'invention porte sur un film maître permettant la production d'un film optique, qui contient un polymère d'alcool vinylique contenant des groupes hydroxyméthyle qui contient 0,1 à 1,9 % en mole d'un motif structural représenté par la formule (1) ; et un procédé de production d'un film optique au moyen de ce film maître permettant la production d'un film optique, qui comporte une étape d'étirement uniaxial. (Dans la formule, R1 représente un groupe alkyle ayant 1 à 3 atomes de carbone.)
PCT/JP2015/052002 2014-01-28 2015-01-26 Film maître permettant la production de film optique WO2015115359A1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP2015527725A JP6408989B2 (ja) 2014-01-28 2015-01-26 光学フィルム製造用原反フィルム
CN201580006076.8A CN105917256B (zh) 2014-01-28 2015-01-26 光学膜制造用初始膜
KR1020167018581A KR102232980B1 (ko) 2014-01-28 2015-01-26 광학 필름 제조용 원반 필름

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2014-013054 2014-01-28
JP2014013054 2014-01-28

Publications (1)

Publication Number Publication Date
WO2015115359A1 true WO2015115359A1 (fr) 2015-08-06

Family

ID=53756933

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2015/052002 WO2015115359A1 (fr) 2014-01-28 2015-01-26 Film maître permettant la production de film optique

Country Status (5)

Country Link
JP (1) JP6408989B2 (fr)
KR (1) KR102232980B1 (fr)
CN (1) CN105917256B (fr)
TW (1) TWI648330B (fr)
WO (1) WO2015115359A1 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017038955A1 (fr) * 2015-09-02 2017-03-09 株式会社クラレ Rouleau de film d'alcool polyvinylique
WO2018164196A1 (fr) * 2017-03-08 2018-09-13 株式会社クラレ Film polarisant, lame polarisante, et leur procédé de fabrication
WO2018164176A1 (fr) * 2017-03-08 2018-09-13 株式会社クラレ Film polarisant, plaque polarisante, et son procédé de fabrication
JP2021012385A (ja) * 2016-02-09 2021-02-04 株式会社クラレ 偏光フィルム及びその製造方法

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20200166673A1 (en) * 2017-07-25 2020-05-28 Lg Chem, Ltd Polarizing plate and liquid crystal display device comprising the same
KR102621169B1 (ko) * 2019-01-11 2024-01-05 산진 옵토일렉트로닉스 (난징) 컴퍼니 리미티드 편광판의 제조 방법
CN111732749B (zh) * 2020-08-10 2022-11-11 安徽皖维高新材料股份有限公司 一种聚乙烯醇光学薄膜的制备方法

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03175404A (ja) * 1989-12-05 1991-07-30 Kuraray Co Ltd 偏光フイルムおよびその製造法
JPH1025330A (ja) * 1996-07-10 1998-01-27 Kuraray Co Ltd 配合組成物および接着剤
JPH11323299A (ja) * 1998-05-13 1999-11-26 Kuraray Co Ltd 水性樹脂組成物および接着剤
JP2001288322A (ja) * 2000-04-04 2001-10-16 Unitika Chem Co Ltd ポリビニルアルコール系熱溶融性樹脂組成物
JP2002174726A (ja) * 2000-12-06 2002-06-21 Kuraray Co Ltd 偏光フィルム
JP2008208347A (ja) * 2007-01-31 2008-09-11 Nippon Synthetic Chem Ind Co Ltd:The ポリビニルアルコール系樹脂組成物およびフィルム
WO2015020046A1 (fr) * 2013-08-09 2015-02-12 株式会社クラレ Film polymère à base d'alcool vinylique

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60230606A (ja) * 1984-04-30 1985-11-16 Kuraray Co Ltd 偏光膜
JP2685790B2 (ja) * 1988-03-28 1997-12-03 株式会社クラレ 偏光素子を含む光学系からなる装置
US5070126A (en) * 1988-08-02 1991-12-03 Aicello Chemical Co., Ltd. Films easily soluble in cold water
JPH03232990A (ja) * 1990-02-07 1991-10-16 Kyushu Hitachi Maxell Ltd メッシュの製造方法
JP3497903B2 (ja) 1995-01-23 2004-02-16 株式会社クラレ 偏光膜の原反用ポリビニルアルコールフィルム
JPH11323290A (ja) * 1998-03-03 1999-11-26 Kawasaki Steel Corp ふっ素樹脂接着用接着剤組成物、ふっ素樹脂被覆金属板およびその製造方法
JP5230221B2 (ja) * 2007-04-20 2013-07-10 富士フイルム株式会社 熱可塑性フィルムおよびその製造方法
JP4800269B2 (ja) 2007-07-19 2011-10-26 日本合成化学工業株式会社 偏光膜用ポリビニルアルコール系フィルム、偏光膜、及び偏光板
JP5628025B2 (ja) * 2008-12-18 2014-11-19 株式会社クラレ ポリビニルアルコールフィルム
JP2010243858A (ja) * 2009-04-07 2010-10-28 Nitto Denko Corp 偏光板、液晶パネルおよび液晶表示装置
JP6017773B2 (ja) * 2011-10-31 2016-11-02 株式会社クラレ 偏光フィルムの製造方法

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03175404A (ja) * 1989-12-05 1991-07-30 Kuraray Co Ltd 偏光フイルムおよびその製造法
JPH1025330A (ja) * 1996-07-10 1998-01-27 Kuraray Co Ltd 配合組成物および接着剤
JPH11323299A (ja) * 1998-05-13 1999-11-26 Kuraray Co Ltd 水性樹脂組成物および接着剤
JP2001288322A (ja) * 2000-04-04 2001-10-16 Unitika Chem Co Ltd ポリビニルアルコール系熱溶融性樹脂組成物
JP2002174726A (ja) * 2000-12-06 2002-06-21 Kuraray Co Ltd 偏光フィルム
JP2008208347A (ja) * 2007-01-31 2008-09-11 Nippon Synthetic Chem Ind Co Ltd:The ポリビニルアルコール系樹脂組成物およびフィルム
WO2015020046A1 (fr) * 2013-08-09 2015-02-12 株式会社クラレ Film polymère à base d'alcool vinylique

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017038955A1 (fr) * 2015-09-02 2017-03-09 株式会社クラレ Rouleau de film d'alcool polyvinylique
JPWO2017038955A1 (ja) * 2015-09-02 2018-05-31 株式会社クラレ ポリビニルアルコールフィルムロール
JP2021012385A (ja) * 2016-02-09 2021-02-04 株式会社クラレ 偏光フィルム及びその製造方法
JP7284740B2 (ja) 2016-02-09 2023-05-31 株式会社クラレ 偏光フィルム
WO2018164196A1 (fr) * 2017-03-08 2018-09-13 株式会社クラレ Film polarisant, lame polarisante, et leur procédé de fabrication
WO2018164176A1 (fr) * 2017-03-08 2018-09-13 株式会社クラレ Film polarisant, plaque polarisante, et son procédé de fabrication
JPWO2018164196A1 (ja) * 2017-03-08 2020-01-09 株式会社クラレ 偏光フィルム、偏光板、及びそれらの製造方法
JPWO2018164176A1 (ja) * 2017-03-08 2020-01-09 株式会社クラレ 偏光フィルム、偏光板、及びそれらの製造方法
JP7199343B2 (ja) 2017-03-08 2023-01-05 株式会社クラレ 偏光フィルム、偏光板、及びそれらの製造方法
JP7234105B2 (ja) 2017-03-08 2023-03-07 株式会社クラレ 偏光フィルム、偏光板、及びそれらの製造方法

Also Published As

Publication number Publication date
KR20160113595A (ko) 2016-09-30
CN105917256A (zh) 2016-08-31
TW201538590A (zh) 2015-10-16
JPWO2015115359A1 (ja) 2017-03-23
JP6408989B2 (ja) 2018-10-17
TWI648330B (zh) 2019-01-21
CN105917256B (zh) 2019-01-15
KR102232980B1 (ko) 2021-03-26

Similar Documents

Publication Publication Date Title
JP6420153B2 (ja) ビニルアルコール系重合体フィルム
JP6408989B2 (ja) 光学フィルム製造用原反フィルム
JP6788673B2 (ja) 偏光フィルム及びその製造方法
JP6383664B2 (ja) 光学フィルム製造用原反フィルム
JP2016222834A (ja) ポリビニルアルコールフィルムの製造方法
WO2021070622A1 (fr) Film pour la production d'un film optique, procédé de production d'un film optique, et film optique
JP5931125B2 (ja) 偏光フィルムの製造方法
JP6776129B2 (ja) フィルム
JP6858499B2 (ja) 光学フィルムの製造方法
WO2019146678A1 (fr) Film polarisant et son procédé de fabrication
JP6255300B2 (ja) ポリビニルアルコール樹脂の製造方法
JP6792456B2 (ja) フィルム
WO2022097336A1 (fr) Film de production de film optique, procédé de production d'un film optique, et film optique
JP7093350B2 (ja) 原反フィルム、延伸光学フィルムの製造方法、及び延伸光学フィルム
JP2023056678A (ja) ポリビニルアルコールフィルム、ポリビニルアルコールフィルムの製造方法、延伸フィルム及び偏光フィルム

Legal Events

Date Code Title Description
ENP Entry into the national phase

Ref document number: 2015527725

Country of ref document: JP

Kind code of ref document: A

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 15743066

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 20167018581

Country of ref document: KR

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 15743066

Country of ref document: EP

Kind code of ref document: A1