WO2015030118A1 - (meth)acrylic resin - Google Patents
(meth)acrylic resin Download PDFInfo
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- WO2015030118A1 WO2015030118A1 PCT/JP2014/072587 JP2014072587W WO2015030118A1 WO 2015030118 A1 WO2015030118 A1 WO 2015030118A1 JP 2014072587 W JP2014072587 W JP 2014072587W WO 2015030118 A1 WO2015030118 A1 WO 2015030118A1
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- 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
- C08F8/30—Introducing nitrogen atoms or nitrogen-containing groups
- C08F8/32—Introducing nitrogen atoms or nitrogen-containing groups by reaction with amines
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- 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
- C08F20/00—Homopolymers and 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 a salt, anhydride, ester, amide, imide or nitrile thereof
- C08F20/02—Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
- C08F20/10—Esters
-
- 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
- C08F20/00—Homopolymers and 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 a salt, anhydride, ester, amide, imide or nitrile thereof
- C08F20/02—Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
- C08F20/52—Amides or imides
-
- 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
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- G—PHYSICS
- G02—OPTICS
- G02B—OPTICAL ELEMENTS, SYSTEMS OR APPARATUS
- G02B1/00—Optical elements characterised by the material of which they are made; Optical coatings for optical elements
- G02B1/04—Optical elements characterised by the material of which they are made; Optical coatings for optical elements made of organic materials, e.g. plastics
-
- G—PHYSICS
- G02—OPTICS
- G02B—OPTICAL ELEMENTS, SYSTEMS OR APPARATUS
- G02B1/00—Optical elements characterised by the material of which they are made; Optical coatings for optical elements
- G02B1/10—Optical coatings produced by application to, or surface treatment of, optical elements
- G02B1/12—Optical coatings produced by application to, or surface treatment of, optical elements by surface treatment, e.g. by irradiation
-
- G—PHYSICS
- G02—OPTICS
- G02B—OPTICAL ELEMENTS, SYSTEMS OR APPARATUS
- G02B1/00—Optical elements characterised by the material of which they are made; Optical coatings for optical elements
- G02B1/10—Optical coatings produced by application to, or surface treatment of, optical elements
- G02B1/14—Protective coatings, e.g. hard coatings
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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
- C08J2333/00—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
- C08J2333/04—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
- C08J2333/06—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
- C08J2333/10—Homopolymers or copolymers of methacrylic acid esters
- C08J2333/12—Homopolymers or copolymers of methyl methacrylate
Definitions
- the present invention relates to a (meth) acrylic resin. More specifically, the present invention relates to polarized light used in a polarizing plate provided in an image display device such as a protective film for a substrate of an optical disk such as VD, CD, DVD, MD, and LD, and a liquid crystal display device such as an LCD.
- Optical films represented by optical protective films such as child protective films, antireflection films used in organic EL displays (OLEDs), transparent conductive films formed with transparent conductive layers such as ITO layers, and the like.
- the present invention relates to a mounted image display device and a (meth) acrylic resin that can be suitably used as a raw material for the optical film.
- an optical film made of a cellulose-based resin produces a phase difference with respect to obliquely incident light, and the phase difference with respect to the obliquely incident light adversely affects viewing angle characteristics in a large liquid crystal display.
- polymethyl methacrylate has been conventionally proposed as an optical material having excellent moldability, high surface hardness, high light transmittance, low birefringence, and low wavelength dependency (see, for example, Patent Document 2).
- polymethyl methacrylate has a low glass transition temperature (Tg) of about 100 ° C. and is inferior in heat resistance, it is difficult to use it in applications requiring heat resistance, such as an image display device.
- Tg glass transition temperature
- JP 2009-265174 A Japanese Patent Laid-Open No. 06-102547 JP 2009-107180 A
- the present invention has been made in view of the prior art, and can be suitably used as a raw material for optical films having excellent heat resistance, low birefringence, high surface hardness, and low photoelastic coefficient ( (Meth) acrylic resin, optical film using the (meth) acrylic resin, transparent conductive film using the (meth) acrylic resin and having a transparent conductive layer such as an ITO layer, and the optical It is an object of the present invention to provide an image display device on which a film is mounted.
- R 1 and R 2 are each independently a hydrogen atom or an alkyl group having 1 to 8 carbon atoms, and R 3 represents a ring structure
- (meth) acryl means “acryl” or “methacryl”.
- a (meth) acrylic resin that can be suitably used as a raw material for an optical film having excellent heat resistance, low birefringence, high surface hardness, and low photoelastic coefficient, and the like
- An optical film using an acrylic resin, a transparent conductive film using the (meth) acrylic resin and having a transparent conductive layer such as an ITO layer formed thereon, and an image display device on which the optical film is mounted are provided.
- the (meth) acrylic resin of the present invention has the formula (I):
- R 1 and R 2 are each independently a hydrogen atom or an alkyl group having 1 to 8 carbon atoms, and R 3 represents a ring structure
- R 4 and R 5 are each independently a hydrogen atom or an alkyl group having 1 to 8 carbon atoms
- R 6 is an alkyl group having 1 to 18 carbon atoms or a cycloalkyl group having 3 to 12 carbon atoms
- an aryl group having 6 to 10 carbon atoms It has a repeating unit represented by
- R 1 and R 2 are each independently a hydrogen atom or an alkyl group having 1 to 8 carbon atoms.
- the alkyl group having 1 to 8 carbon atoms include methyl group, ethyl group, n-propyl group, isopropyl group, n-butyl group, isobutyl group, tert-butyl group, n-pentyl group, isopentyl group, n- Examples include a hexyl group, an isohexyl group, an n-heptyl group, an isoheptyl group, an n-octyl group, and a 2-ethylhexyl group, but the present invention is not limited to such examples.
- a hydrogen atom or an alkyl group having 1 to 4 carbon atoms is preferable from the viewpoint of obtaining an optical film having excellent heat resistance and low birefringence.
- R 3 represents a ring structure.
- the ring structure include a cycloalkyl group having 3 to 12 carbon atoms and an aryl group having 6 to 10 carbon atoms.
- the cycloalkyl group having 3 to 12 carbon atoms include a cyclopropyl group, a cyclobutyl group, a cyclopentyl group, a cyclohexyl group, and the like, but the present invention is not limited to such examples.
- cycloalkyl groups a cycloalkyl group having 3 to 6 carbon atoms is preferable and a cyclohexyl group is more preferable from the viewpoint of obtaining an optical film having excellent heat resistance and low birefringence.
- Examples of the aryl group having 6 to 10 carbon atoms include phenyl, benzyl, o-tolyl, m-tolyl, p-tolyl, 2,3-xylyl, 2,4-xylyl, 2,5- Examples include xylyl group, 2,6-xylyl group, 3,4-xylyl group, 3,5-xylyl group, 1-naphthyl group, 2-naphthyl group, binaphthyl group, anthryl group, and the like. It is not limited to illustration only.
- aryl groups a phenyl group and a tolyl group are preferable from the viewpoint of obtaining an optical film having excellent heat resistance and low birefringence.
- R 3 a cycloalkyl group having 3 to 6 carbon atoms, a phenyl group, and a tolyl group are preferable, and a cyclohexyl group and a phenyl group are more preferable from the viewpoint of obtaining an optical film having excellent heat resistance and low birefringence. preferable.
- R 1 and R 2 are each independently a hydrogen atom or an alkyl group having 1 to 4 carbon atoms. , Preferably a hydrogen atom or a methyl group, and it is desirable that R 3 is a cyclohexyl group or a phenyl group, preferably a phenyl group.
- the (meth) acrylic resin may contain two or more types of repeating units represented by the formula (I).
- R 4 and R 5 are each independently a hydrogen atom or an alkyl group having 1 to 8 carbon atoms.
- the alkyl group having 1 to 8 carbon atoms include methyl group, ethyl group, n-propyl group, isopropyl group, n-butyl group, isobutyl group, tert-butyl group, n-pentyl group, isopentyl group, n- Examples include a hexyl group, an isohexyl group, an n-heptyl group, an isoheptyl group, an n-octyl group, and a 2-ethylhexyl group, but the present invention is not limited to such examples.
- an alkyl group having 1 to 4 carbon atoms is preferable from the viewpoint of obtaining an optical film having excellent heat resistance, low birefringence, high surface hardness, and low photoe
- R 6 is an alkyl group having 1 to 18 carbon atoms, a cycloalkyl group having 3 to 12 carbon atoms, or an aryl group having 6 to 10 carbon atoms.
- alkyl group having 1 to 18 carbon atoms include methyl group, ethyl group, n-propyl group, isopropyl group, n-butyl group, isobutyl group, tert-butyl group, pentyl group, hexyl group, heptyl group, octyl group.
- cycloalkyl group having 3 to 12 carbon atoms examples include a cyclopropyl group, a cyclobutyl group, a cyclopentyl group, a cyclohexyl group, and the like, but the present invention is not limited to such examples.
- Examples of the aryl group having 6 to 10 carbon atoms include phenyl, benzyl, o-tolyl, m-tolyl, p-tolyl, 2,3-xylyl, 2,4-xylyl, 2,5- Examples include xylyl group, 2,6-xylyl group, 3,4-xylyl group, 3,5-xylyl group, 1-naphthyl group, 2-naphthyl group, binaphthyl group, anthryl group, and the like. It is not limited to illustration only.
- an alkyl group having 1 to 18 carbon atoms is preferable, and an alkyl group having 1 to 8 carbon atoms is preferable.
- Group is more preferable, an alkyl group having 1 to 4 carbon atoms is more preferable, and a methyl group, an ethyl group, and an n-butyl group are still more preferable.
- R 4 and R 5 are each independently from the viewpoint of obtaining an optical film having excellent heat resistance, low birefringence, high surface hardness, and low photoelastic coefficient.
- a hydrogen atom or an alkyl group having 1 to 8 carbon atoms preferably a hydrogen atom or an alkyl group having 1 to 4 carbon atoms, more preferably a hydrogen atom or a methyl group
- R 6 is an alkyl group having 1 to 18 carbon atoms
- the (meth) acrylic resin may contain two or more types of repeating units represented by the formula (II).
- the content of the repeating unit represented by the formula (I) in the (meth) acrylic resin is preferably from the viewpoint of improving the heat resistance and transparency of the (meth) acrylic resin and obtaining an optical film having a small birefringence.
- the content of the repeating unit represented by the formula (II) in the (meth) acrylic resin is improved from the viewpoint of improving the moldability to the film, increasing the mechanical strength, and obtaining an optical film having a small birefringence.
- it is 15% by weight or more, more preferably 20% by weight or more, and further preferably 25% by weight or more, and an optical film having improved birefringence and improved heat resistance and transparency of the (meth) acrylic resin is obtained.
- it is preferably 95% by weight or less, more preferably 90% by weight or less, and still more preferably 85% by weight or less.
- the (meth) acrylic resin includes, for example, repeating units other than the repeating unit represented by the formula (I) and the repeating unit represented by the formula (II), such as a styrene unit, within the range in which the object of the present invention is not hindered. Units may be included.
- the repeating unit represented by the formula (I) and the repeating unit other than the repeating unit represented by the formula (II) are styrene units
- the content of styrene units in all the repeating units is preferably 10% by weight or less. More preferably, it is 5% by weight or less, more preferably 2% by weight or less, and still more preferably 1% by weight or less.
- the weight average molecular weight of the (meth) acrylic resin is preferably 10,000 or more, more preferably 30000 or more from the viewpoint of increasing the mechanical strength of the film, and preferably 500,000 or less from the viewpoint of improving the moldability to the film. More preferably, it is 300,000 or less.
- the weight average molecular weight of the (meth) acrylic resin is a value obtained by gel permeation chromatography (GPC) under the following conditions.
- the glass transition temperature of the (meth) acrylic resin is preferably 120 ° C. or higher, more preferably 130 ° C. or higher, further preferably 140 ° C. or higher, and even more preferably 150 ° C. or higher. is there.
- the glass transition temperature of the (meth) acrylic resin is preferably 250 ° C. or less, more preferably 230 ° C. or less, further preferably 210 ° C. or less, and still more preferably, from the viewpoint of improving the molding processability to a film. It is 200 degrees C or less.
- the glass transition temperature of the (meth) acrylic resin is a value obtained in accordance with JIS K7121. More specifically, a differential scanning calorimeter [trade name: Thermo plus EVO DSC-8230 manufactured by Rigaku Corporation] was used, and ⁇ -alumina was used as a reference, and about 10 mg of (meth) acrylic resin in a nitrogen gas atmosphere. Is a temperature obtained by raising the temperature from room temperature to 200 ° C. at a rate of temperature rise of 20 ° C./min and obtaining the starting point method from the obtained DSC curve.
- the acid value of the (meth) acrylic resin is preferably 1.4 mmol / g or less, more preferably 0.8 mmol / g or less, and still more preferably 0.8, from the viewpoint of improving molding processability such as film formation. 5 mmol / g or less, still more preferably 0.3 mmol / g or less.
- the acid value of the (meth) acrylic resin is a value when measured based on the method described in the following examples.
- the absolute value of the stress optical coefficient (Cr) of the (meth) acrylic resin is preferably from the viewpoint of suppressing the birefringence by suppressing the anisotropy of the refractive index of the optical film made of the resin, for example, a stretched film. It is 0.3 ⁇ 10 ⁇ 9 Pa ⁇ 1 or less, more preferably 0.2 ⁇ 10 ⁇ 9 Pa ⁇ 1 or less, and further preferably 0.1 ⁇ 10 ⁇ 9 Pa ⁇ 1 or less.
- the stress optical coefficient (Cr) of the (meth) acrylic resin is a value when measured based on the method described in the following examples.
- the thickness direction retardation Rth of the optical film after biaxial stretching can be 20 nm or less.
- the (meth) acrylic resin can be obtained, for example, by imidizing a (meth) acrylic resin having a repeating unit represented by the formula (II) with an imidizing agent.
- the (meth) acrylic resin (hereinafter simply referred to as “(meth) acrylic resin”) having a repeating unit represented by the formula (II) is, for example, the formula (III):
- the monomer represented by the formula (III) may contain other monomers as long as the object of the present invention is not inhibited.
- (meth) acrylic acid is used as the other monomer
- (meth) acrylic acid is contained in the monomer represented by formula (III) at a content of 45% by weight or less, preferably 40% by weight or less. Can do.
- Examples of the monomer represented by the formula (III) include alkyl (meth) acrylates having 1 to 18 carbon atoms in the alkyl group, cycloalkyl (meth) acrylates having 3 to 12 carbon atoms in the cycloalkyl group, and carbon numbers in the aryl group. 6 to 10 aryl (meth) acrylates. These (meth) acrylates may be used alone or in combination of two or more.
- alkyl (meth) acrylate having an alkyl group having 1 to 18 carbon atoms examples include methyl (meth) acrylate, ethyl (meth) acrylate, n-propyl (meth) acrylate, isopropyl (meth) acrylate, n-butyl ( (Meth) acrylate, isobutyl (meth) acrylate, tert-butyl (meth) acrylate, pentyl (meth) acrylate, hexyl (meth) acrylate, heptyl (meth) acrylate, octyl (meth) acrylate, decyl (meth) acrylate, dodecyl ( Examples include meth) acrylate, tetradecyl (meth) acrylate, pentadecyl (meth) acrylate, hexadecyl (meth) acrylate, heptadecyl (
- the present invention is not limited only to those exemplified.
- Examples of the cycloalkyl (meth) acrylate having 3 to 12 carbon atoms in the cycloalkyl group include cyclopropyl (meth) acrylate, cyclobutyl (meth) acrylate, cyclopentyl (meth) acrylate, cyclohexyl (meth) acrylate, and the like.
- the present invention is not limited to such examples.
- Examples of the aryl (meth) acrylate having 6 to 10 carbon atoms in the aryl group include phenyl (meth) acrylate, benzyl (meth) acrylate, o-tolyl (meth) acrylate, m-tolyl (meth) acrylate, p- Tolyl (meth) acrylate, 2,3-xylyl (meth) acrylate, 2,4-xylyl (meth) acrylate, 2,5-xylyl (meth) acrylate, 2,6-xylyl (meth) acrylate, 3,4- Examples include xylyl (meth) acrylate, 3,5-xylyl (meth) acrylate, 1-naphthyl (meth) acrylate, 2-naphthyl (meth) acrylate, binaphthyl (meth) acrylate, anthryl (meth) acrylate, etc. The invention is not limited to such examples
- Examples of the method for polymerizing the monomer represented by the formula (III) include a bulk polymerization method, a solution polymerization method, an emulsion polymerization method, a suspension polymerization method, and the like, but the present invention is limited only to such examples. It is not a thing.
- Examples of the method of imidizing the (meth) acrylic resin with an imidizing agent include a known imidizing method.
- a specific method for imidizing a (meth) acrylic resin with an imidizing agent for example, (1) A (meth) acrylic resin can be dissolved, the (meth) acrylic resin is dissolved in a solvent inert to imidization, and an imidizing agent is added to the obtained (meth) acrylic resin solution And by reacting the (meth) acrylic resin with an imidizing agent, the (meth) acrylic resin is imidized with an imidizing agent (batch reaction method), (2) An imidizing agent is added to a molten (meth) acrylic resin using an extruder or the like, and the (meth) acrylic resin and the imidizing agent are reacted to imidize the (meth) acrylic resin.
- Method (melt kneading method) is not limited to such examples.
- a batch reaction tank pressure vessel
- the batch-type reaction vessel preferably has a structure in which a solution in which a (meth) acrylic resin is dissolved in a solvent can be heated and stirred, and an imidizing agent can be added. Since the viscosity of the solution may increase as the reaction proceeds, it is more preferable that the stirring efficiency is excellent.
- Examples of the batch-type reaction vessel (pressure vessel) include a Max blend (registered trademark) agitation vessel manufactured by Sumitomo Heavy Industries, Ltd., but the present invention is not limited to such examples. Absent.
- examples of the solvent inert to imidization include aliphatic alcohols such as methanol, ethanol, n-propanol, isopropanol, n-butanol, and isobutanol; benzene, toluene, xylene, and chlorobenzene. And aromatic compounds such as chlorotoluene; ether compounds and the like, but the present invention is not limited to such examples.
- These solvents may be used alone or in combination of two or more. Among these solvents, toluene and a mixed solvent of toluene and methanol are preferable.
- the reaction temperature for reacting the (meth) acrylic resin with the imidizing agent is such that the (meth) acrylic resin is efficiently imidized with the imidizing agent and (meth) acrylic due to an excessive thermal history ( )
- the reaction temperature for reacting the (meth) acrylic resin with the imidizing agent is such that the (meth) acrylic resin is efficiently imidized with the imidizing agent and (meth) acrylic due to an excessive thermal history ( )
- it is preferably 160 to 400 ° C, more preferably 180 to 350 ° C, still more preferably 200 to 300 ° C.
- an extruder In the melt kneading method, an extruder can be used.
- the extruder include a single-screw extruder, a twin-screw extruder, and a multi-screw extruder, but the present invention is not limited to such examples.
- a (meth) acrylic resin and an imidizing agent can be efficiently mixed, and therefore a twin screw extruder is preferable.
- the twin screw extruder include, for example, a non-meshing type co-rotating twin screw extruder, a meshing type co-rotating twin screw extruder, a non-meshing different direction rotating twin screw extruder, and a meshing type.
- twin screw extruder Although a different direction rotation type twin screw extruder etc. are mentioned, this invention is not limited only to this illustration. These extruders may be used singly or two or more may be connected in series. Among the twin screw extruders, the meshing type co-rotating twin screw extruder is preferable because it can rotate at high speed and can efficiently mix the (meth) acrylic resin and the imidizing agent.
- imidation of the (meth) acrylic resin is performed by, for example, charging the (meth) acrylic resin from the raw material charging unit of the extruder, melting the (meth) acrylic resin, and filling the cylinder. Thereafter, the imidizing agent can be injected into the extruder with an addition pump.
- the temperature of the reaction zone (resin temperature) in the extruder is preferably from the viewpoint of efficiently progressing the imidization reaction of the (meth) acrylic resin and improving chemical resistance and heat resistance. 180 ° C. or higher, more preferably 220 ° C. or higher, from the viewpoint of suppressing the decomposition of the (meth) acrylic resin and improving the bending resistance of the optical film, preferably 380 ° C. or lower, more preferably 350 ° C. or lower, Preferably it is 300 degrees C or less.
- the reaction zone in the said extruder means the area
- the imidization of the (meth) acrylic resin can be promoted by lengthening the reaction time between the (meth) acrylic resin and the imidizing agent in the reaction zone in the extruder.
- the time required for imidation of the (meth) acrylic resin in the reaction zone in the extruder is preferably 10 seconds or longer, more preferably 30 seconds or longer from the viewpoint of sufficiently imidizing the (meth) acrylic resin.
- the pressure of the (meth) acrylic resin in the extruder is preferably not less than atmospheric pressure, more preferably not less than 1 MPa, preferably considering the pressure resistance of the extruder. 50 MPa or less, more preferably 30 MPa or less.
- the extruder prefferably provides the extruder with a vent that can be depressurized to atmospheric pressure or less in order to remove unreacted imidizing agent and by-products in the extruder.
- the number of vents may be only one or plural.
- the imidizing agent examples include arylamines having 6 to 10 carbon atoms such as cycloalkylamine having 3 to 12 carbon atoms such as cyclohexylamine, aniline, benzylamine, toluidine, and trichloroaniline.
- arylamines having 6 to 10 carbon atoms such as cycloalkylamine having 3 to 12 carbon atoms
- cyclohexylamine, aniline, benzylamine, toluidine, and trichloroaniline such as cyclohexylamine, aniline, benzylamine, toluidine, and trichloroaniline.
- these imidizing agents may be used alone or in combination of two or more.
- cyclohexylamine, aniline and toluidine are preferable, and aniline is more preferable from the viewpoint of obtaining an optical film having excellent heat resistance and low birefringence.
- the amount of the imidizing agent varies depending on the content of the repeating unit represented by the formula (I) and the content of the repeating unit represented by the formula (II) in the (meth) acrylic resin to be obtained, it should be decided unconditionally. Therefore, it is preferable to adjust the (meth) acrylic resin so that the repeating unit represented by the formula (I) and the repeating unit represented by the formula (II) are contained at a predetermined content. In other words, the content of the repeating unit represented by the formula (I) and the repeating unit represented by the formula (II) in the (meth) acrylic resin can be easily adjusted by adjusting the amount of the imidizing agent. Can do.
- a carboxyl group or an acid anhydride group may be by-produced.
- many carboxyl groups or acid anhydride groups may remain in the (meth) acrylic resin.
- the viscosity of the (meth) acrylic resin increases, so that, for example, molding processability during filming is reduced. There is a risk.
- hydrolysis of the acid anhydride group proceeds, and the durability of the resin and film may be reduced.
- the carboxyl group and acid anhydride group contained in the (meth) acrylic resin into an ester it is preferable to convert the carboxyl group and acid anhydride group contained in the (meth) acrylic resin into an ester.
- Examples of the method for converting a carboxyl group and an acid anhydride group contained in the (meth) acrylic resin into an ester include a method for converting to an ester described in US Pat. No. 4,727,117, The present invention is not limited to such examples.
- esterifying the (meth) acrylic resin with an esterifying agent for example, in the same manner as the method of imidizing the (meth) acrylic resin with an imidizing agent, (1)
- the (meth) acrylic resin can be dissolved, the (meth) acrylic resin is dissolved in a solvent inert to esterification, and the resulting (meth) acrylic resin solution is esterified.
- esterification method By adding an agent and reacting the (meth) acrylic resin with the esterifying agent to esterify the (meth) acrylic resin with the esterifying agent (batch reaction method), (2) An esterifying agent is added to the molten (meth) acrylic resin using an extruder or the like, and the (meth) acrylic resin and the esterifying agent are reacted to thereby change the (meth) acrylic resin. Esterification method (melt kneading method) However, the present invention is not limited to such examples.
- esterifying agent examples include dimethyl carbonate, 2,2-dimethoxypropane, dimethyl sulfoxide, triethyl orthoformate, trimethyl orthoacetate, trimethyl orthoformate, diphenyl carbonate, dimethyl sulfate, methyl toluene sulfonate, methyl trifluoromethyl sulfonate.
- the amount of the esterifying agent per 100 parts by weight of the (meth) acrylic resin is usually preferably 0 to 32 parts by weight, more preferably 0 to 16 parts by weight.
- the esterifying agent can be used in combination with a catalyst.
- the catalyst include aliphatic tertiary amines such as trimethylamine, triethylamine, and tributylamine, and base catalysts such as diazabicycloundecene and diazabicyclononene, but the present invention is limited only to such examples. Is not to be done. These catalysts may be used alone or in combination of two or more. Among these catalysts, diazabicycloundecene is preferable from the viewpoint of reducing costs and preventing adverse effects such as coloring on the meth) acrylic resin.
- the amount of the catalyst is not particularly limited, but is usually preferably 0 to 10 parts by weight, more preferably 0 to 5 parts by weight, and still more preferably 0 to 2 parts by weight per 100 parts by weight of the (meth) acrylic resin. is there.
- a glutarimide resin is obtained by imidizing a (meth) acrylic resin such as polymethylmethacrylate (PMMA) with a primary amine. It is known to go through an acid structure.
- PMMA polymethylmethacrylate
- a glutaric anhydride resin is prepared from a (meth) acrylic resin using an extruder or the like, and the glutaric anhydride resin produced as necessary is isolated.
- a glutarimide structure can be efficiently generated in (meth) acryl. This method is effective when, for example, aniline having a smaller basicity than an alkylamine such as methylamine is used as an imidizing agent.
- a catalyst When preparing a glutaric anhydride resin from a (meth) acrylic resin, a catalyst can be used from the viewpoint of promoting a cyclization reaction to a glutaric anhydride structure.
- a catalyst for promoting the cyclization reaction to a glutaric anhydride structure at least one selected from the group consisting of acids, bases and salts thereof can be used.
- kinds of acids, bases and salts thereof are not particularly limited.
- the catalyst is preferably used within the range where the (meth) acrylic resin is not adversely affected such as coloring and the transparency of the (meth) acrylic resin is not lowered.
- Examples of the acid include hydrochloric acid, sulfuric acid, p-toluenesulfonic acid, phosphoric acid, phosphorous acid, phenylphosphonic acid, methyl phosphate, and the like, but the present invention is not limited to such examples.
- Examples of the base include metal hydroxides, amines, imines, alkali metal derivatives, alkoxides, ammonium hydroxide salts, and the like, but the present invention is not limited to such examples.
- Examples of the acid and base salts include metal acetates, metal stearates, metal carbonates, etc., but the present invention is not limited to such examples.
- a compound having an alkali metal is preferable because an excellent reaction promoting effect is exhibited even in a small amount.
- the compound having an alkali metal include alkali metal hydroxides such as lithium hydroxide, sodium hydroxide and potassium hydroxide, sodium methoxide, sodium ethoxide, sodium phenoxide, potassium methoxide, potassium ethoxide and potassium phenoxide.
- the alkali metal alkoxide compound such as lithium acetate, sodium acetate, potassium acetate, and sodium stearate include organic carboxylic acid alkali metal salts, but the present invention is not limited to such examples.
- sodium hydroxide, sodium methoxide, lithium acetate and sodium acetate are preferable, and sodium methoxide and lithium acetate are more preferable.
- the amount of the catalyst is not particularly limited, but it is usually preferably about 0.01 to 1 part by weight per 100 parts by weight of the (meth) acrylic resin.
- the (meth) acrylic resin may contain other thermoplastic resins as long as the object of the present invention is not impaired.
- Other thermoplastic resins include, for example, olefinic polymers such as polyethylene, polypropylene, ethylene-propylene copolymer, poly (4-methyl-1-pentene); halogen-containing polymers such as vinyl chloride and chlorinated vinyl resins; (Meth) acrylic polymers such as polymethyl methacrylate; styrene polymers such as polystyrene, styrene-methyl methacrylate copolymer, styrene-acrylonitrile copolymer, acrylonitrile-butadiene-styrene block copolymer; polyethylene terephthalate, poly Polyesters such as butylene terephthalate and polyethylene naphthalate; biodegradable polyesters such as polylactic acid and polybutylene succinate; polyamides such as nylon 6, nylon 66, nylon 610; polyaceter Polycarbon
- the (meth) acrylic resin includes, for example, antioxidants such as hindered phenol antioxidants, phosphorus antioxidants, sulfur antioxidants, and the like within the range in which the object of the present invention is not hindered; Stabilizers such as stabilizers, weathering stabilizers and heat stabilizers; reinforcing materials such as glass fibers and carbon fibers; near infrared absorbers; difficulties such as tris (dibromopropyl) phosphate, triallyl phosphate and antimony oxide
- An antistatic agent such as an anionic surfactant, a cationic surfactant, or a nonionic surfactant; a colorant such as an inorganic pigment, an organic pigment, or a dye; a filler such as an organic filler or an inorganic filler; Resin modifiers; plasticizers; lubricants and the like may be included.
- the optical film of the present invention can be manufactured using a (meth) acrylic resin by, for example, a melt extrusion molding method such as a T-die method or an inflation method, a cast molding method, a press molding method, or the like.
- a melt extrusion method such as a T-die method or an inflation method
- a cast molding method such as a cast molding method
- a press molding method such as a press molding method, or the like.
- a melt extrusion method for example, a single screw extruder, a twin screw extruder, or the like can be used.
- the optical film of the present invention can be obtained.
- the optical film of the present invention is preferably uniaxially stretched or biaxially stretched, and biaxially stretched. Is more preferable.
- Examples of the method for biaxially stretching the optical film of the present invention include a sequential biaxial stretching method and a simultaneous biaxial stretching method.
- the present invention is not limited to such examples.
- the stretching temperature when stretching the optical film of the present invention is preferably a glass transition of a (meth) acrylic resin from the viewpoint of stretching the optical film without causing breakage of the optical film and sufficiently aligning the molecules.
- the stretching ratio of the optical film is preferably about 1.5 to 3 times from the viewpoint of increasing the mechanical strength in both the longitudinal direction and the transverse direction perpendicular to the longitudinal direction. More preferably, it is about 5 to 2.5 times.
- the dimensional change rate of the stretched optical film is preferably 1.0% or less, more preferably 0.7% or less, from the viewpoint of improving the durability of a film subjected to secondary processing such as an ITO film. More preferably, it is 0.5% or less, and still more preferably 0.2% or less.
- the thickness of the optical film of the present invention cannot be determined unconditionally because it varies depending on its use.
- a protective film used for an image display device such as an organic EL display device, an antireflection film, a polarizing film
- the thickness of the optical film is The thickness is preferably 1 to 250 ⁇ m, more preferably 10 to 100 ⁇ m, still more preferably 20 to 80 ⁇ m.
- the thickness of the optical film is preferably 20 It is ⁇ 400 ⁇ m, more preferably 30 to 350 ⁇ m, still more preferably 40 to 300 ⁇ m.
- the thickness of an optical film is a thickness when it measures using a Digimatic micrometer [product made from Mitutoyo Corporation], for example.
- the in-plane retardation Re of the optical film of the present invention is preferably 20 nm or less, more preferably 10 nm or less, and further preferably 5 nm or less, from the viewpoint of suppressing the refractive index anisotropy of the optical film and reducing the birefringence. Still more preferably, it is 3 nm or less.
- the absolute value of the thickness direction retardation Rth of the optical film of the present invention is preferably from the viewpoint of suppressing the anisotropy of the refractive index of the optical film and reducing the birefringence similarly to the in-plane retardation Re. Is 20 nm or less, more preferably 10 nm or less, still more preferably 5 nm or less, and even more preferably 3 nm or less.
- the in-plane retardation Re and the thickness direction retardation Rth of the optical film with respect to light having a wavelength of 590 nm are calculated using the retardation film / optical material inspection apparatus [manufactured by Otsuka Electronics Co., Ltd., product number: RETS-100]. It is a value when used and measured under the condition of an incident angle of 40 °.
- the absolute value of the photoelastic coefficient with respect to light having a wavelength of 590 nm of the optical film of the present invention is preferably 10 ⁇ 10 ⁇ 12 Pa ⁇ 1 or less from the viewpoint of suppressing light leakage, particularly light leakage in a high-temperature and high-humidity environment. More preferably, it is 6 ⁇ 10 ⁇ 12 Pa ⁇ 1 or less.
- the photoelastic coefficient of the optical film with respect to light with a wavelength of 590 nm is cut into 20 mm ⁇ 50 mm with the stretching direction of the optical film as the long side, and a sample is prepared.
- This sample is an ellipsometer [manufactured by JASCO Corporation , Product number: M-150], and birefringence is measured at three points while applying a stress load of 5 to 25 N parallel to the stretching direction. It is a value when the inclination of refraction is obtained as a photoelastic coefficient.
- the linear expansion coefficient in the temperature range of 60 to 100 ° C. of the optical film of the present invention is preferably 80 ⁇ 10 ⁇ 6 K ⁇ 1 or less, more preferably 70 ⁇ 10 ⁇ from the viewpoint of suppressing dimensional change in a high temperature environment. 6 K -1 or less.
- the linear expansion coefficient of the optical film at 60 to 100 ° C. is determined from 60 ° C. to 100 ° C. under the following measurement conditions using a thermomechanical measuring apparatus (manufactured by Shimadzu Corporation, product number: TMA-60). It was calculated as the slope at. ⁇ Measurement condition ⁇ ⁇ Sample size: 5 mm ⁇ 20 mm (the long side is the stretching direction) Sample pretreatment: After pretreatment at 60 ° C. for 15 hours, cooling to room temperature Measurement weight: 5 g ⁇ Raising rate: 5 ° C / min
- the water absorption of the optical film of the present invention is preferably 3.0% or less, more preferably 2.5% or less, and even more preferably 2.0% or less, from the viewpoint of improving the molding processability to an ITO film, for example. It is.
- the water absorption rate of the optical film is a value when measured based on the method described in the following examples.
- a coating layer may be formed on the surface of the optical film of the present invention as necessary.
- the coating layer include an antistatic layer, an adhesive layer, an adhesive layer, an easy-adhesion layer, an antiglare layer (non-glare) layer, a photocatalyst layer, an antifouling layer, an antireflection layer, a hard coat layer, an ultraviolet shielding layer, and a heat ray.
- a shielding layer, an electromagnetic wave shielding layer, a gas barrier layer, etc. are mentioned, this invention is not limited only to this illustration.
- the optical film of the present invention has a weak positive birefringence based on the repeating unit represented by the formula (I) and a weak negative birefringence based on the repeating unit represented by the formula (II).
- the birefringence of the two cancels each other out, it has a low birefringence as a whole.
- the optical film of the present invention has a repeating unit represented by the formula (I), it has excellent heat resistance, and has substantially no repeating unit based on an aromatic vinyl monomer typified by styrene. In some cases, it has excellent properties of having a hard surface hardness and a low photoelastic coefficient, which are characteristics based on the repeating unit represented by the formula (II).
- the optical film of the present invention is, for example, a protective film for an optical disc, a polarizer protective film used for a polarizing plate of an image display device such as a liquid crystal display device, a retardation film, a viewing angle compensation film, a light diffusion film, a reflective film, a reflective film. It is expected to be used for applications such as a prevention film, an antiglare film, a brightness enhancement film, a conductive film for a touch panel, a diffusion plate, a light guide, and a prism sheet. Therefore, the optical film of the present invention is expected to be suitably used for applications such as image display devices such as liquid crystal display devices and capacitive touch panels.
- a transparent conductive layer, an optical adjustment layer, a transparent hard coat layer, an antiglare layer, an antireflection layer, and the like may be formed on at least one surface of the optical film of the present invention.
- the optical film having a transparent conductive layer formed on at least one surface of the optical film of the present invention can be used as a transparent conductive film.
- the transparent conductive layer include an inorganic compound layer having a property of reflecting infrared rays, such as an indium-tin oxide (ITO) layer, and a metal mesh layer made of a metal such as silver, copper, nickel, and tungsten.
- ITO indium-tin oxide
- the present invention is not limited to such examples.
- the thickness of the transparent conductive layer is preferably 0.001 to 10 ⁇ m, more preferably 0.005 to 1 ⁇ m, and more preferably from the viewpoint of improving conductivity and light transmittance. Preferably, it is 0.01 to 0.5 ⁇ m.
- the thickness of the transparent conductive layer is preferably from 0.1 to 30 ⁇ m, more preferably from 0.1 to 10 ⁇ m, from the viewpoint of improving conductivity and light transmittance. More preferably, it is 1 to 5 ⁇ m.
- the optical adjustment layer is a layer for appropriately adjusting the transmittance or reflectance of incident light.
- the optical adjustment layer is formed by alternately arranging a low refractive index layer having a relatively low refractive index and a high refractive index layer having a relatively high refractive index. It can be formed by laminating.
- Example 1 (A) Preparation of (meth) acrylic resin Methyl methacrylate (manufactured by Sumitomo Chemical Co., Ltd., trade name: Sumipex EX, weight average molecular weight: 140,000) 29.5 parts by weight, aniline 27.3 parts by weight in a 2 liter autoclave Parts and 33.2 parts by weight of toluene were charged. The autoclave was heated to 240 ° C. and stirred for 3 hours to obtain a reaction solution.
- Methyl methacrylate manufactured by Sumitomo Chemical Co., Ltd., trade name: Sumipex EX, weight average molecular weight: 140,000
- the reaction solution obtained above was subjected to a vent type screw having a barrel temperature of 260 ° C., a rotation speed of 70 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a rear vent number of 1, and a forevent number of 2.
- Transparent (meth) acrylic is introduced into a shaft extruder (hole diameter: 15 mm, L / D: 45) at a processing rate of 300 g / h in terms of resin amount, devolatilized and extruded in this extruder. A resin pellet was obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 100,000.
- the (meth) acrylic resin obtained above has a repeating unit in the formula (I) wherein R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group. , R 4 is a hydrogen atom, R 5 is a methyl group, R 6 is a (meth) acrylic resin having a repeating unit having a methyl group and having a glass transition temperature of 142 ° C.
- the imidation ratio of the (meth) acrylic resin, the content of repeating units represented by the formula (II), and the stress optical coefficient (Cr) were examined based on the following method.
- the imidization ratio of the (meth) acrylic resin was 9.6%
- the content of the repeating unit represented by the formula (II) was 82.1% by weight
- the stress optical coefficient (Cr) was ⁇ 0.01. ⁇ 10 -9 Pa -1
- [Imidation rate] (Meth) imidization ratio of acrylic resin, 1803Cm the absorption derived from a carboxylic acid anhydride group in the vicinity of -1, the absorption derived from the ester carbonyl group in the vicinity of 1720 cm -1, an imide carbonyl groups near 1680 cm -1
- the imidization ratio was determined from the intensity ratio with the absorption derived from.
- the imidization rate is a ratio of imide carbonyl groups in all carbonyl groups.
- (meth) acrylic resin (weight: a) and 1,1,2,2-tetrachloroethane (molecular weight: 167.85, weight: b) as an internal standard are dissolved in heavy acetone, Area ratio of peak derived from internal standard (5.9 ppm, 2 protons) and R 6 proton adjacent to ester carbonyl group [peak area A derived from R 6 proton adjacent to ester carbonyl group and internal standard proton From the ratio to the peak area B derived from (peak area A / peak area B)], the content of the repeating unit represented by the formula (II) was calculated.
- R 4 of the repeating unit represented by the formula (II) is a hydrogen atom
- R 5 is a methyl group
- R 6 is a methyl group
- Stress optical coefficient (Cr) The stress optical coefficient (Cr) of the (meth) acrylic resin is obtained by cutting an unstretched film into a 60 mm ⁇ 20 mm rectangle, selecting a weight so that the stress is 1 N / mm 2 or less, and attaching it to the lower end of the unstretched film. It was.
- This unstretched film was set at a temperature of 3 ° C. higher than the glass transition temperature of the (meth) acrylic resin at a constant temperature dryer (manufactured by ASONE, product number: DOV-450A) with a distance between chucks of 40 mm. After stretching by holding for about 30 minutes, heating was stopped, and cooling was performed at a cooling rate of about 1 ° C./min until the temperature became 40 ° C. lower than the glass transition temperature of the (meth) acrylic resin. Then, the obtained stretched film was taken out from the constant temperature dryer, and the length, thickness and weight of the stretched film were measured, and the in-plane retardation Re of the stretched film was measured.
- the length, thickness and weight of the stretched film were measured in the same manner as described above using four kinds of weights so that the stress was 1 N / mm 2 or less, and the film was stretched. In-plane retardation Re was measured.
- nx is the refractive index in the slow axis direction in the plane of the film (direction showing the maximum refractive index in the film plane), and ny is the fast axis direction in the plane of the film (perpendicular to nx in the film plane).
- ⁇ is a stress (N / m 2 ) on stretching.
- the obtained unstretched film was cut into 96 mm ⁇ 96 mm and stretched at a temperature of 157 ° C. at 240 mm / min using a sequential biaxial stretching machine (manufactured by Toyo Seiki Seisakusho, product number: X-6S). Biaxial stretching was sequentially performed so that the stretching ratio was doubled in the order of the machine direction (MD direction) and the transverse direction (TD direction).
- MD direction machine direction
- TD direction transverse direction
- the stretched film obtained above was quickly taken out from the test apparatus and cooled to obtain an optical film having a thickness of 40 ⁇ m.
- Table 1 shows the glass transition temperature of the (meth) acrylic resin as an index of heat resistance.
- Haze and total light transmittance were measured using a turbidimeter [Nippon Denshoku Industries Co., Ltd., product number: NDH 5000].
- the MIT fold resistance test number was determined by cutting an optical film into 15 mm length and 90 mm length according to JIS P8115, and using the obtained test piece, an MIT fold resistance test machine [ Measured by applying a load of 200 g in an atmosphere having a temperature of 23 ° C. and a relative humidity of 50% using a tester industry, product number: BE-201].
- film impact strength was measured in accordance with ASTM D3420 in an atmosphere at a temperature of 23 ° C. and a relative humidity of 50% using a film impact tester [Tester Sangyo Co., Ltd., product number: BU-302]. .
- Pencil Hardness According to JIS K5600-5-4 (1999), a pencil scratch hardness tester (manufactured by Yasuda Seiki Seisakusho Co., Ltd.) was used and measured at a load of 750 g.
- Example 2 (A) Preparation of (meth) acrylic resin
- a (meth) acrylic resin was obtained in the same manner as in Example 1 except that the reaction temperature of the autoclave was changed to 245 ° C.
- the weight average molecular weight of the obtained (meth) acrylic resin was 100,000.
- the (meth) acrylic resin obtained above has a repeating unit in the formula (I) wherein R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group. , R 4 is a hydrogen atom, R 5 is a methyl group, R 6 is a (meth) acrylic resin having a repeating unit having a methyl group and a glass transition temperature of 152 ° C.
- the imidization ratio of the (meth) acrylic resin, the content of repeating units represented by the formula (II), and the stress optical coefficient (Cr) were examined in the same manner as in Example 1.
- the imidation ratio of the (meth) acrylic resin was 20.9%
- the content of the repeating unit represented by the formula (II) was 60.4% by weight
- the stress optical coefficient (Cr) was 0.02 ⁇ 10 ⁇ 9 Pa ⁇ 1 .
- Example 2 Production of optical film
- the (meth) acrylic resin obtained above was used as the (meth) acrylic resin
- the T-die temperature was 280 ° C
- the roll temperature was 150 ° C
- the stretching temperature was 167 ° C.
- Example 3 (A) Preparation of (meth) acrylic resin (meth) acrylic resin in Example 1, except that the reaction temperature of the autoclave was changed to 247 ° C and the barrel temperature was changed to 270 ° C. Got.
- the obtained (meth) acrylic resin had a weight average molecular weight of 90,000.
- the (meth) acrylic resin obtained above has a repeating unit in the formula (I) wherein R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group. , R 4 is a hydrogen atom, R 5 is a methyl group, R 6 is a (meth) acrylic resin having a repeating unit having a methyl group and a glass transition temperature of 160 ° C.
- the imidization ratio of the (meth) acrylic resin, the content of repeating units represented by the formula (II), and the stress optical coefficient (Cr) were examined in the same manner as in Example 1.
- the imidation ratio of the (meth) acrylic resin was 23.9%
- the content of the repeating unit represented by the formula (II) was 55.6% by weight
- the stress optical coefficient (Cr) was 0.04 ⁇ 10 ⁇ 9 Pa ⁇ 1 .
- Example 2 Production of optical film
- the (meth) acrylic resin obtained above was used as the (meth) acrylic resin
- the T-die temperature was 285 ° C
- the roll temperature was 155 ° C
- the stretching temperature was 285 ° C
- An optical film having a thickness of 40 ⁇ m was obtained in the same manner as in Example 1 except that was changed to 175 ° C.
- Example 4 Preparation of (meth) acrylic resin A (meth) acrylic resin was prepared in the same manner as in Example 1, except that the reaction temperature of the autoclave was changed to 250 ° C and the barrel temperature was changed to 270 ° C. Got. The obtained (meth) acrylic resin had a weight average molecular weight of 90,000.
- the (meth) acrylic resin obtained above has a repeating unit in the formula (I) wherein R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group. , R 4 is a hydrogen atom, R 5 is a methyl group, R 6 is a (meth) acrylic resin having a repeating unit having a methyl group and a glass transition temperature of 167 ° C.
- the imidization ratio of the (meth) acrylic resin, the content of repeating units represented by the formula (II), and the stress optical coefficient (Cr) were examined in the same manner as in Example 1.
- the imidation ratio of the (meth) acrylic resin was 30.9%
- the content of the repeating unit represented by the formula (II) was 45.5% by weight
- the stress optical coefficient (Cr) was 0.05 ⁇ . 10 ⁇ 9 Pa ⁇ 1 .
- Example 2 Production of optical film
- the (meth) acrylic resin obtained above was used as the (meth) acrylic resin
- the T-die temperature was 295 ° C
- the roll temperature was 165 ° C
- the stretching temperature An optical film having a thickness of 40 ⁇ m was obtained in the same manner as in Example 1 except that was changed to 182 ° C.
- Example 5 (A) Preparation of (meth) acrylic resin 6,6 ′, 6 ′′-(1,3,5-) as an ultraviolet absorber with respect to 100 parts by weight of the (meth) acrylic resin obtained in Example 1 Triazine-2,4,6-triyl) tris (3-hexyloxy-2-methylphenol) [manufactured by ADEKA, trade name: ADK STAB (registered trademark) LA-F70], ultraviolet rays at a ratio of 0.66 parts by weight
- the absorbent was added to the (meth) acrylic resin, kneaded at 260 ° C. using a twin screw extruder, and extruded to obtain transparent (meth) acrylic resin pellets.
- the weight average molecular weight of the obtained (meth) acrylic resin was 100,000.
- the (meth) acrylic resin obtained above has a repeating unit in the formula (I) wherein R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group. , R 4 is a hydrogen atom, R 5 is a methyl group, R 6 is a (meth) acrylic resin having a repeating unit having a methyl group and having a glass transition temperature of 142 ° C.
- the imidization ratio of the (meth) acrylic resin, the content of repeating units represented by the formula (II), and the stress optical coefficient (Cr) were examined in the same manner as in Example 1.
- the imidation ratio of the (meth) acrylic resin was 9.6%
- the content of the repeating unit represented by the formula (II) was 82.1% by weight
- the stress optical coefficient (Cr) was 0.03 ⁇ 10 ⁇ 9 Pa ⁇ 1 .
- Example 1 An optical film having a thickness of 40 ⁇ m was used in the same manner as in Example 1 except that the (meth) acrylic resin obtained above was used as the (meth) acrylic resin. Got.
- Example 6 Preparation of (meth) acrylic resin In a reaction kettle equipped with a stirrer, temperature sensor, cooling pipe and nitrogen gas introduction pipe, 79.4 parts by weight of methyl methacrylate, 20.6 parts by weight of methacrylic acid, polymerization solvent As a mixed solvent of 65.2 parts by weight of toluene and 16.3 parts by weight of methanol, and 0.05 parts by weight of an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112), n-dodecyl mercaptan as a chain transfer agent 0.2 part by weight was charged, and the temperature was raised to 80 ° C. while passing nitrogen gas through the reaction kettle.
- ADEKA trade name: ADK STAB 2112
- dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 10 parts by weight is added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] 0.20 part by weight was added dropwise to the reaction kettle over 2 hours, and solution polymerization was performed under reflux at about 80 to 85 ° C., and after completion of the addition of dimethyl-2,2′-azobis (2-methylpropionate), an additional 4 Aged over time.
- the content of repeating units derived from methacrylic acid in the (meth) acrylic resin contained in the obtained polymer solution was 21.2% by weight. Moreover, the weight average molecular weight of the (meth) acrylic resin was 100,000.
- the (meth) acrylic resin obtained above has a repeating unit in the formula (I) wherein R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group. , R 4 is a hydrogen atom, R 5 is a methyl group, R 6 is a methyl group, has a repeating unit, and has a glass transition temperature of 154 ° C. (meth) acrylic resin.
- the imidization ratio of the (meth) acrylic resin, the content of repeating units represented by the formula (II), and the stress optical coefficient (Cr) were examined in the same manner as in Example 1.
- the imidation ratio of the (meth) acrylic resin was 23.1%
- the content of the repeating unit represented by the formula (II) was 56.9% by weight
- the stress optical coefficient (Cr) was 0.04 ⁇ 10 ⁇ 9 Pa ⁇ 1 .
- Example 2 Production of optical film
- the (meth) acrylic resin obtained above was used as the (meth) acrylic resin
- the T-die temperature was 285 ° C
- the roll temperature was 150 ° C
- the stretching temperature. was changed to 169 ° C.
- an optical film having a thickness of 40 ⁇ m was obtained in the same manner as in Example 1.
- Example 7 (A) Preparation of (meth) acrylic resin
- the polymer solution obtained in Example 6 was subjected to a barrel temperature of 260 ° C., a rotation speed of 70 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), and a rear vent number of 1. Introduced into a vent type screw twin screw extruder (hole diameter: 15 mm, L / D: 45) with a fore vent number of 2 at a processing speed of 300 g / h in terms of resin amount, and devolatilized in this extruder. By extrusion, transparent (meth) acrylic resin pellets were obtained.
- the obtained (meth) acrylic resin had a weight average molecular weight of 100,000 and a glass transition temperature of 136 ° C.
- the pellet obtained above is a vent type screw twin screw extruder (hole diameter: 15 mm, L / D) having a barrel temperature of 270 ° C., a rotation speed of 300 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), and a single vent. : 45) was introduced from the hopper at a processing rate of 300 g / h in terms of resin amount, and aniline was injected from the hopper at a feeding rate of 277 g / h from the hopper, and extruded to give a transparent ( A pellet of (meth) acrylic resin was obtained.
- the obtained (meth) acrylic resin had a weight average molecular weight of 90,000.
- the (meth) acrylic resin obtained above has a repeating unit in the formula (I) wherein R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group. , R 4 is a hydrogen atom, R 5 is a methyl group, R 6 is a (meth) acrylic resin having a repeating unit having a methyl group and a glass transition temperature of 148 ° C.
- the imidization ratio of the (meth) acrylic resin, the content of repeating units represented by the formula (II), and the stress optical coefficient (Cr) were examined in the same manner as in Example 1.
- the imidation ratio of the (meth) acrylic resin was 16.8%
- the content of the repeating unit represented by the formula (II) was 67.4% by weight
- the stress optical coefficient (Cr) was 0.01 ⁇ 10 ⁇ 9 Pa ⁇ 1 .
- Example 2 Production of optical film
- the (meth) acrylic resin obtained above was used as the (meth) acrylic resin
- the T-die temperature was 275 ° C
- the roll temperature was 145 ° C
- the stretching temperature was 163 ° C.
- the reaction solution obtained above had a barrel temperature of 260 ° C., a rotation speed of 70 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a rear vent number of 1, and a forevent number of 2 Transparent resin by introducing into a vent type screw twin screw extruder (hole diameter: 15 mm, L / D: 45) at a processing rate of 300 g / h in terms of resin amount, devolatilizing and extruding in this extruder Pellets were obtained.
- the resulting methyl methacrylate-styrene imide resin had a glass transition temperature of 143 ° C. and a weight average molecular weight of 90,000.
- the imidization ratio and stress optical coefficient (Cr) of the methyl methacrylate-styrene imide resin obtained above were measured in the same manner as in Example 1.
- the imidation ratio of the methyl methacrylate-styrene imide resin was 89.5%
- the stress optical coefficient (Cr) was ⁇ 1.72 ⁇ 10 ⁇ 9 Pa ⁇ 1 .
- the styrene content in the methyl methacrylate-styrene imide resin obtained above was measured based on the following method, the styrene content was 44.9% by weight.
- the styrene content of the resin was determined by measuring the 1 H-NMR spectrum using an NMR measurement apparatus (manufactured by Varian, trade name: Unity Plus 400), and measuring the area of hydrogen atoms derived from the aromatic ring on the low magnetic field side and the high magnetic field side. Measurement was based on the area ratio of aliphatic hydrogen atoms.
- Example 2 Production of optical film In Example 1, except that the methyl methacrylate-styrene imide resin obtained above was used in place of the (meth) acrylic resin and the stretching temperature was changed to 158 ° C. In the same manner as in Example 1, an optical film having a thickness of 40 ⁇ m was obtained.
- Comparative Example 2 (A) Preparation of (meth) acrylic resin
- methyl methacrylate-styrene copolymer was changed to methyl methacrylate-styrene copolymer [manufactured by Nippon Steel & Sumikin Chemical Co., Ltd., trade name: Estyrene MS700, weight average molecular weight: 130,000] and a methyl methacrylate-styrene imide resin was obtained in the same manner as in Comparative Example 1 except that the amount of the 40% methylamine-methanol solution was changed to 3.5 parts by weight.
- the obtained methyl methacrylate-styrene imide resin had a weight average molecular weight of 90,000 and a glass transition temperature of 152 ° C.
- the methyl methacrylate-styrene imide resin had an imidation ratio of 90.8% and a stress optical coefficient (Cr) of 0.09 ⁇ 10 ⁇ 9 Pa ⁇ 1 .
- Comparative Example 3 (A) Preparation of (meth) acrylic resin
- methyl methacrylate-styrene copolymer was changed to methyl methacrylate-styrene copolymer [manufactured by Nippon Steel & Sumikin Chemical Co., Ltd., trade name: Estyrene MS800, weight average molecular weight: 130,000] and a methyl methacrylate-styrene imide resin was obtained in the same manner as in Comparative Example 1 except that the amount of the 40% methylamine-methanol solution was changed to 4 parts by weight.
- the resulting methyl methacrylate-styrene imide resin had a weight average molecular weight of 90,000 and a glass transition temperature of 160 ° C.
- the imidation ratio of the methyl methacrylate-styrene imide resin was 92.6%, and the stress optical coefficient (Cr) was 0.93 ⁇ 10 ⁇ 9 Pa ⁇ 1 .
- each of the optical films obtained in each example has good heat resistance, haze, total light transmittance, MIT folding resistance and impact strength, and in-plane retardation.
- the thickness direction retardation is small, it has low birefringence, high surface hardness (pencil hardness), and excellent properties such as a small absolute value of the photoelastic coefficient.
- Production Example 1 In a reaction kettle equipped with a stirrer, a temperature sensor, a cooling pipe and a nitrogen gas introduction pipe, 79.4 parts by weight of methyl methacrylate, 20.6 parts by weight of methacrylic acid, 90.0 parts by weight of toluene as a polymerization solvent and 22. A mixed solvent with 5 parts by weight and 0.05 parts by weight of an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were charged, and the temperature was raised to 73 ° C. while passing nitrogen gas into the reaction kettle.
- an antioxidant manufactured by ADEKA, trade name: ADK STAB 2112
- dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 7.3 parts by weight of toluene and 1.8 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), aging was carried out for an additional 4 hours.
- the content of repeating units derived from methacrylic acid in the (meth) acrylic resin contained in the polymer solution obtained above was 20.6% by weight. Moreover, the weight average molecular weight of the (meth) acrylic resin was 110,000.
- Vent type screw twin screw extruder having a barrel temperature of 290 ° C., a rotation speed of 70 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a rear vent number of 1, and a forevent number of 2 (Pore diameter: 15 mm, L / D: 45) is introduced at a processing rate of 300 g / h in terms of resin amount, devolatilized in this twin-screw extruder, and extruded with a residence time of about 0.9 minutes in the shaft. As a result, a transparent (meth) acrylic resin pellet was obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 100,000, and the glass transition temperature was 131 ° C.
- the anhydrous glutar oxidation rate of the (meth) acrylic resin obtained above was investigated based on the following method. As a result, the anhydrous (glutaric) oxidation rate of the obtained (meth) acrylic resin was 17.5%.
- Anhydrous glutar oxidation rate (Meth) glutaric anhydride oxidation rate of the acrylic resin, the absorption derived from a carboxylic acid anhydride group in the vicinity of 1803cm -1, and the absorption derived from the ester carbonyl group in the vicinity of 1720 cm -1, imide carbonyl near 1680 cm -1
- the anhydrous glutar oxidation rate was determined from the intensity ratio with the absorption derived from the group.
- the anhydrous glutar oxidation rate is the ratio of carboxylic anhydride groups in all carbonyl groups.
- Example 8 The pellet obtained in Production Example 1 has a barrel temperature of 290 ° C., a rotation speed of 300 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a vent type screw twin screw extruder having a single vent (hole diameter: 15 mm, L / D: 45) is introduced from the hopper at a processing rate of 420 g / h in terms of resin amount, and aniline is injected from the hopper after the hopper at a charging rate of 101 g / h. By extruding in about 1 minute, transparent (meth) acrylic resin pellets were obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 90,000.
- the (meth) acrylic resin includes a repeating unit in which R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group in the formula (I) and in the formula (II), R 4 is It was a (meth) acrylic resin which has a repeating unit which is a hydrogen atom, R 5 is a methyl group, R 6 is a methyl group, and has a glass transition temperature of 162 ° C.
- the imidation ratio of the (meth) acrylic resin obtained above was 44.1%
- the content of the repeating unit represented by the formula (II) was 37.3% by weight
- the stress optical coefficient (Cr) was 0.08.
- ⁇ 10 -9 Pa -1 content of the metal in the said (meth) acrylic-type resin was investigated based on the following method. As a result, the metal content in the obtained (meth) acrylic resin was 470 ppm.
- Production Example 2 In a reaction kettle equipped with a stirrer, a temperature sensor, a cooling pipe and a nitrogen gas introduction pipe, 79.4 parts by weight of methyl methacrylate, 20.6 parts by weight of methacrylic acid, 90.0 parts by weight of toluene as a polymerization solvent and 22. A mixed solvent with 5 parts by weight and 0.05 parts by weight of an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were charged, and the temperature was raised to 73 ° C. while passing nitrogen gas into the reaction kettle.
- an antioxidant manufactured by ADEKA, trade name: ADK STAB 2112
- dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 7.3 parts by weight of toluene and 1.8 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), aging was carried out for an additional 4 hours.
- the content of repeating units derived from methacrylic acid in the (meth) acrylic resin contained in the polymer solution obtained above was 20.6% by weight. Moreover, the weight average molecular weight of the (meth) acrylic resin was 110,000.
- Vent type screw twin screw extruder having a barrel temperature of 280 ° C., a rotation speed of 70 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a rear vent number of 1, and a forevent number of 2 (Pore diameter: 15 mm, L / D: 45), introduced at a processing rate of 420 g / h in terms of resin amount, devolatilized in this twin-screw extruder, and extruded in a shaft residence time of about 3.2 minutes As a result, a transparent (meth) acrylic resin pellet was obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 97,000, and the glass transition temperature was 131 ° C. Moreover, the anhydrous glutar oxidation rate of the (meth) acrylic resin was 16.3%.
- Example 9 The pellet obtained in Production Example 2 was a vent type screw twin screw extruder (hole diameter: 15 mm, L) with a barrel temperature of 290 ° C., a rotation speed of 300 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), and a single vent. / D: 45) is introduced from the hopper at a processing rate of 420 g / h in terms of resin amount, and aniline is injected from the hopper after the hopper at a charging rate of 101 g / h. By extruding in about 2 minutes, transparent (meth) acrylic resin pellets were obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 89,000.
- the (meth) acrylic resin includes a repeating unit in which R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group in the formula (I) and in the formula (II), R 4 is It was a (meth) acrylic resin having a repeating unit that is a hydrogen atom, R 5 is a methyl group, R 6 is a methyl group, and has a glass transition temperature of 167 ° C.
- the imidation ratio of the (meth) acrylic resin obtained above was 47.2%, the content of the repeating unit represented by the formula (II) was 35.4% by weight, and the stress optical coefficient (Cr) was 0.11. ⁇ 10 -9 Pa -1
- the metal content in the (meth) acrylic resin was 235 ppm.
- Production Example 3 In a reaction kettle equipped with a stirrer, a temperature sensor, a cooling pipe and a nitrogen gas introduction pipe, 79.4 parts by weight of methyl methacrylate, 20.6 parts by weight of methacrylic acid, 90.0 parts by weight of toluene as a polymerization solvent and 22. A mixed solvent with 5 parts by weight and 0.05 parts by weight of an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were charged, and the temperature was raised to 73 ° C. while passing nitrogen gas into the reaction kettle.
- an antioxidant manufactured by ADEKA, trade name: ADK STAB 2112
- dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 7.3 parts by weight of toluene and 1.8 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), the mixture was further aged for 4 hours to obtain a polymer solution.
- the content of repeating units derived from methacrylic acid in the (meth) acrylic resin contained in the polymer solution obtained above was 20.6% by weight. Moreover, the weight average molecular weight of the (meth) acrylic resin was 110,000.
- Vent type screw twin screw extruder having a barrel temperature of 290 ° C., a rotation speed of 70 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a rear vent number of 1, and a forevent number of 2 (Pore diameter: 15 mm, L / D: 45) Introduced at a processing rate of 300 g / h in terms of resin amount, devolatilized in this extruder, and extruded in a shaft residence time of about 3.0 minutes A transparent (meth) acrylic resin pellet was obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 100,000, and the glass transition temperature was 130 ° C. Moreover, the anhydrous glutar oxidation rate of the (meth) acrylic resin was 15.9%.
- Example 10 The pellet obtained in Production Example 3 was a vent type screw twin screw extruder (hole diameter: 15 mm, L) with a barrel temperature of 290 ° C., a rotation speed of 300 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), and a single vent. / D: 45) is introduced from the hopper at a treatment rate of 432 g / h in terms of resin amount, and aniline is injected from the hopper after the hopper at a feed rate of 104 g / h. By extruding in about 2 minutes, transparent (meth) acrylic resin pellets were obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 92,000.
- the (meth) acrylic resin includes a repeating unit in which R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group in the formula (I) and in the formula (II), R 4 is It was a (meth) acrylic resin having a repeating unit that is a hydrogen atom, R 5 is a methyl group, R 6 is a methyl group, and has a glass transition temperature of 161 ° C.
- the imidation ratio of the (meth) acrylic resin obtained above was 42.0%, the content of the repeating unit represented by the formula (II) was 38.5% by weight, and the stress optical coefficient (Cr) was 0.07. ⁇ 10 -9 Pa -1
- the metal content in the (meth) acrylic resin was 135 ppm.
- Example 2 Using the pellets obtained in Examples 8 to 10, in Example 1, except that the T die temperature, roll temperature, and stretching temperature were changed as shown in Table 2, the thickness was 40 ⁇ m. An optical film was obtained.
- the optical films obtained in each Example all have good heat resistance, haze, total light transmittance, MIT folding resistance and impact strength, and in-plane retardation.
- the thickness direction retardation is small, it has low birefringence, high surface hardness (pencil hardness), and excellent properties such as a small absolute value of the photoelastic coefficient.
- Production Example 4 In a reaction kettle equipped with a stirrer, a temperature sensor, a cooling pipe and a nitrogen gas introduction pipe, 79.4 parts by weight of methyl methacrylate, 20.6 parts by weight of methacrylic acid, 90.0 parts by weight of toluene as a polymerization solvent and 22. A mixed solvent with 5 parts by weight and 0.05 parts by weight of an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were charged, and the temperature was raised to 73 ° C. while passing nitrogen gas into the reaction kettle.
- an antioxidant manufactured by ADEKA, trade name: ADK STAB 2112
- dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 7.3 parts by weight of toluene and 1.8 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), the mixture was further aged for 4 hours to obtain a polymer solution.
- the content of repeating units derived from methacrylic acid in the (meth) acrylic resin contained in the polymer solution obtained above was 20.6% by weight. Moreover, the weight average molecular weight of the (meth) acrylic resin was 110,000.
- Vent type screw twin screw extruder having a barrel temperature of 290 ° C., a rotational speed of 238 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a rear vent number of 1, and a forevent number of 2 (Pore diameter: 15 mm, L / D: 45) Introduced at a processing rate of 300 g / h in terms of resin amount, devolatilized in this extruder, and extruded with an in-shaft residence time of about 0.9 minutes. A transparent (meth) acrylic resin pellet was obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 100,000, and the glass transition temperature was 131 ° C.
- the pellet obtained above was a barrel type screw twin screw extruder (hole diameter: 15 mm, bore temperature: 290 ° C., rotation speed: 300 rpm, degree of vacuum: 13.3 to 400 hPa (10 to 300 mmHg), one vent number) L / D: 45) is introduced from the hopper at a processing rate of 420 g / h in terms of resin amount, and aniline is injected from the hopper after the hopper at a charging rate of 162 g / h. By extruding in about 6 minutes, transparent (meth) acrylic resin pellets were obtained. The weight average molecular weight of the (meth) acrylic resin obtained above was 94,000.
- the (meth) acrylic resin obtained above has a repeating unit in the formula (I) wherein R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group. , R 4 is a hydrogen atom, R 5 is a methyl group, R 6 is a (meth) acrylic resin having a repeating unit having a methyl group and a glass transition temperature of 161 ° C.
- the imidation ratio of the (meth) acrylic resin obtained above was 44.1%, the content of the repeating unit represented by the formula (II) was 37.3% by weight, and the stress optical coefficient (Cr) was 0.12 ⁇ 10 ⁇ 9 Pa ⁇ 1 .
- the acid value of the (meth) acrylic resin was 1.27 mmol / g.
- Example 11 The pellet obtained in Production Example 4 has a barrel temperature of 260 ° C., a rotation speed of 300 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a vent type screw twin screw extruder having a single vent (hole diameter: 15 mm, L / D: 45) is introduced from the hopper at a processing rate of 420 g / h in terms of resin amount, and 16.0 parts by weight of dimethyl carbonate (DBC) and diazabicycloundecene (DBU) with respect to the raw material resin after the hopper. ) A mixed liquid of 2.0 parts by weight was injected with a liquid pump, and extruded with an in-shaft residence time of about 5.2 minutes to obtain transparent (meth) acrylic resin pellets.
- DDC dimethyl carbonate
- DBU diazabicycloundecene
- the (meth) acrylic resin obtained above had a weight average molecular weight of 80,000.
- the (meth) acrylic resin includes a repeating unit in which R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group in the formula (I) and in the formula (II), R 4 is It was a (meth) acrylic resin having a hydrogen atom, a repeating unit in which R 5 is a methyl group, R 6 is a methyl group, and a glass transition temperature of 148 ° C.
- the imidation ratio of the (meth) acrylic resin obtained above was 47.9%, the content of the repeating unit represented by the formula (II) was 59.1% by weight, and the stress optical coefficient (Cr) was ⁇ 0.18. ⁇ 10 -9 Pa -1 Moreover, the acid value of the (meth) acrylic resin was 0.13 mmol / g.
- the pellet obtained above is put into a single screw extruder (hole diameter: 20 mm, L / D: 25), the T die temperature is adjusted to 275 ° C., and melt extrusion is performed from a coat hanger type T die (width 150 mm). And was discharged onto a cooling roll having a roll temperature of 145 ° C. to produce an unstretched film having a thickness of 160 ⁇ m.
- the unstretched film obtained above was cut into 96 mm ⁇ 96 mm, and using a sequential biaxial stretching machine (manufactured by Toyo Seiki Seisakusho, product number: X-6S), a stretching speed of 240 mm / min at a temperature of 168 ° C. Then, biaxial stretching was sequentially performed so that the stretching ratio was doubled in the order of the machine direction (MD direction) and the transverse direction (TD direction). After biaxial stretching of the unstretched film, the obtained stretched film was quickly taken out from the test apparatus and cooled to obtain an optical film having a thickness of 40 ⁇ m.
- the in-plane retardation and thickness direction retardation of the obtained optical film were 4.5 nm and ⁇ 13.3 nm, respectively.
- the measuring method of a water absorption rate and a dimensional change rate is as follows. Also in the following examples and comparative examples, the water absorption rate and the dimensional change rate were examined based on the following method.
- the unstretched film obtained above is absorbed in water by storing it in a thermostatic bath at 85 ° C. and a relative humidity of 85%, taken out from the thermostatic bath after 250 hours, and the mass of the unstretched film after water absorption (Y ) Was measured.
- the sample was stored in a thermostat at 85 ° C. and a relative humidity of 85%, taken out of the thermostat after 250 hours, and the lengths of the four pieces of the sample (Lb1, Lb2, Lb3, Lb4) were measured again. .
- La represents the length of one side before the test
- Lb represents the length of one piece after the test
- Production Example 5 In a reaction kettle equipped with a stirrer, a temperature sensor, a cooling pipe and a nitrogen gas introduction pipe, 79.4 parts by weight of methyl methacrylate, 20.6 parts by weight of methacrylic acid, 90.0 parts by weight of toluene as a polymerization solvent and 22. A mixed solvent with 5 parts by weight and 0.05 parts by weight of an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were charged, and the temperature was raised to 73 ° C. while passing nitrogen gas into the reaction kettle.
- an antioxidant manufactured by ADEKA, trade name: ADK STAB 2112
- dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 7.3 parts by weight of toluene and 1.8 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), aging was carried out for an additional 4 hours.
- the content of repeating units derived from methacrylic acid in the (meth) acrylic resin contained in the polymer solution obtained above was 20.6% by weight. Moreover, the weight average molecular weight of the (meth) acrylic resin was 110,000.
- Vent type screw twin screw extruder having a barrel temperature of 290 ° C., a rotational speed of 238 rpm, a reduced pressure of 13.3 to 400 hPa (10 to 300 mmHg), a rear vent number of 1, and a forevent number of 2 (Pore diameter: 15 mm, L / D: 45) Introduced at a processing speed of 480 g / h in terms of resin amount, devolatilized in this extruder, and extruded with a shaft residence time of about 3.7 minutes A transparent (meth) acrylic resin pellet was obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 102,000, and the glass transition temperature was 130 ° C.
- the pellet obtained above was a barrel type screw twin screw extruder (hole diameter: 15 mm, bore temperature: 290 ° C., rotation speed: 300 rpm, degree of vacuum: 13.3 to 400 hPa (10 to 300 mmHg), one vent number) L / D: 45) was introduced from the hopper at a treatment rate of 432 g / h in terms of resin amount, and aniline was injected from the hopper after the hopper at a feed rate of 250 g / h, and the residence time in the shaft was 5 By extruding in about 5 minutes, transparent (meth) acrylic resin pellets were obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 97,000.
- the (meth) acrylic resin obtained above has a repeating unit in the formula (I) wherein R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group. , R 4 is a hydrogen atom, R 5 is a methyl group, R 6 is a methyl group, and a (meth) acrylic resin having a glass transition temperature of 171 ° C.
- the imidation ratio of the (meth) acrylic resin obtained above was 52.6%
- the content of the repeating unit represented by the formula (II) was 29.5% by weight
- the stress optical coefficient (Cr) was 0.00. It was 23 ⁇ 10 ⁇ 9 Pa ⁇ 1 .
- the acid value of the (meth) acrylic resin was 1.58 mmol / g.
- Example 12 The pellet obtained in Production Example 5 has a barrel temperature of 260 ° C., a rotation speed of 300 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a vent type screw twin screw extruder having a single vent (hole diameter: 15 mm, L / D: 45) is introduced from the hopper at a processing rate of 420 g / h in terms of resin amount, and 16.0 parts by weight of dimethyl carbonate (DBC) and diazabicycloundecene (DBU) with respect to the raw material resin after the hopper.
- DBC dimethyl carbonate
- DBU diazabicycloundecene
- the (meth) acrylic resin obtained above has a repeating unit in the formula (I) wherein R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group. , R 4 is a hydrogen atom, R 5 is a methyl group, R 6 is a (meth) acrylic resin having a repeating unit having a methyl group and a glass transition temperature of 155 ° C.
- the imidation ratio of the (meth) acrylic resin obtained above was 50.1%, the content of the repeating unit represented by the formula (II) was 44.2% by weight, and the stress optical coefficient (Cr) was ⁇ 0.05. ⁇ 10 -9 Pa -1 Moreover, the acid value of the (meth) acrylic resin was 0.77 mmol / g.
- the pellet obtained above is put into a single screw extruder (hole diameter: 20 mm, L / D: 25), the T die temperature is adjusted to 280 ° C., and melt extrusion is performed from a coat hanger type T die (width 150 mm). Then, the film was discharged onto a cooling roll having a roll temperature of 150 ° C. to produce an unstretched film having a thickness of 160 ⁇ m.
- the unstretched film obtained above was cut into 96 mm ⁇ 96 mm, and was sequentially 240 mm / min at a temperature of 175 ° C. using a biaxial stretching machine (manufactured by Toyo Seiki Seisakusho, product number: X-6S). Biaxial stretching was performed sequentially so that the stretching ratio was doubled in the order of the machine direction (MD direction) and the transverse direction (TD direction) at the stretching speed of.
- MD direction machine direction
- TD direction transverse direction
- the in-plane retardation and the thickness direction retardation of the optical film obtained above were 0.4 nm and ⁇ 2.7 nm, respectively.
- Production Example 6 In a reaction kettle equipped with a stirrer, a temperature sensor, a cooling pipe and a nitrogen gas introduction pipe, 79.4 parts by weight of methyl methacrylate, 20.6 parts by weight of methacrylic acid, 90.0 parts by weight of toluene as a polymerization solvent and 22. A mixed solvent with 5 parts by weight and 0.05 parts by weight of an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were charged, and the temperature was raised to 73 ° C. while passing nitrogen gas into the reaction kettle.
- an antioxidant manufactured by ADEKA, trade name: ADK STAB 2112
- dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 7.3 parts by weight of toluene and 1.8 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), aging was carried out for an additional 4 hours.
- the content of repeating units derived from methacrylic acid in the (meth) acrylic resin contained in the polymer solution obtained above was 20.6% by weight. Moreover, the weight average molecular weight of the (meth) acrylic resin was 110,000.
- the polymerization solution obtained above was subjected to a vent type screw having a barrel temperature of 280 ° C., a rotation speed of 238 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a rear vent number of 1, and a forevent number of 2. It is introduced into a shaft extruder (hole diameter: 15 mm, L / D: 45) at a processing speed of 624 g / h in terms of resin amount, devolatilized in this extruder, and pushed in a shaft residence time of about 2.6 minutes. As a result, a transparent (meth) acrylic resin pellet was obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 98,000, and the glass transition temperature was 130 ° C.
- the pellet obtained above was a barrel type screw twin screw extruder (hole diameter: 15 mm, bore temperature: 290 ° C., rotation speed: 300 rpm, degree of vacuum: 13.3 to 400 hPa (10 to 300 mmHg), one vent number) L / D: 45) was introduced from the hopper at a processing rate of 420 g / h in terms of resin amount, and aniline was injected from the hopper after the hopper at a charging rate of 202 g / h. By extruding in about 5 minutes, transparent (meth) acrylic resin pellets were obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 92,000.
- the (meth) acrylic resin obtained above has a repeating unit in the formula (I) wherein R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group. , R 4 is a hydrogen atom, R 5 is a methyl group, R 6 is a (meth) acrylic resin having a repeating unit having a methyl group and a glass transition temperature of 178 ° C.
- the imidation ratio of the (meth) acrylic resin obtained above was 54.6%, the content of the repeating unit represented by the formula (II) was 26.2% by weight, and the stress optical coefficient (Cr) was 0.20 ⁇ 10 ⁇ 9 Pa ⁇ 1 . Moreover, the acid value of the (meth) acrylic resin was 1.40 mmol / g.
- Example 13 The pellet obtained in Production Example 6 was a vent type screw twin screw extruder (hole diameter: 15 mm, L) with a barrel temperature of 290 ° C., a rotation speed of 300 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), and a single vent. / D: 45) is introduced from the hopper at a processing rate of 420 g / h in terms of resin amount, and 16.0 parts by weight of dimethyl carbonate (DBC) and diazabicycloundecene (DBU) with respect to the raw material resin after the hopper. ) A mixed liquid of 2.0 parts by weight was injected with a liquid pump, and extruded with an in-shaft residence time of about 5.2 minutes to obtain transparent (meth) acrylic resin pellets.
- DBC dimethyl carbonate
- DBU diazabicycloundecene
- the weight average molecular weight of the (meth) acrylic resin obtained above was 83,000.
- the (meth) acrylic resin obtained above has a repeating unit in the formula (I) wherein R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group. , R 4 is a hydrogen atom, R 5 is a methyl group, R 6 is a (meth) acrylic resin having a repeating unit having a methyl group and a glass transition temperature of 158 ° C.
- the imidation ratio of the (meth) acrylic resin obtained above was 52.2%, the content of the repeating unit represented by the formula (II) was 43.5% by weight, and the stress optical coefficient (Cr) was ⁇ 0.12. ⁇ 10 -9 Pa -1
- the acid value of the (meth) acrylic resin was 0.48 mmol / g.
- the pellet obtained above is put into a single screw extruder (hole diameter: 20 mm, L / D: 25), the T die temperature is adjusted to 285 ° C., and melt extrusion is performed from a coat hanger type T die (width 150 mm). And was discharged onto a cooling roll having a roll temperature of 155 ° C. to produce an unstretched film having a thickness of 160 ⁇ m.
- the unstretched film obtained above was cut out to 96 mm ⁇ 96 mm, and was successively 240 mm / min at a temperature of 178 ° C. using a biaxial stretching machine (manufactured by Toyo Seiki Seisakusho, product number: X-6S). Biaxial stretching was performed sequentially so that the stretching ratio was doubled in the order of the machine direction (MD direction) and the transverse direction (TD direction) at the stretching speed of.
- MD direction machine direction
- TD direction transverse direction
- the in-plane retardation and the thickness direction retardation of the optical film obtained above were 2.1 nm and ⁇ 8.0 nm, respectively.
- each of the optical films obtained in each Example is excellent in that the water absorption of the unstretched film is low and the thickness direction retardation change value and the dimensional change rate of the stretched film are small. It can be seen that these have the properties.
- the optical films obtained in each example all have good heat resistance, haze, total light transmittance, MIT folding resistance and impact strength, and in-plane retardation.
- the thickness direction retardation is small, it has low birefringence, high surface hardness (pencil hardness), and excellent properties such as a small absolute value of the photoelastic coefficient.
- Example 14 In a reaction kettle equipped with a stirrer, temperature sensor, cooling pipe and nitrogen gas introduction pipe, 70 parts by weight of ethyl methacrylate, 30 parts by weight of methacrylic acid, 78.8 parts by weight of toluene as a polymerization solvent and 33.8 parts by weight of methanol A mixed solvent and an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were added in an amount of 0.05 part by weight, and the temperature was raised to 73 ° C. while passing nitrogen gas through the reaction kettle.
- ADEKA trade name: ADK STAB 2112
- dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 6.4 parts by weight of toluene and 2.7 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), aging was carried out for an additional 4 hours.
- the content of repeating units derived from methacrylic acid in the (meth) acrylic resin contained in the polymer solution obtained above was 30.2% by weight. Moreover, the weight average molecular weight of the (meth) acrylic resin was 122,000.
- Vent type screw twin screw extruder having a barrel temperature of 290 ° C., a rotation speed of 160 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a rear vent number of 1, and a forevent number of 2 (Pore diameter: 15 mm, L / D: 45) Introduced at a processing rate of 420 g / h in terms of resin amount, devolatilized in this extruder, and extruded in a shaft residence time of about 3.6 minutes. A transparent (meth) acrylic resin pellet was obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 113,000, and the glass transition temperature was 109 ° C.
- the pellet obtained in the above was a barrel type screw twin screw extruder (hole diameter: 15 mm, bore temperature: 290 ° C., rotation speed: 300 rpm, reduced pressure: 13.3 to 400 hPa (10 to 300 mmHg), single vent number) L / D: 45) was introduced from the hopper at a processing rate of 420 g / h in terms of resin amount, and aniline was injected from the hopper after the hopper at a charging rate of 202 g / h. By extruding in about 2 minutes, transparent (meth) acrylic resin pellets were obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 10.11,000.
- the (meth) acrylic resin obtained above has a repeating unit in the formula (I) wherein R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group. , R 4 is a hydrogen atom, R 5 is a methyl group, R 6 is a (meth) acrylic resin having a repeating unit of an ethyl group and a glass transition temperature of 168 ° C.
- the imidation ratio of the (meth) acrylic resin obtained above was 54.6%, the content of the repeating unit represented by the formula (II) was 26.0% by weight, and the stress optical coefficient (Cr) was 0.02 ⁇ 10 ⁇ 9 Pa ⁇ 1 .
- the acid value of the (meth) acrylic resin was 0.88 mmol / g.
- the pellet obtained above is put into a single screw extruder (hole diameter: 20 mm, L / D: 25), the T die temperature is adjusted to 290 ° C., and melt extrusion is performed from a coat hanger type T die (width 150 mm). And was discharged onto a cooling roll having a roll temperature of 163 ° C. to produce an unstretched film having a thickness of 160 ⁇ m.
- the unstretched film obtained above was cut out into 96 mm ⁇ 96 mm, and successively 240 mm / min at a temperature of 188 ° C. using a biaxial stretching machine (manufactured by Toyo Seiki Seisakusho, product number: X-6S). Biaxial stretching was performed sequentially so that the stretching ratio was doubled in the order of the machine direction (MD direction) and the transverse direction (TD direction) at the stretching speed of.
- MD direction machine direction
- TD direction transverse direction
- the in-plane retardation and the thickness direction retardation of the optical film obtained above were 0.4 nm and 1.4 nm, respectively.
- Example 15 In a reaction kettle equipped with a stirrer, a temperature sensor, a cooling pipe and a nitrogen gas introduction pipe, 60 parts by weight of n-butyl methacrylate, 40 parts by weight of methacrylic acid, 67.5 parts by weight of toluene as a polymerization solvent and 45 parts by weight of methanol A mixed solvent and an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were added in an amount of 0.05 part by weight, and the temperature was raised to 73 ° C. while passing nitrogen gas through the reaction kettle.
- ADEKA trade name: ADK STAB 2112
- dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 5.5 parts by weight of toluene and 3.6 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), aging was performed for another 5 hours.
- the content of repeating units derived from methacrylic acid in the (meth) acrylic resin contained in the polymer solution obtained above was 40.1% by weight. Moreover, the weight average molecular weight of the (meth) acrylic resin was 145,000.
- the polymer solution obtained above was subjected to a vent type screw having a barrel temperature of 290 ° C., a rotation speed of 70 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a rear vent number of 1, and a forevent number of 2. It is introduced into a shaft extruder (hole diameter: 15 mm, L / D: 45) at a processing rate of 420 g / h in terms of resin amount, devolatilized in this extruder, and pushed in a shaft residence time of about 3.6 minutes. As a result, a transparent (meth) acrylic resin pellet was obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 1280, and the glass transition temperature was 98 ° C.
- the pellet obtained above was a barrel type screw twin screw extruder (hole diameter: 15 mm, bore temperature: 290 ° C., rotation speed: 300 rpm, degree of vacuum: 13.3 to 400 hPa (10 to 300 mmHg), one vent number) L / D: 45) is introduced from the hopper at a processing rate of 456 g / h in terms of resin amount, and aniline is injected from the hopper after the hopper at a feed rate of 378 g / h, and the residence time in the shaft is 5 By extruding in about 2 minutes, transparent (meth) acrylic resin pellets were obtained.
- the weight average molecular weight of the (meth) acrylic resin obtained above was 107,000.
- the (meth) acrylic resin obtained above has a repeating unit in the formula (I) wherein R 1 is a methyl group, R 2 is a hydrogen atom, and R 3 is a phenyl group. , R 4 is a hydrogen atom, R 5 is a methyl group, R 6 is a (meth) acrylic resin having a repeating unit of an n-butyl group and having a glass transition temperature of 162 ° C.
- the imidation ratio of the (meth) acrylic resin obtained above was 61.8%, the content of the repeating unit represented by the formula (II) was 22.6% by weight, and the stress optical coefficient (Cr) was 0.09 ⁇ 10 ⁇ 9 Pa ⁇ 1 .
- the acid value of the (meth) acrylic resin was 0.92 mmol / g.
- the pellet obtained above is put into a single screw extruder (hole diameter: 20 mm, L / D: 25), the T die temperature is adjusted to 285 ° C., and melt extrusion is performed from a coat hanger type T die (width 150 mm). And was discharged onto a cooling roll having a roll temperature of 155 ° C. to produce an unstretched film having a thickness of 160 ⁇ m.
- the unstretched film obtained above was cut out to 96 mm ⁇ 96 mm, and successively 240 mm / min at a temperature of 182 ° C. using a biaxial stretching machine (manufactured by Toyo Seiki Seisakusho, product number: X-6S). Biaxial stretching was performed sequentially so that the stretching ratio was doubled in the order of the machine direction (MD direction) and the transverse direction (TD direction) at the stretching speed of.
- MD direction machine direction
- TD direction transverse direction
- the in-plane retardation and the thickness direction retardation of the optical film obtained above were 1.2 nm and 6.1 nm, respectively.
- each of the optical films obtained in each Example is excellent in that the water absorption rate of the unstretched film is low and the thickness direction retardation change value and the dimensional change rate of the stretched film are small. It can be seen that these have the properties.
- the optical films obtained in each example all have good heat resistance, haze, total light transmittance, MIT folding resistance and impact strength, and in-plane retardation.
- the thickness direction retardation is small, it has low birefringence, high surface hardness (pencil hardness), and excellent properties such as a small absolute value of the photoelastic coefficient.
Abstract
Description
(1) 式(I): The present invention
(1) Formula (I):
で表わされる繰返し単位および式(II): (Wherein R 1 and R 2 are each independently a hydrogen atom or an alkyl group having 1 to 8 carbon atoms, and R 3 represents a ring structure)
Repeating units represented by the formula (II):
で表わされる繰返し単位を有する(メタ)アクリル系樹脂、
(2) (メタ)アクリル系樹脂が式(I)で表わされる繰返し単位5~85重量%および式(II)で表わされる繰返し単位15~95重量%を有する前記(1)に記載の(メタ)アクリル系樹脂、
(3) ガラス転移温度が120℃以上である前記(1)または(2)に記載の(メタ)アクリル系樹脂、
(4)応力光学係数(Cr)の絶対値が0.3×10-9Pa-1以下である前記(1)~(3)のいずれかに記載の(メタ)アクリル系樹脂、
(5) 前記式(II)で表わされる繰返し単位を有する(メタ)アクリル樹脂をイミド化剤でイミド化させる前記(1)~(4)のいずれかに記載の(メタ)アクリル系樹脂の製造方法、
(6) 前記(1)~(4)のいずれかに記載の(メタ)アクリル系樹脂を含有してなる光学フィルム、
(7) 波長590nmにおける面内位相差Reが20nm以下であり、厚さ方向位相差Rthの絶対値が20nm以下である前記(6)に記載の光学フィルム、
(8) 波長590nmの光に対する光弾性係数の絶対値が10×10-12Pa-1以下である前記(6)または(7)に記載の光学フィルム、
(9) 60~100℃における線膨張係数が80×10-6K-1以下である前記(6)~(8)のいずれかに記載の光学フィルム、
(10) 二軸延伸フィルムである前記(6)~(9)のいずれかに記載の光学フィルム、
(11) 前記(6)~(10)のいずれかに記載の光学フィルムの少なくとも一方表面に透明導電層が形成されてなる透明導電性フィルム、
(12) 前記(6)~(10)のいずれかに記載の光学フィルムを有する画像表示装置、および
(13) 前記(11)に記載の透明導電性フィルムを有する画像表示装置
に関する。 (Wherein R 4 and R 5 are each independently a hydrogen atom or an alkyl group having 1 to 8 carbon atoms, R 6 is an alkyl group having 1 to 18 carbon atoms or a cycloalkyl group having 3 to 12 carbon atoms) Or an aryl group having 6 to 10 carbon atoms)
A (meth) acrylic resin having a repeating unit represented by:
(2) The (meth) acrylic resin according to (1), wherein the (meth) acrylic resin has 5 to 85% by weight of repeating units represented by the formula (I) and 15 to 95% by weight of repeating units represented by the formula (II). ) Acrylic resin,
(3) The (meth) acrylic resin according to (1) or (2), wherein the glass transition temperature is 120 ° C. or higher.
(4) The (meth) acrylic resin according to any one of (1) to (3), wherein the absolute value of the stress optical coefficient (Cr) is 0.3 × 10 −9 Pa −1 or less,
(5) The production of the (meth) acrylic resin according to any one of (1) to (4) above, wherein the (meth) acrylic resin having the repeating unit represented by the formula (II) is imidized with an imidizing agent. Method,
(6) An optical film comprising the (meth) acrylic resin according to any one of (1) to (4),
(7) The optical film according to (6), wherein the in-plane retardation Re at a wavelength of 590 nm is 20 nm or less, and the absolute value of the thickness direction retardation Rth is 20 nm or less,
(8) The optical film according to (6) or (7), wherein the absolute value of the photoelastic coefficient with respect to light having a wavelength of 590 nm is 10 × 10 −12 Pa −1 or less,
(9) The optical film according to any one of (6) to (8), wherein the linear expansion coefficient at 60 to 100 ° C. is 80 × 10 −6 K −1 or less,
(10) The optical film according to any one of (6) to (9), which is a biaxially stretched film,
(11) A transparent conductive film in which a transparent conductive layer is formed on at least one surface of the optical film according to any one of (6) to (10),
(12) The present invention relates to an image display device having the optical film described in any one of (6) to (10), and (13) an image display device including the transparent conductive film described in (11).
で表わされる繰返し単位および式(II): (Wherein R 1 and R 2 are each independently a hydrogen atom or an alkyl group having 1 to 8 carbon atoms, and R 3 represents a ring structure)
Repeating units represented by the formula (II):
で表わされる繰返し単位を有する。 (Wherein R 4 and R 5 are each independently a hydrogen atom or an alkyl group having 1 to 8 carbon atoms, R 6 is an alkyl group having 1 to 18 carbon atoms or a cycloalkyl group having 3 to 12 carbon atoms) Or an aryl group having 6 to 10 carbon atoms)
It has a repeating unit represented by
・展開溶媒:テトラヒドロフラン〔和光純薬工業(株)製、特級〕
・溶媒流量:0.6mL/min
・標準試料:TSK標準ポリスチレン〔(株)東ソー製、商品名:PS-オリゴマーキット〕
・測定側カラム構成:ガードカラム〔(株)東ソー製、商品名:TSK-GEL super HZM-M 6.0×150を2本直列接続、(株)東ソー製、商品名:TSK-GEL super HZ-Lを1本使用
・リファレンス側カラムの構成:リファレンスカラム〔(株)東ソー製、商品名:TSK-GEL SuperH-RC 6.0×150、2本直列接続〕
・カラム温度:40℃ ・ System: Made by Tosoh Corporation, trade name: GPC system HLC-8220
・ Developing solvent: Tetrahydrofuran [Wako Pure Chemical Industries, Ltd., special grade]
・ Solvent flow rate: 0.6 mL / min
Standard sample: TSK standard polystyrene [manufactured by Tosoh Corporation, trade name: PS-oligomer kit]
Measurement side column configuration: guard column [manufactured by Tosoh Corporation, trade name: TSK-GEL super HZM-M 6.0 × 150 in series, two manufactured by Tosoh Corporation, trade name: TSK-GEL super HZ -L is used ・ Reference column configuration: Reference column [Tosoh Corporation, trade name: TSK-GEL SuperH-RC 6.0 × 150, 2 in series]
-Column temperature: 40 ° C
で表わされるモノマーを重合させることによって得ることができる。式(III)で表わされるモノマーには、本発明の目的が阻害されない範囲内で他のモノマーが含まれていてもよい。例えば、当該他のモノマーとして(メタ)アクリル酸を使用する場合、式(III)で表わされるモノマーに(メタ)アクリル酸を45重量%以下、好ましくは40重量%以下の含有率で含有させることができる。 (Wherein R 4 , R 5 and R 6 are the same as above)
It can obtain by polymerizing the monomer represented by. The monomer represented by the formula (III) may contain other monomers as long as the object of the present invention is not inhibited. For example, when (meth) acrylic acid is used as the other monomer, (meth) acrylic acid is contained in the monomer represented by formula (III) at a content of 45% by weight or less, preferably 40% by weight or less. Can do.
(1)(メタ)アクリル樹脂を溶解させることができ、イミド化に対して不活性な溶媒に当該(メタ)アクリル樹脂を溶解させ、得られた(メタ)アクリル樹脂溶液にイミド化剤を添加し、(メタ)アクリル樹脂とイミド化剤とを反応させることにより、(メタ)アクリル樹脂をイミド化剤でイミド化させる方法(バッチ式反応法)、
(2)押出機などを用いて溶融状態の(メタ)アクリル樹脂にイミド化剤を添加し、(メタ)アクリル樹脂とイミド化剤とを反応させることにより、(メタ)アクリル樹脂をイミド化させる方法(溶融混練法)
などが挙げられるが、本発明は、かかる例示のみに限定されるものではない。 Examples of the method of imidizing the (meth) acrylic resin with an imidizing agent include a known imidizing method. As a specific method for imidizing a (meth) acrylic resin with an imidizing agent, for example,
(1) A (meth) acrylic resin can be dissolved, the (meth) acrylic resin is dissolved in a solvent inert to imidization, and an imidizing agent is added to the obtained (meth) acrylic resin solution And by reacting the (meth) acrylic resin with an imidizing agent, the (meth) acrylic resin is imidized with an imidizing agent (batch reaction method),
(2) An imidizing agent is added to a molten (meth) acrylic resin using an extruder or the like, and the (meth) acrylic resin and the imidizing agent are reacted to imidize the (meth) acrylic resin. Method (melt kneading method)
However, the present invention is not limited to such examples.
(1)(メタ)アクリル系樹脂を溶解させることができ、エステル化に対して不活性な溶媒に当該(メタ)アクリル系樹脂を溶解させ、得られた(メタ)アクリル系樹脂溶液にエステル化剤を添加し、(メタ)アクリル系樹脂とエステル化剤とを反応させることにより、(メタ)アクリル系樹脂をエステル化剤でエステル化させる方法(バッチ式反応法)、
(2)押出機などを用いて溶融状態の(メタ)アクリル系樹脂にエステル化剤を添加し、(メタ)アクリル系樹脂とエステル化剤とを反応させることにより、(メタ)アクリル系樹脂をエステル化させる方法(溶融混練法)
などが挙げられるが、本発明は、かかる例示のみに限定されるものではない。 As a specific method of esterifying the (meth) acrylic resin with an esterifying agent, for example, in the same manner as the method of imidizing the (meth) acrylic resin with an imidizing agent,
(1) The (meth) acrylic resin can be dissolved, the (meth) acrylic resin is dissolved in a solvent inert to esterification, and the resulting (meth) acrylic resin solution is esterified. By adding an agent and reacting the (meth) acrylic resin with the esterifying agent to esterify the (meth) acrylic resin with the esterifying agent (batch reaction method),
(2) An esterifying agent is added to the molten (meth) acrylic resin using an extruder or the like, and the (meth) acrylic resin and the esterifying agent are reacted to thereby change the (meth) acrylic resin. Esterification method (melt kneading method)
However, the present invention is not limited to such examples.
〔面内位相差Re〕=(nx-ny)×d
〔式中、nxは波長590nmの光に対する遅相軸方向(光学フィルムの面内において最大の屈折率を示す方向)の屈折率、nyは進相軸方向(光学フィルムの面内におけるnxと垂直な方向)の屈折率、nyはフィルムの面内における進相軸方向の屈折率、dは光学フィルムの厚さ(nm)を示す〕
に基づいて求められる。 The in-plane retardation Re of the optical film is expressed by the formula:
[In-plane retardation Re] = (nx−ny) × d
[Where nx is the refractive index in the slow axis direction (the direction showing the maximum refractive index in the plane of the optical film) for light having a wavelength of 590 nm, and ny is the fast axis direction (perpendicular to nx in the plane of the optical film) The refractive index in the azimuth direction), ny is the refractive index in the fast axis direction in the plane of the film, and d is the thickness (nm) of the optical film.
Based on.
〔厚さ方向位相差Rth〕={(nx+ny)/2-nz}×d
〔式中、nxは波長590nmの光に対する遅相軸方向の屈折率、nyは進相軸方向の屈折率、nzはフィルムの厚さ方向の屈折率、dはフィルムの厚さ(nm)〕
に基づいて求められる。 Further, the thickness direction retardation Rth is expressed by the formula:
[Thickness direction retardation Rth] = {(nx + ny) / 2−nz} × d
[Where nx is the refractive index in the slow axis direction for light of wavelength 590 nm, ny is the refractive index in the fast axis direction, nz is the refractive index in the film thickness direction, and d is the film thickness (nm)].
Based on.
〔測定条件〕
・試料の大きさ:5mm×20mm(延伸方向を長辺とする)
・試料の前処理:60℃で15時間の前処理を行なった後、室温まで冷却
・測定加重:5g
・昇温速度:5℃/min In this specification, the linear expansion coefficient of the optical film at 60 to 100 ° C. is determined from 60 ° C. to 100 ° C. under the following measurement conditions using a thermomechanical measuring apparatus (manufactured by Shimadzu Corporation, product number: TMA-60). It was calculated as the slope at.
〔Measurement condition〕
・ Sample size: 5 mm × 20 mm (the long side is the stretching direction)
Sample pretreatment: After pretreatment at 60 ° C. for 15 hours, cooling to room temperature Measurement weight: 5 g
・ Raising rate: 5 ° C / min
(A)(メタ)アクリル系樹脂の調製
2L容のオートクレーブにメチルメタクリレート〔住友化学(株)製、商品名:スミペックスEX、重量平均分子量:14万〕29.5重量部、アニリン27.3重量部およびトルエン33.2重量部を仕込んだ。このオートクレーブを240℃まで昇温させ、3時間撹拌を行なうことにより、反応溶液を得た。 Example 1
(A) Preparation of (meth) acrylic resin Methyl methacrylate (manufactured by Sumitomo Chemical Co., Ltd., trade name: Sumipex EX, weight average molecular weight: 140,000) 29.5 parts by weight, aniline 27.3 parts by weight in a 2 liter autoclave Parts and 33.2 parts by weight of toluene were charged. The autoclave was heated to 240 ° C. and stirred for 3 hours to obtain a reaction solution.
(メタ)アクリル系樹脂のイミド化率は、1803cm-1付近のカルボン酸無水物基に由来する吸収と、1720cm-1付近のエステルカルボニル基に由来する吸収と、1680cm-1付近のイミドカルボニル基に由来する吸収との強度比からイミド化率を決定した。ここで、イミド化率は、全カルボニル基においてイミドカルボニル基が占める割合である。 [Imidation rate]
(Meth) imidization ratio of acrylic resin, 1803Cm the absorption derived from a carboxylic acid anhydride group in the vicinity of -1, the absorption derived from the ester carbonyl group in the vicinity of 1720 cm -1, an imide carbonyl groups near 1680 cm -1 The imidization ratio was determined from the intensity ratio with the absorption derived from. Here, the imidization rate is a ratio of imide carbonyl groups in all carbonyl groups.
(メタ)アクリル系樹脂において、式(II)で表わされる繰返し単位の含有率は、NMR測定装置(Varian社製、商品名:Unity Plus400)を用いて1H-NMRスペクトルを測定することによって求めた。 [Content of repeating unit represented by formula (II)]
In the (meth) acrylic resin, the content of the repeating unit represented by the formula (II) is determined by measuring a 1 H-NMR spectrum using an NMR measuring apparatus (trade name: Unity Plus 400, manufactured by Varian). It was.
〔式(II)で表わされる繰返し単位の含有率(重量%)〕
=[(ピーク面積A/ピーク面積B)×(2/3)×(b/167.85)×(1/100.12)]×(100/a)
に基づいて求めることができる。 For example, when R 4 of the repeating unit represented by the formula (II) is a hydrogen atom, R 5 is a methyl group, and R 6 is a methyl group (the molecular weight of the repeating unit is 100.12), the formula (II The content (% by weight) of the repeating unit represented by
[Content of repeating unit represented by formula (II) (% by weight)]
= [(Peak area A / Peak area B) × (2/3) × (b / 167.85) × (1 / 100.12)] × (100 / a)
Can be determined based on
(メタ)アクリル系樹脂の応力光学係数(Cr)は、未延伸フィルムを60mm×20mmの長方形に切り出し、1N/mm2以下の応力となるように重りを選択し、未延伸フィルムの下端に取り付けた。 [Stress optical coefficient (Cr)]
The stress optical coefficient (Cr) of the (meth) acrylic resin is obtained by cutting an unstretched film into a 60 mm × 20 mm rectangle, selecting a weight so that the stress is 1 N / mm 2 or less, and attaching it to the lower end of the unstretched film. It was.
前記で得られたペレットを単軸押出機(孔径:20mm、L/D:25)に入れ、Tダイ温度を270℃に調節し、コートハンガータイプTダイ(幅150mm)から溶融押出しを行ない、ロール温度140℃の冷却ロール上に吐出し、厚さ160μmの未延伸フィルムを作製した。 (B) Production of optical film The pellets obtained above were put into a single screw extruder (hole diameter: 20 mm, L / D: 25), the T die temperature was adjusted to 270 ° C, and the coat hanger type T die (width 150 mm) ) Was melt extruded and discharged onto a cooling roll having a roll temperature of 140 ° C. to produce an unstretched film having a thickness of 160 μm.
ヘイズおよび全光線透過率は、濁度計〔日本電色工業(株)製、品番:NDH 5000〕を用いて測定した。 (1) Haze and total light transmittance Haze and total light transmittance were measured using a turbidimeter [Nippon Denshoku Industries Co., Ltd., product number: NDH 5000].
MIT耐折度試験回数は、JIS P8115に準じて光学フィルムを縦15mm、長さ90mmに裁断し、得られた試験片を用いてMIT耐折度試験機〔テスター産業(株)製、品番:BE-201〕にて、温度23℃、相対湿度50%の雰囲気中で荷重200gを加えて測定した。 (2) MIT fold resistance test number The MIT fold resistance test number was determined by cutting an optical film into 15 mm length and 90 mm length according to JIS P8115, and using the obtained test piece, an MIT fold resistance test machine [ Measured by applying a load of 200 g in an atmosphere having a temperature of 23 ° C. and a relative humidity of 50% using a tester industry, product number: BE-201].
フィルムインパクト強度は、フィルムインパクトテスター〔テスター産業(株)製、品番:BU-302〕を用い、温度23℃、相対湿度50%の雰囲気中でASTM D3420に準じて測定した。 (3) Film impact strength The film impact strength was measured in accordance with ASTM D3420 in an atmosphere at a temperature of 23 ° C. and a relative humidity of 50% using a film impact tester [Tester Sangyo Co., Ltd., product number: BU-302]. .
JIS K5600-5-4(1999年)に準じ、鉛筆引っかき硬度試験機〔(株)安田精機製作所製〕を用い、荷重750gにて測定した。 (4) Pencil Hardness According to JIS K5600-5-4 (1999), a pencil scratch hardness tester (manufactured by Yasuda Seiki Seisakusho Co., Ltd.) was used and measured at a load of 750 g.
(A)(メタ)アクリル系樹脂の調製
実施例1において、オートクレーブの反応温度を245℃に変更したこと以外は、実施例1と同様にして(メタ)アクリル系樹脂を得た。得られた(メタ)アクリル系樹脂の重量平均分子量は10万であった。 Example 2
(A) Preparation of (meth) acrylic resin In Example 1, a (meth) acrylic resin was obtained in the same manner as in Example 1 except that the reaction temperature of the autoclave was changed to 245 ° C. The weight average molecular weight of the obtained (meth) acrylic resin was 100,000.
実施例1において、(メタ)アクリル系樹脂として前記で得られた(メタ)アクリル系樹脂を用い、Tダイ温度を280℃に、ロール温度を150℃に、延伸温度を167℃に変更したこと以外は、実施例1と同様にして厚さ40μmの光学フィルムを得た。 (B) Production of optical film In Example 1, the (meth) acrylic resin obtained above was used as the (meth) acrylic resin, the T-die temperature was 280 ° C, the roll temperature was 150 ° C, and the stretching temperature. An optical film having a thickness of 40 μm was obtained in the same manner as in Example 1 except that was changed to 167 ° C.
(A)(メタ)アクリル系樹脂の調製
実施例1において、オートクレーブの反応温度を247℃に、バレル温度を270℃に変更したこと以外は、実施例1と同様にして(メタ)アクリル系樹脂を得た。得られた(メタ)アクリル系樹脂の重量平均分子量は9万であった。 Example 3
(A) Preparation of (meth) acrylic resin (meth) acrylic resin in Example 1, except that the reaction temperature of the autoclave was changed to 247 ° C and the barrel temperature was changed to 270 ° C. Got. The obtained (meth) acrylic resin had a weight average molecular weight of 90,000.
実施例1において、(メタ)アクリル系樹脂として前記で得られた(メタ)アクリル系樹脂を用い、Tダイ温度を285℃に、ロール温度を155℃に、延伸温度を175℃に変更したこと以外は、実施例1と同様にして厚さ40μmの光学フィルムを得た。 (B) Production of optical film In Example 1, the (meth) acrylic resin obtained above was used as the (meth) acrylic resin, the T-die temperature was 285 ° C, the roll temperature was 155 ° C, and the stretching temperature. An optical film having a thickness of 40 μm was obtained in the same manner as in Example 1 except that was changed to 175 ° C.
(A)(メタ)アクリル系樹脂の調製
実施例1において、オートクレーブの反応温度を250℃に、バレル温度を270℃に変更したこと以外は、実施例1と同様にして(メタ)アクリル系樹脂を得た。得られた(メタ)アクリル系樹脂の重量平均分子量は9万であった。 Example 4
(A) Preparation of (meth) acrylic resin A (meth) acrylic resin was prepared in the same manner as in Example 1, except that the reaction temperature of the autoclave was changed to 250 ° C and the barrel temperature was changed to 270 ° C. Got. The obtained (meth) acrylic resin had a weight average molecular weight of 90,000.
実施例1において、(メタ)アクリル系樹脂として前記で得られた(メタ)アクリル系樹脂を用い、Tダイ温度を295℃に、ロール温度を165℃に、延伸温度を182℃に変更したこと以外は、実施例1と同様にして厚さ40μmの光学フィルムを得た。 (B) Production of optical film In Example 1, the (meth) acrylic resin obtained above was used as the (meth) acrylic resin, the T-die temperature was 295 ° C, the roll temperature was 165 ° C, and the stretching temperature An optical film having a thickness of 40 μm was obtained in the same manner as in Example 1 except that was changed to 182 ° C.
(A)(メタ)アクリル系樹脂の調製
実施例1で得られた(メタ)アクリル系樹脂100重量部に対して紫外線吸収剤として6,6’,6’’-(1,3,5-トリアジン-2,4,6-トリイル)トリス(3-ヘキシルオキシ-2-メチルフェノール)〔(株)ADEKA製、商品名:アデカスタブ(登録商標)LA-F70〕0.66重量部の割合で紫外線吸収剤を(メタ)アクリル系樹脂に添加し、二軸押出し機を用いて260℃で混練し、押出すことにより、透明な(メタ)アクリル系樹脂のペレットを得た。得られた(メタ)アクリル系樹脂の重量平均分子量は、10万であった。 Example 5
(A) Preparation of (meth) acrylic resin 6,6 ′, 6 ″-(1,3,5-) as an ultraviolet absorber with respect to 100 parts by weight of the (meth) acrylic resin obtained in Example 1 Triazine-2,4,6-triyl) tris (3-hexyloxy-2-methylphenol) [manufactured by ADEKA, trade name: ADK STAB (registered trademark) LA-F70], ultraviolet rays at a ratio of 0.66 parts by weight The absorbent was added to the (meth) acrylic resin, kneaded at 260 ° C. using a twin screw extruder, and extruded to obtain transparent (meth) acrylic resin pellets. The weight average molecular weight of the obtained (meth) acrylic resin was 100,000.
実施例1において、(メタ)アクリル系樹脂として前記で得られた(メタ)アクリル系樹脂を用いたこと以外は、実施例1と同様にして厚さ40μmの光学フィルムを得た。 (B) Production of optical film In Example 1, an optical film having a thickness of 40 μm was used in the same manner as in Example 1 except that the (meth) acrylic resin obtained above was used as the (meth) acrylic resin. Got.
(A)(メタ)アクリル系樹脂の調製
攪拌装置、温度センサー、冷却管および窒素ガス導入管を備えた反応釜に、メタクリル酸メチル79.4重量部、メタクリル酸20.6重量部、重合溶媒としてトルエン65.2重量部とメタノール16.3重量部との混合溶媒、および酸化防止剤〔(株)ADEKA製、商品名:アデカスタブ2112〕0.05重量部、連鎖移動剤としてn-ドデシルメルカプタン0.2重量部を仕込み、反応釜内に窒素ガスを通じながら80℃まで昇温させた。昇温に伴う還流が始まった時点で、重合開始剤としてジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.10重量部を反応釜内に添加するとともに、ジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.20重量部を2時間かけて反応釜内に滴下しながら、約80~85℃の還流下で溶液重合を行ない、ジメチル-2,2’-アゾビス(2-メチルプロピオネート)の滴下終了後に、さらに4時間かけて熟成を行なった。得られた重合体溶液に含まれる(メタ)アクリル系樹脂におけるメタクリル酸に由来の繰返し単位の含有率は、21.2重量%であった。また、当該(メタ)アクリル系樹脂の重量平均分子量は、10万であった。 Example 6
(A) Preparation of (meth) acrylic resin In a reaction kettle equipped with a stirrer, temperature sensor, cooling pipe and nitrogen gas introduction pipe, 79.4 parts by weight of methyl methacrylate, 20.6 parts by weight of methacrylic acid, polymerization solvent As a mixed solvent of 65.2 parts by weight of toluene and 16.3 parts by weight of methanol, and 0.05 parts by weight of an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112), n-dodecyl mercaptan as a chain transfer agent 0.2 part by weight was charged, and the temperature was raised to 80 ° C. while passing nitrogen gas through the reaction kettle. At the time when the reflux accompanying the temperature rise starts, dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 10 parts by weight is added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] 0.20 part by weight Was added dropwise to the reaction kettle over 2 hours, and solution polymerization was performed under reflux at about 80 to 85 ° C., and after completion of the addition of dimethyl-2,2′-azobis (2-methylpropionate), an additional 4 Aged over time. The content of repeating units derived from methacrylic acid in the (meth) acrylic resin contained in the obtained polymer solution was 21.2% by weight. Moreover, the weight average molecular weight of the (meth) acrylic resin was 100,000.
実施例1において、(メタ)アクリル系樹脂として前記で得られた(メタ)アクリル系樹脂を用い、Tダイ温度を285℃に、ロール温度を150℃に、延伸温度を169℃に変更したこと以外は、実施例1と同様にして厚さ40μmの光学フィルムを得た。 (B) Production of optical film In Example 1, the (meth) acrylic resin obtained above was used as the (meth) acrylic resin, the T-die temperature was 285 ° C, the roll temperature was 150 ° C, and the stretching temperature. Was changed to 169 ° C., and an optical film having a thickness of 40 μm was obtained in the same manner as in Example 1.
(A)(メタ)アクリル系樹脂の調製
実施例6で得られた重合体溶液をバレル温度260℃、回転数70rpm、減圧度13.3~400hPa(10~300mmHg)、リアベント数が1個、フォアベント数が2個のベントタイプスクリュー二軸押出し機(孔径:15mm、L/D:45)内に樹脂量換算で300g/hの処理速度で導入し、この押出し機内で脱揮を行ない、押出すことにより、透明な(メタ)アクリル系樹脂のペレットを得た。得られた(メタ)アクリル系樹脂の重量平均分子量は10万であり、ガラス転移温度は136℃であった。 Example 7
(A) Preparation of (meth) acrylic resin The polymer solution obtained in Example 6 was subjected to a barrel temperature of 260 ° C., a rotation speed of 70 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), and a rear vent number of 1. Introduced into a vent type screw twin screw extruder (hole diameter: 15 mm, L / D: 45) with a fore vent number of 2 at a processing speed of 300 g / h in terms of resin amount, and devolatilized in this extruder. By extrusion, transparent (meth) acrylic resin pellets were obtained. The obtained (meth) acrylic resin had a weight average molecular weight of 100,000 and a glass transition temperature of 136 ° C.
実施例1において、(メタ)アクリル系樹脂として前記で得られた(メタ)アクリル系樹脂を用い、Tダイ温度を275℃に、ロール温度を145℃に、延伸温度を163℃に変更したこと以外は、実施例1と同様にして厚さ40μmの光学フィルムを得た。 (B) Production of optical film In Example 1, the (meth) acrylic resin obtained above was used as the (meth) acrylic resin, the T-die temperature was 275 ° C, the roll temperature was 145 ° C, and the stretching temperature. An optical film having a thickness of 40 μm was obtained in the same manner as in Example 1 except that was changed to 163 ° C.
(A)(メタ)アクリル系樹脂の調製
2L容のオートクレーブにメチルメタクリレート-スチレン共重合体〔新日鉄住金化学(株)製、商品名:エスチレンMS600、重量平均分子量:13万〕16重量部、40%メチルアミン-メタノール溶液3重量部およびトルエン24重量部を仕込んだ。このオートクレーブを230℃まで昇温させ、2時間撹拌を行なった。 Comparative Example 1
(A) Preparation of (meth) acrylic resin Methyl methacrylate-styrene copolymer (manufactured by Nippon Steel & Sumikin Chemical Co., Ltd., trade name: Estyrene MS600, weight average molecular weight: 130,000) 16 parts by weight in a 2 L autoclave 3 parts by weight of a% methylamine-methanol solution and 24 parts by weight of toluene were charged. The autoclave was heated to 230 ° C. and stirred for 2 hours.
前記で得られた反応溶液をバレル温度260℃、回転数70rpm、減圧度13.3~400hPa(10~300mmHg)、リアベント数が1個、フォアベント数が2個のベントタイプスクリュー二軸押出し機(孔径:15mm、L/D:45)に樹脂量換算で300g/hの処理速度で導入し、この押出し機内で脱揮を行ない、押出すことにより、透明な樹脂のペレットを得た。得られたメチルメタクリレート-スチレン系イミド樹脂のガラス転移温度は143℃であり、重量平均分子量は9万であった。 (B) Production of optical film The reaction solution obtained above had a barrel temperature of 260 ° C., a rotation speed of 70 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a rear vent number of 1, and a forevent number of 2 Transparent resin by introducing into a vent type screw twin screw extruder (hole diameter: 15 mm, L / D: 45) at a processing rate of 300 g / h in terms of resin amount, devolatilizing and extruding in this extruder Pellets were obtained. The resulting methyl methacrylate-styrene imide resin had a glass transition temperature of 143 ° C. and a weight average molecular weight of 90,000.
樹脂のスチレン含量は、NMR測定装置〔Varian社製、商品名:Unity Plus400〕を用い、1H-NMRスペクトルを測定し、低磁場側の芳香環に由来する水素原子の面積と高磁場側の脂肪族に由来する水素原子の面積比に基づいて測定した。 [Method for measuring styrene content]
The styrene content of the resin was determined by measuring the 1 H-NMR spectrum using an NMR measurement apparatus (manufactured by Varian, trade name: Unity Plus 400), and measuring the area of hydrogen atoms derived from the aromatic ring on the low magnetic field side and the high magnetic field side. Measurement was based on the area ratio of aliphatic hydrogen atoms.
実施例1において、(メタ)アクリル系樹脂の代わりに前記で得られたメチルメタクリレート-スチレン系イミド樹脂を用い、延伸温度を158℃に変更したこと以外は、実施例1と同様にして厚さ40μmの光学フィルムを得た。 (B) Production of optical film In Example 1, except that the methyl methacrylate-styrene imide resin obtained above was used in place of the (meth) acrylic resin and the stretching temperature was changed to 158 ° C. In the same manner as in Example 1, an optical film having a thickness of 40 μm was obtained.
(A)(メタ)アクリル系樹脂の調製
比較例1において、メチルメタクリレート-スチレン共重合体をメチルメタクリレート-スチレン共重合体〔新日鉄住金化学(株)製、商品名:エスチレンMS700、重量平均分子量:13万〕に変更し、40%メチルアミン-メタノール溶液の量を3.5重量部に変更したこと以外は、比較例1と同様にしてメチルメタクリレート-スチレン系イミド樹脂を得た。得られたメチルメタクリレート-スチレン系イミド樹脂の重量平均分子量は9万であり、ガラス転移温度は152℃であった。また、当該メチルメタクリレート-スチレン系イミド樹脂のイミド化率は90.8%、応力光学係数(Cr)は0.09×10-9Pa-1であった。 Comparative Example 2
(A) Preparation of (meth) acrylic resin In Comparative Example 1, methyl methacrylate-styrene copolymer was changed to methyl methacrylate-styrene copolymer [manufactured by Nippon Steel & Sumikin Chemical Co., Ltd., trade name: Estyrene MS700, weight average molecular weight: 130,000] and a methyl methacrylate-styrene imide resin was obtained in the same manner as in Comparative Example 1 except that the amount of the 40% methylamine-methanol solution was changed to 3.5 parts by weight. The obtained methyl methacrylate-styrene imide resin had a weight average molecular weight of 90,000 and a glass transition temperature of 152 ° C. The methyl methacrylate-styrene imide resin had an imidation ratio of 90.8% and a stress optical coefficient (Cr) of 0.09 × 10 −9 Pa −1 .
比較例1において、メチルメタクリレート-スチレン系イミド樹脂として、前記で得られたメチルメタクリレート-スチレン系イミド樹脂を用い、Tダイ温度を280℃に、ロール温度を150℃に、延伸温度を167℃に変更したこと以外は、比較例1と同様にして厚さ40μmの光学フィルムを得た。 (B) Production of optical film In Comparative Example 1, the methyl methacrylate-styrene imide resin obtained above was used as the methyl methacrylate-styrene imide resin, the T-die temperature was 280 ° C, and the roll temperature was 150 ° C. An optical film having a thickness of 40 μm was obtained in the same manner as in Comparative Example 1 except that the stretching temperature was changed to 167 ° C.
(A)(メタ)アクリル系樹脂の調製
比較例1において、メチルメタクリレート-スチレン共重合体をメチルメタクリレート-スチレン共重合体〔新日鉄住金化学(株)製、商品名:エスチレンMS800、重量平均分子量:13万〕に変更し、40%メチルアミン-メタノール溶液の量を4重量部に変更したこと以外は、比較例1と同様にしてメチルメタクリレート-スチレン系イミド樹脂を得た。得られたメチルメタクリレート-スチレン系イミド樹脂の重量平均分子量は9万であり、ガラス転移温度は160℃であった。また、当該メチルメタクリレート-スチレン系イミド樹脂のイミド化率は92.6%、応力光学係数(Cr)は0.93×10-9Pa-1であった。 Comparative Example 3
(A) Preparation of (meth) acrylic resin In Comparative Example 1, methyl methacrylate-styrene copolymer was changed to methyl methacrylate-styrene copolymer [manufactured by Nippon Steel & Sumikin Chemical Co., Ltd., trade name: Estyrene MS800, weight average molecular weight: 130,000] and a methyl methacrylate-styrene imide resin was obtained in the same manner as in Comparative Example 1 except that the amount of the 40% methylamine-methanol solution was changed to 4 parts by weight. The resulting methyl methacrylate-styrene imide resin had a weight average molecular weight of 90,000 and a glass transition temperature of 160 ° C. The imidation ratio of the methyl methacrylate-styrene imide resin was 92.6%, and the stress optical coefficient (Cr) was 0.93 × 10 −9 Pa −1 .
比較例1において、メチルメタクリレート-スチレン系イミド樹脂として、前記で得られたメチルメタクリレート-スチレン系イミド樹脂を用い、Tダイ温度を285℃に、ロール温度を155℃に、延伸温度を175℃に変更したこと以外は、比較例1と同様にして厚さ40μmの光学フィルムを得た。 (B) Production of optical film In Comparative Example 1, the methyl methacrylate-styrene imide resin obtained above was used as the methyl methacrylate-styrene imide resin, the T die temperature was 285 ° C, and the roll temperature was 155 ° C. An optical film having a thickness of 40 μm was obtained in the same manner as in Comparative Example 1 except that the stretching temperature was changed to 175 ° C.
攪拌装置、温度センサー、冷却管および窒素ガス導入管を備えた反応釜に、メタクリル酸メチル79.4重量部、メタクリル酸20.6重量部、重合溶媒としてトルエン90.0重量部とメタノール22.5重量部との混合溶媒、および酸化防止剤〔(株)ADEKA製、商品名:アデカスタブ2112〕0.05重量部を仕込み、反応釜内に窒素ガスを通じながら73℃まで昇温させた。昇温に伴う還流が始まった時点で、重合開始剤としてジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.25重量部を反応釜内に添加するとともに、トルエン7.3重量部とメタノール1.8重量部との混合溶媒にジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.35重量部を溶解させた溶液を2時間かけて反応釜内に滴下しながら、約71~76℃の還流下で溶液重合を行ない、ジメチル-2,2’-アゾビス(2-メチルプロピオネート)の滴下終了後に、さらに4時間かけて熟成を行なった。 Production Example 1
In a reaction kettle equipped with a stirrer, a temperature sensor, a cooling pipe and a nitrogen gas introduction pipe, 79.4 parts by weight of methyl methacrylate, 20.6 parts by weight of methacrylic acid, 90.0 parts by weight of toluene as a polymerization solvent and 22. A mixed solvent with 5 parts by weight and 0.05 parts by weight of an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were charged, and the temperature was raised to 73 ° C. while passing nitrogen gas into the reaction kettle. At the time when the reflux accompanying the temperature rise starts, dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 7.3 parts by weight of toluene and 1.8 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), aging was carried out for an additional 4 hours.
(メタ)アクリル系樹脂の無水グルタル酸化率は、1803cm-1付近のカルボン酸無水物基に由来する吸収と、1720cm-1付近のエステルカルボニル基に由来する吸収と、1680cm-1付近のイミドカルボニル基に由来する吸収との強度比から無水グルタル酸化率を決定した。ここで、無水グルタル酸化率は、全カルボニル基においてカルボン酸無水物基が占める割合である。 [Anhydrous glutar oxidation rate]
(Meth) glutaric anhydride oxidation rate of the acrylic resin, the absorption derived from a carboxylic acid anhydride group in the vicinity of 1803cm -1, and the absorption derived from the ester carbonyl group in the vicinity of 1720 cm -1, imide carbonyl near 1680 cm -1 The anhydrous glutar oxidation rate was determined from the intensity ratio with the absorption derived from the group. Here, the anhydrous glutar oxidation rate is the ratio of carboxylic anhydride groups in all carbonyl groups.
製造例1で得られたペレットをバレル温度290℃、回転数300rpm、減圧度13.3~400hPa(10~300mmHg)、ベント数が1個のベントタイプスクリュー二軸押出し機(孔径:15mm、L/D:45)内に樹脂量換算で420g/hの処理速度でホッパーから導入し、ホッパーの後よりアニリンを液添ポンプにて101g/hの投入速度で注入し、軸内滞留時間2.1分間程度で押出すことにより、透明な(メタ)アクリル系樹脂のペレットを得た。 Example 8
The pellet obtained in Production Example 1 has a barrel temperature of 290 ° C., a rotation speed of 300 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a vent type screw twin screw extruder having a single vent (hole diameter: 15 mm, L / D: 45) is introduced from the hopper at a processing rate of 420 g / h in terms of resin amount, and aniline is injected from the hopper after the hopper at a charging rate of 101 g / h. By extruding in about 1 minute, transparent (meth) acrylic resin pellets were obtained.
(メタ)アクリル系樹脂における金属の含有量は、(メタ)アクリル系樹脂をマイクロ波試料前処理装置〔(株)マイルストーンゼネラル製、商品名:ETHOS One〕で灰化させ、得られた溶液を用いてICP発光分光分析装置〔(株)リガク製、商品名:CIROS-120〕にて金属原子の含有量を測定することによって求めた。 [Content of metal in (meth) acrylic resin]
The content of the metal in the (meth) acrylic resin was determined by ashing the (meth) acrylic resin with a microwave sample pretreatment device [trade name: ETHOS One, manufactured by Milestone General Co., Ltd.] Was obtained by measuring the content of metal atoms with an ICP emission spectroscopic analyzer [trade name: CIROS-120, manufactured by Rigaku Corporation].
攪拌装置、温度センサー、冷却管および窒素ガス導入管を備えた反応釜に、メタクリル酸メチル79.4重量部、メタクリル酸20.6重量部、重合溶媒としてトルエン90.0重量部とメタノール22.5重量部との混合溶媒、および酸化防止剤〔(株)ADEKA製、商品名:アデカスタブ2112〕0.05重量部を仕込み、反応釜内に窒素ガスを通じながら73℃まで昇温させた。昇温に伴う還流が始まった時点で、重合開始剤としてジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.25重量部を反応釜内に添加するとともに、トルエン7.3重量部とメタノール1.8重量部との混合溶媒にジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.35重量部を溶解させた溶液を2時間かけて反応釜内に滴下しながら、約71~76℃の還流下で溶液重合を行ない、ジメチル-2,2’-アゾビス(2-メチルプロピオネート)の滴下終了後に、さらに4時間かけて熟成を行なった。 Production Example 2
In a reaction kettle equipped with a stirrer, a temperature sensor, a cooling pipe and a nitrogen gas introduction pipe, 79.4 parts by weight of methyl methacrylate, 20.6 parts by weight of methacrylic acid, 90.0 parts by weight of toluene as a polymerization solvent and 22. A mixed solvent with 5 parts by weight and 0.05 parts by weight of an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were charged, and the temperature was raised to 73 ° C. while passing nitrogen gas into the reaction kettle. At the time when the reflux accompanying the temperature rise starts, dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 7.3 parts by weight of toluene and 1.8 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), aging was carried out for an additional 4 hours.
製造例2で得られたペレットをバレル温度290℃、回転数300rpm、減圧度13.3~400hPa(10~300mmHg)、ベント数が1個のベントタイプスクリュー二軸押出し機(孔径:15mm、L/D:45)内に樹脂量換算で420g/hの処理速度でホッパーから導入し、ホッパーの後よりアニリンを液添ポンプにて101g/hの投入速度で注入し、軸内滞留時間5.2分間程度で押出すことにより、透明な(メタ)アクリル系樹脂のペレットを得た。 Example 9
The pellet obtained in Production Example 2 was a vent type screw twin screw extruder (hole diameter: 15 mm, L) with a barrel temperature of 290 ° C., a rotation speed of 300 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), and a single vent. / D: 45) is introduced from the hopper at a processing rate of 420 g / h in terms of resin amount, and aniline is injected from the hopper after the hopper at a charging rate of 101 g / h. By extruding in about 2 minutes, transparent (meth) acrylic resin pellets were obtained.
攪拌装置、温度センサー、冷却管および窒素ガス導入管を備えた反応釜に、メタクリル酸メチル79.4重量部、メタクリル酸20.6重量部、重合溶媒としてトルエン90.0重量部とメタノール22.5重量部との混合溶媒、および酸化防止剤〔(株)ADEKA製、商品名:アデカスタブ2112〕0.05重量部を仕込み、反応釜内に窒素ガスを通じながら73℃まで昇温させた。昇温に伴う還流が始まった時点で、重合開始剤としてジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.25重量部を反応釜内に添加するとともに、トルエン7.3重量部とメタノール1.8重量部との混合溶媒にジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.35重量部を溶解させた溶液を2時間かけて反応釜内に滴下しながら、約71~76℃の還流下で溶液重合を行ない、ジメチル-2,2’-アゾビス(2-メチルプロピオネート)の滴下終了後に、さらに4時間かけて熟成を行なうことにより、重合体溶液を得た。 Production Example 3
In a reaction kettle equipped with a stirrer, a temperature sensor, a cooling pipe and a nitrogen gas introduction pipe, 79.4 parts by weight of methyl methacrylate, 20.6 parts by weight of methacrylic acid, 90.0 parts by weight of toluene as a polymerization solvent and 22. A mixed solvent with 5 parts by weight and 0.05 parts by weight of an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were charged, and the temperature was raised to 73 ° C. while passing nitrogen gas into the reaction kettle. At the time when the reflux accompanying the temperature rise starts, dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 7.3 parts by weight of toluene and 1.8 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), the mixture was further aged for 4 hours to obtain a polymer solution.
製造例3で得られたペレットをバレル温度290℃、回転数300rpm、減圧度13.3~400hPa(10~300mmHg)、ベント数が1個のベントタイプスクリュー二軸押出し機(孔径:15mm、L/D:45)内に樹脂量換算で432g/hの処理速度でホッパーから導入し、ホッパーの後よりアニリンを液添ポンプにて104g/hの投入速度で注入し、軸内滞留時間5.2分間程度で押出すことにより、透明な(メタ)アクリル系樹脂のペレットを得た。 Example 10
The pellet obtained in Production Example 3 was a vent type screw twin screw extruder (hole diameter: 15 mm, L) with a barrel temperature of 290 ° C., a rotation speed of 300 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), and a single vent. / D: 45) is introduced from the hopper at a treatment rate of 432 g / h in terms of resin amount, and aniline is injected from the hopper after the hopper at a feed rate of 104 g / h. By extruding in about 2 minutes, transparent (meth) acrylic resin pellets were obtained.
攪拌装置、温度センサー、冷却管および窒素ガス導入管を備えた反応釜に、メタクリル酸メチル79.4重量部、メタクリル酸20.6重量部、重合溶媒としてトルエン90.0重量部とメタノール22.5重量部との混合溶媒、および酸化防止剤〔(株)ADEKA製、商品名:アデカスタブ2112〕0.05重量部を仕込み、反応釜内に窒素ガスを通じながら73℃まで昇温させた。昇温に伴う還流が始まった時点で、重合開始剤としてジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.25重量部を反応釜内に添加するとともに、トルエン7.3重量部とメタノール1.8重量部との混合溶媒にジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.35重量部を溶解させた溶液を2時間かけて反応釜内に滴下しながら、約71~76℃の還流下で溶液重合を行ない、ジメチル-2,2’-アゾビス(2-メチルプロピオネート)の滴下終了後に、さらに4時間かけて熟成を行なうことにより、重合体溶液を得た。 Production Example 4
In a reaction kettle equipped with a stirrer, a temperature sensor, a cooling pipe and a nitrogen gas introduction pipe, 79.4 parts by weight of methyl methacrylate, 20.6 parts by weight of methacrylic acid, 90.0 parts by weight of toluene as a polymerization solvent and 22. A mixed solvent with 5 parts by weight and 0.05 parts by weight of an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were charged, and the temperature was raised to 73 ° C. while passing nitrogen gas into the reaction kettle. At the time when the reflux accompanying the temperature rise starts, dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 7.3 parts by weight of toluene and 1.8 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), the mixture was further aged for 4 hours to obtain a polymer solution.
塩化メチレン24.94gに(メタ)アクリル系樹脂0.15gを溶解させ、得られた溶液にメタノール14.85gを添加し、3時間撹拌した。その後、この溶液に1重量%フェノールフタレインエタノール溶液2滴を添加し、撹拌しながら0.1N水酸化ナトリウム水溶液を添加し、室温で1時間撹拌を継続し、0.1N水酸化ナトリウム水溶液の量をAmlとした。この溶液に0.1N塩酸を滴下し、溶液の赤紫色が消失するまでの0.1N塩酸の滴下量(Bml)を測定した。 [Method for measuring the amount of acid component (acid value) remaining in (meth) acrylic resin]
In 24.94 g of methylene chloride, 0.15 g of (meth) acrylic resin was dissolved, and 14.85 g of methanol was added to the resulting solution, followed by stirring for 3 hours. Then, 2 drops of 1 wt% phenolphthalein ethanol solution was added to this solution, 0.1N sodium hydroxide aqueous solution was added with stirring, and stirring was continued for 1 hour at room temperature. The amount was Aml. 0.1N hydrochloric acid was added dropwise to this solution, and the amount of 0.1N hydrochloric acid added until the reddish purple color of the solution disappeared (Bml) was measured.
〔(メタ)アクリル系樹脂に残存する酸成分の量(カルボキシル基および酸無水物基の合計量)(mmol/g)〕
=0.1×[(A-B)-(C-D)]/0.15
に基づいて求めた。 The amount of the acid component remaining in the (meth) acrylic resin (total amount of carboxyl group and acid anhydride group) (mmol / g) is expressed by the formula:
[Amount of acid component remaining in (meth) acrylic resin (total amount of carboxyl group and acid anhydride group) (mmol / g)]
= 0.1 × [(AB)-(CD)] / 0.15
Based on.
製造例4で得られたペレットをバレル温度260℃、回転数300rpm、減圧度13.3~400hPa(10~300mmHg)、ベント数が1個のベントタイプスクリュー二軸押出し機(孔径:15mm、L/D:45)内に樹脂量換算で420g/hの処理速度でホッパーから導入し、ホッパーの後より原料樹脂に対して炭酸ジメチル(DBC)16.0重量部とジアザビシクロウンデセン(DBU)2.0重量部との混合液を液添ポンプにて注入し、軸内滞留時間5.2分間程度で押出すことにより、透明な(メタ)アクリル系樹脂のペレットを得た。 Example 11
The pellet obtained in Production Example 4 has a barrel temperature of 260 ° C., a rotation speed of 300 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a vent type screw twin screw extruder having a single vent (hole diameter: 15 mm, L / D: 45) is introduced from the hopper at a processing rate of 420 g / h in terms of resin amount, and 16.0 parts by weight of dimethyl carbonate (DBC) and diazabicycloundecene (DBU) with respect to the raw material resin after the hopper. ) A mixed liquid of 2.0 parts by weight was injected with a liquid pump, and extruded with an in-shaft residence time of about 5.2 minutes to obtain transparent (meth) acrylic resin pellets.
手動式加熱プレス機〔(株)井元製作所製、IMC-180C型〕を用い、250℃の温度で20MPaの圧力にて樹脂ペレットを2分間溶融プレス成形し、厚さが200μmの未延伸フィルムを作製した。得られた未延伸フィルムを80℃で24時間乾燥させた後、その質量(X)を測定した。 [Water absorption rate]
Using a manual heating press machine (IMC-180C, manufactured by Imoto Seisakusho Co., Ltd.), resin pellets were melt-pressed at a pressure of 20 MPa at a temperature of 250 ° C. for 2 minutes to form an unstretched film having a thickness of 200 μm. Produced. The obtained unstretched film was dried at 80 ° C. for 24 hours, and then its mass (X) was measured.
〔吸水率(%)〕=[(Y-X)/X]×100
に基づいて求めた。 The water absorption of the unstretched film is expressed by the formula:
[Water absorption rate (%)] = [(Y−X) / X] × 100
Based on.
光学フィルムを裁断することにより、縦40mm、横40mmの正方形状のサンプル3枚を作製した。サンプルの四辺の長さ(La1、La2、La3、La4)をデジタルノギスで測定した。 [Dimensional change rate]
By cutting the optical film, three square samples having a length of 40 mm and a width of 40 mm were produced. The length of each side of the sample (La1, La2, La3, La4) was measured with a digital caliper.
〔寸法変化率(%)〕=|(Lb-La)/La|×100
(式中、Laは試験前における一辺の長さ、Lbは試験後における一片の長さを示す)
に基づいて求め、求められたサンプル3枚の各辺の寸法変化率の平均値を求め、その各辺の平均値の和を求めた後、その和を4で除することにより、光学フィルムの寸法変化率とした。 Next, the dimensional change rate at each side of the three samples is expressed by the formula:
[Dimensional change rate (%)] = | (Lb−La) / La | × 100
(In the formula, La represents the length of one side before the test, and Lb represents the length of one piece after the test)
After obtaining the average value of the dimensional change rate of each side of the three obtained samples, and obtaining the sum of the average value of each side, dividing the sum by 4 The dimensional change rate was used.
攪拌装置、温度センサー、冷却管および窒素ガス導入管を備えた反応釜に、メタクリル酸メチル79.4重量部、メタクリル酸20.6重量部、重合溶媒としてトルエン90.0重量部とメタノール22.5重量部との混合溶媒、および酸化防止剤〔(株)ADEKA製、商品名:アデカスタブ2112〕0.05重量部を仕込み、反応釜内に窒素ガスを通じながら73℃まで昇温させた。昇温に伴う還流が始まった時点で、重合開始剤としてジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.25重量部を反応釜内に添加するとともに、トルエン7.3重量部とメタノール1.8重量部との混合溶媒にジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.35重量部を溶解させた溶液を2時間かけて反応釜内に滴下しながら、約71~76℃の還流下で溶液重合を行ない、ジメチル-2,2’-アゾビス(2-メチルプロピオネート)の滴下終了後に、さらに4時間かけて熟成を行なった。 Production Example 5
In a reaction kettle equipped with a stirrer, a temperature sensor, a cooling pipe and a nitrogen gas introduction pipe, 79.4 parts by weight of methyl methacrylate, 20.6 parts by weight of methacrylic acid, 90.0 parts by weight of toluene as a polymerization solvent and 22. A mixed solvent with 5 parts by weight and 0.05 parts by weight of an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were charged, and the temperature was raised to 73 ° C. while passing nitrogen gas into the reaction kettle. At the time when the reflux accompanying the temperature rise starts, dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 7.3 parts by weight of toluene and 1.8 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), aging was carried out for an additional 4 hours.
製造例5で得られたペレットをバレル温度260℃、回転数300rpm、減圧度13.3~400hPa(10~300mmHg)、ベント数が1個のベントタイプスクリュー二軸押出し機(孔径:15mm、L/D:45)内に樹脂量換算で420g/hの処理速度でホッパーから導入し、ホッパーの後より原料樹脂に対して炭酸ジメチル(DBC)16.0重量部とジアザビシクロウンデセン(DBU)2.0重量部との混合液を液添ポンプにて注入し、軸内滞留時間5.2分間程度で押出すことにより、透明な(メタ)アクリル系樹脂のペレットを得た。前記で得られた(メタ)アクリル系樹脂の重量平均分子量は、8.6万であった。 Example 12
The pellet obtained in Production Example 5 has a barrel temperature of 260 ° C., a rotation speed of 300 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), a vent type screw twin screw extruder having a single vent (hole diameter: 15 mm, L / D: 45) is introduced from the hopper at a processing rate of 420 g / h in terms of resin amount, and 16.0 parts by weight of dimethyl carbonate (DBC) and diazabicycloundecene (DBU) with respect to the raw material resin after the hopper. ) A mixed liquid of 2.0 parts by weight was injected with a liquid pump, and extruded with an in-shaft residence time of about 5.2 minutes to obtain transparent (meth) acrylic resin pellets. The weight average molecular weight of the (meth) acrylic resin obtained above was 86,000.
攪拌装置、温度センサー、冷却管および窒素ガス導入管を備えた反応釜に、メタクリル酸メチル79.4重量部、メタクリル酸20.6重量部、重合溶媒としてトルエン90.0重量部とメタノール22.5重量部との混合溶媒、および酸化防止剤〔(株)ADEKA製、商品名:アデカスタブ2112〕0.05重量部を仕込み、反応釜内に窒素ガスを通じながら73℃まで昇温させた。昇温に伴う還流が始まった時点で、重合開始剤としてジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.25重量部を反応釜内に添加するとともに、トルエン7.3重量部とメタノール1.8重量部との混合溶媒にジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.35重量部を溶解させた溶液を2時間かけて反応釜内に滴下しながら、約71~76℃の還流下で溶液重合を行ない、ジメチル-2,2’-アゾビス(2-メチルプロピオネート)の滴下終了後に、さらに4時間かけて熟成を行なった。 Production Example 6
In a reaction kettle equipped with a stirrer, a temperature sensor, a cooling pipe and a nitrogen gas introduction pipe, 79.4 parts by weight of methyl methacrylate, 20.6 parts by weight of methacrylic acid, 90.0 parts by weight of toluene as a polymerization solvent and 22. A mixed solvent with 5 parts by weight and 0.05 parts by weight of an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were charged, and the temperature was raised to 73 ° C. while passing nitrogen gas into the reaction kettle. At the time when the reflux accompanying the temperature rise starts, dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 7.3 parts by weight of toluene and 1.8 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), aging was carried out for an additional 4 hours.
製造例6で得られたペレットをバレル温度290℃、回転数300rpm、減圧度13.3~400hPa(10~300mmHg)、ベント数が1個のベントタイプスクリュー二軸押出し機(孔径:15mm、L/D:45)内に樹脂量換算で420g/hの処理速度でホッパーから導入し、ホッパーの後より原料樹脂に対して炭酸ジメチル(DBC)16.0重量部とジアザビシクロウンデセン(DBU)2.0重量部との混合液を液添ポンプにて注入し、軸内滞留時間5.2分間程度で押出すことにより、透明な(メタ)アクリル系樹脂のペレットを得た。 Example 13
The pellet obtained in Production Example 6 was a vent type screw twin screw extruder (hole diameter: 15 mm, L) with a barrel temperature of 290 ° C., a rotation speed of 300 rpm, a degree of vacuum of 13.3 to 400 hPa (10 to 300 mmHg), and a single vent. / D: 45) is introduced from the hopper at a processing rate of 420 g / h in terms of resin amount, and 16.0 parts by weight of dimethyl carbonate (DBC) and diazabicycloundecene (DBU) with respect to the raw material resin after the hopper. ) A mixed liquid of 2.0 parts by weight was injected with a liquid pump, and extruded with an in-shaft residence time of about 5.2 minutes to obtain transparent (meth) acrylic resin pellets.
攪拌装置、温度センサー、冷却管および窒素ガス導入管を備えた反応釜に、メタクリル酸エチル70重量部、メタクリル酸30重量部、重合溶媒としてトルエン78.8重量部とメタノール33.8重量部との混合溶媒、および酸化防止剤〔(株)ADEKA製、商品名:アデカスタブ2112〕0.05重量部を仕込み、反応釜内に窒素ガスを通じながら73℃まで昇温させた。昇温に伴う還流が始まった時点で、重合開始剤としてジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.25重量部を反応釜内に添加するとともに、トルエン6.4重量部とメタノール2.7重量部との混合溶媒にジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.35重量部を溶解させた溶液を2時間かけて反応釜内に滴下しながら、約71~76℃の還流下で溶液重合を行ない、ジメチル-2,2’-アゾビス(2-メチルプロピオネート)の滴下終了後に、さらに4時間かけて熟成を行なった。 Example 14
In a reaction kettle equipped with a stirrer, temperature sensor, cooling pipe and nitrogen gas introduction pipe, 70 parts by weight of ethyl methacrylate, 30 parts by weight of methacrylic acid, 78.8 parts by weight of toluene as a polymerization solvent and 33.8 parts by weight of methanol A mixed solvent and an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were added in an amount of 0.05 part by weight, and the temperature was raised to 73 ° C. while passing nitrogen gas through the reaction kettle. At the time when the reflux accompanying the temperature rise starts, dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 6.4 parts by weight of toluene and 2.7 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), aging was carried out for an additional 4 hours.
攪拌装置、温度センサー、冷却管および窒素ガス導入管を備えた反応釜に、メタクリル酸n-ブチル60重量部、メタクリル酸40重量部、重合溶媒としてトルエン67.5重量部とメタノール45重量部との混合溶媒、および酸化防止剤〔(株)ADEKA製、商品名:アデカスタブ2112〕0.05重量部を仕込み、反応釜内に窒素ガスを通じながら73℃まで昇温させた。昇温に伴う還流が始まった時点で、重合開始剤としてジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.25重量部を反応釜内に添加するとともに、トルエン5.5重量部とメタノール3.6重量部との混合溶媒にジメチル-2,2’-アゾビス(2-メチルプロピオネート)〔和光純薬工業(株)製、商品名:V-601〕0.35重量部を溶解させた溶液を2時間かけて反応釜内に滴下しながら、約71~76℃の還流下で溶液重合を行ない、ジメチル-2,2’-アゾビス(2-メチルプロピオネート)の滴下終了後に、さらに5時間かけて熟成を行なった。 Example 15
In a reaction kettle equipped with a stirrer, a temperature sensor, a cooling pipe and a nitrogen gas introduction pipe, 60 parts by weight of n-butyl methacrylate, 40 parts by weight of methacrylic acid, 67.5 parts by weight of toluene as a polymerization solvent and 45 parts by weight of methanol A mixed solvent and an antioxidant (manufactured by ADEKA, trade name: ADK STAB 2112) were added in an amount of 0.05 part by weight, and the temperature was raised to 73 ° C. while passing nitrogen gas through the reaction kettle. At the time when the reflux accompanying the temperature rise starts, dimethyl-2,2′-azobis (2-methylpropionate) [manufactured by Wako Pure Chemical Industries, Ltd., trade name: V-601] is used as a polymerization initiator. 25 parts by weight was added to the reaction kettle, and dimethyl-2,2′-azobis (2-methylpropionate) [Wako Pure Chemical Industries, Ltd.] was added to a mixed solvent of 5.5 parts by weight of toluene and 3.6 parts by weight of methanol. (Trade name: V-601, manufactured by Kogyo Co., Ltd.) Solution polymerization was carried out under reflux at about 71 to 76 ° C. while adding 0.35 parts by weight of the solution dissolved in the reaction kettle over 2 hours. After completion of the dropwise addition of dimethyl-2,2′-azobis (2-methylpropionate), aging was performed for another 5 hours.
From the results shown in Table 7, the optical films obtained in each example all have good heat resistance, haze, total light transmittance, MIT folding resistance and impact strength, and in-plane retardation. In addition, since the thickness direction retardation is small, it has low birefringence, high surface hardness (pencil hardness), and excellent properties such as a small absolute value of the photoelastic coefficient.
Claims (13)
- 式(I):
で表わされる繰返し単位および式(II):
で表わされる繰返し単位を有する(メタ)アクリル系樹脂。 Formula (I):
Repeating units represented by the formula (II):
A (meth) acrylic resin having a repeating unit represented by: - (メタ)アクリル系樹脂が式(I)で表わされる繰返し単位5~85重量%および式(II)で表わされる繰返し単位15~95重量%を有する請求項1に記載の(メタ)アクリル系樹脂。 The (meth) acrylic resin according to claim 1, wherein the (meth) acrylic resin has 5 to 85% by weight of repeating units represented by the formula (I) and 15 to 95% by weight of repeating units represented by the formula (II). .
- ガラス転移温度が120℃以上である請求項1または2に記載の(メタ)アクリル系樹脂。 The (meth) acrylic resin according to claim 1 or 2, wherein the glass transition temperature is 120 ° C or higher.
- 応力光学係数(Cr)の絶対値が0.3×10-9Pa-1以下である請求項1~3のいずれかに記載の(メタ)アクリル系樹脂、 The (meth) acrylic resin according to any one of claims 1 to 3, wherein the absolute value of the stress optical coefficient (Cr) is 0.3 × 10 -9 Pa -1 or less.
- 式(II):
で表わされる繰返し単位を有する(メタ)アクリル樹脂をイミド化剤でイミド化させる請求項1~4のいずれかに記載の(メタ)アクリル系樹脂の製造方法。 Formula (II):
The method for producing a (meth) acrylic resin according to any one of claims 1 to 4, wherein a (meth) acrylic resin having a repeating unit represented by the formula is imidized with an imidizing agent. - 請求項1~4のいずれかに記載の(メタ)アクリル系樹脂を含有してなる光学フィルム。 An optical film comprising the (meth) acrylic resin according to any one of claims 1 to 4.
- 波長590nmにおける面内位相差Reが20nm以下であり、厚さ方向位相差Rthの絶対値が20nm以下である請求項6に記載の光学フィルム。 The optical film according to claim 6, wherein the in-plane retardation Re at a wavelength of 590 nm is 20 nm or less, and the absolute value of the thickness direction retardation Rth is 20 nm or less.
- 波長590nmの光に対する光弾性係数の絶対値が10×10-12Pa-1以下である請求項6または7に記載の光学フィルム。 The optical film according to claim 6 or 7, wherein an absolute value of a photoelastic coefficient with respect to light having a wavelength of 590 nm is 10 x 10 -12 Pa -1 or less.
- 60~100℃における線膨張係数が80×10-6K-1以下である請求項6~8のいずれかに記載の光学フィルム。 The optical film according to any one of claims 6 to 8, which has a coefficient of linear expansion at 60 to 100 ° C of 80 × 10 -6 K -1 or less.
- 二軸延伸フィルムである請求項5~8のいずれかに記載の光学フィルム。 The optical film according to any one of claims 5 to 8, which is a biaxially stretched film.
- 請求項6~10のいずれかに記載の光学フィルムの少なくとも一方表面に透明導電層が形成されてなる透明導電性フィルム。 A transparent conductive film in which a transparent conductive layer is formed on at least one surface of the optical film according to any one of claims 6 to 10.
- 請求項6~10のいずれかに記載の光学フィルムを有する画像表示装置。 An image display device comprising the optical film according to any one of claims 6 to 10.
- 請求項11に記載の透明導電性フィルムを有する画像表示装置。 An image display device comprising the transparent conductive film according to claim 11.
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JPWO2018124137A1 (en) * | 2016-12-28 | 2019-10-31 | 日本ゼオン株式会社 | Optical film and polarizing plate |
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JP2021050255A (en) * | 2019-09-20 | 2021-04-01 | 株式会社日本触媒 | Acrylic polymer and method for producing the same |
JP2021192106A (en) * | 2017-03-15 | 2021-12-16 | 株式会社カネカ | Stretched film and manufacturing method for stretched film |
WO2022145174A1 (en) * | 2020-12-28 | 2022-07-07 | 日本ゼオン株式会社 | Optical film and manufacturing method therefor |
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JP7129181B2 (en) * | 2017-03-17 | 2022-09-01 | 旭化成株式会社 | Parts for head-mounted displays |
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