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  • C08L35/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical, and containing at least one other carboxyl radical in the molecule, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Compositions of derivatives of such polymers
  • C08L35/02—Homopolymers or copolymers of esters
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  • C08F212/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
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  • C08F212/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
  • C08F212/02—Monomers containing only one unsaturated aliphatic radical
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  • C08F212/08—Styrene
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  • C08F220/00—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
  • C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
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  • C08F220/00—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
  • C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
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  • C08F220/00—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
  • C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
  • C08F220/10—Esters
  • C08F220/12—Esters of monohydric alcohols or phenols
• • C—CHEMISTRY; METALLURGY
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  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F222/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical and containing at least one other carboxyl radical in the molecule; Salts, anhydrides, esters, amides, imides, or nitriles thereof
  • C08F222/02—Acids; Metal salts or ammonium salts thereof, e.g. maleic acid or itaconic acid
• • C—CHEMISTRY; METALLURGY
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  • C08F222/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical and containing at least one other carboxyl radical in the molecule; Salts, anhydrides, esters, amides, imides, or nitriles thereof
  • C08F222/04—Anhydrides, e.g. cyclic anhydrides
  • C08F222/06—Maleic anhydride
• • C—CHEMISTRY; METALLURGY
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  • C08F24/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a heterocyclic ring containing oxygen
• • C—CHEMISTRY; METALLURGY
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  • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
  • C08J5/18—Manufacture of films or sheets
• • C—CHEMISTRY; METALLURGY
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  • C08L33/00—Compositions 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; Compositions of derivatives of such polymers
  • C08L33/04—Homopolymers or copolymers of esters
  • C08L33/06—Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, which oxygen atoms are present only as part of the carboxyl radical
• • C—CHEMISTRY; METALLURGY
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  • C08L33/00—Compositions 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; Compositions of derivatives of such polymers
  • C08L33/04—Homopolymers or copolymers of esters
  • C08L33/06—Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, which oxygen atoms are present only as part of the carboxyl radical
  • C08L33/062—Copolymers with monomers not covered by C08L33/06
  • C08L33/064—Copolymers with monomers not covered by C08L33/06 containing anhydride, COOH or COOM groups, with M being metal or onium-cation
• • C—CHEMISTRY; METALLURGY
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  • C08L33/00—Compositions 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; Compositions of derivatives of such polymers
  • C08L33/04—Homopolymers or copolymers of esters
  • C08L33/06—Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, which oxygen atoms are present only as part of the carboxyl radical
  • C08L33/08—Homopolymers or copolymers of acrylic acid esters
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L33/00—Compositions 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; Compositions of derivatives of such polymers
  • C08L33/04—Homopolymers or copolymers of esters
  • C08L33/06—Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, which oxygen atoms are present only as part of the carboxyl radical
  • C08L33/10—Homopolymers or copolymers of methacrylic acid esters
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L33/00—Compositions 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; Compositions of derivatives of such polymers
  • C08L33/04—Homopolymers or copolymers of esters
  • C08L33/06—Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, which oxygen atoms are present only as part of the carboxyl radical
  • C08L33/10—Homopolymers or copolymers of methacrylic acid esters
  • C08L33/12—Homopolymers or copolymers of methyl methacrylate
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  • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
  • C09J133/00—Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Adhesives based on derivatives of such polymers
  • C09J133/04—Homopolymers or copolymers of esters
  • C09J133/06—Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, the oxygen atom being present only as part of the carboxyl radical
• • 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
• • 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
  • C08F222/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical and containing at least one other carboxyl radical in the molecule; Salts, anhydrides, esters, amides, imides, or nitriles thereof
  • C08F222/04—Anhydrides, e.g. cyclic anhydrides
• • 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
• • 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
• • 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
  • C08J2335/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical, and containing at least one other carboxyl radical in the molecule, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Derivatives of such polymers
  • C08J2335/02—Characterised by the use of homopolymers or copolymers of esters
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2433/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers
  • C08J2433/04—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers esters
  • C08J2433/06—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers esters of esters containing only carbon, hydrogen, and oxygen, the oxygen atom being present only as part of the carboxyl radical
  • C08J2433/10—Homopolymers or copolymers of methacrylic acid esters
  • C08J2433/12—Homopolymers or copolymers of methyl methacrylate
• • 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
  • C08J2435/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical, and containing at least one other carboxyl radical in the molecule, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Derivatives of such polymers
  • C08J2435/02—Characterised by the use of homopolymers or copolymers of esters
• • C—CHEMISTRY; METALLURGY
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  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L25/00—Compositions of, homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Compositions of derivatives of such polymers
  • C08L25/02—Homopolymers or copolymers of hydrocarbons
  • C08L25/04—Homopolymers or copolymers of styrene
  • C08L25/08—Copolymers of styrene
  • C08L25/14—Copolymers of styrene with unsaturated esters

Definitions

• the present invention relates to a copolymer for improving heat resistance of a methacrylic resin, a resin composition of the copolymer for improving heat resistance of the methacrylic resin and a methacrylic resin, and a molded body made from the resin composition.
• Transparent resin is used for various purposes including parts of consumer electronics, a food container, and general goods. Recently, from the viewpoint of light weight, productivity, and cost, transparent resin has been used frequently as a retardation film, a polarizing film protecting film, an antireflection film, a diffusion board, and a light guide plate; which are used in thin liquid crystal display for substituting cathode-ray tube TV monitors or optical parts of electroluminescence elements.
• methacrylic resin For optical application, methacrylic resin has been widely used.
• methacrylic resin is superior in optical characteristics such as transparency and the like, however, it is inferior in heat resistance and the like, and thus the application of methacrylic resin was limited.
• Patent Literature 1 a copolymer resin obtained by copolymerizing methyl methacrylate, maleic anhydride, and styrene has been known (for example, Patent Literature 1).
• a copolymer resin obtained by a copolymerizing aromatic vinyl monomer, meth(acrylic) acid ester monomer, and at least one of unsaturated dicarboxylic acid imide derivative and unsaturated dicarboxylic acid anhydride monomer for example, Patent Literature 2.
• Patent Literature 2 WO 2009/031544
• Patent Literature 1 is superior in heat resistance compared with the methacrylic resin.
• the resin of Patent Literature 1 is inferior in heat stability, and thus tends to suffer so-called molding defects such as silver streak, gas burning, coloring, and air voids during molding. Therefore, the application of the resin was limited.
• Patent Literature 2 is superior in heat resistance, however, it is inferior in moldability. Therefore, molding defects such as flow marks and coloring tend to occur, resulting in limited application.
• the present invention has been made by taking the afore-mentioned circumstances into consideration.
• the present invention provides a copolymer for improving heat resistance of a methacrylic resin which can achieve preservation of excellent transparency of the methacrylic resin, improvement in heat resistance, and a molded product having excellent appearance, by adding a specified amount of the copolymer to the methacrylic resin.
• the present invention is summarized as follows.
• a copolymer for improving heat resistance of a methacrylic resin comprising:
• a resin composition comprising:
• a molded body comprising a resin composition of (4) or (5).
• the molded body of (6) being an optical part.
• the molded body of (7) being an optical film.
• the molded body of (8) being a polarizing film protecting film, a retardation film, or an antireflection film.
• a copolymer for improving heat resistance of a methacrylic resin which can achieve preservation of excellent transparency of the methacrylic resin and improvement in heat resistance, and can provide a molded product having excellent appearance, by adding the copolymer to the methacrylic resin, can be provided.
• a to B means A or more and B or less.
• aromatic vinyl monomer unit units derived from various styrene-based monomers such as styrene, o-methyl styrene, m-methyl styrene, p-methyl styrene, 2,4-dimethyl styrene, ethyl styrene, p-tert-butyl styrene, ⁇ -methyl styrene, and ⁇ -methyl-p-methyl styrene can be mentioned.
• styrene unit is preferable.
• the aromatic vinyl monomer unit can comprise one type of these units or can comprise two or more types of these units.
• (meth)acrylic acid ester monomer unit units derived from various methacrylic acid ester monomers such as methyl methacrylate, ethyl methacrylate, n-butyl methacrylate, 2-ethylhexyl methacrylate, dicyclopentanyl methacrylate, and isobornyl methacrylate; and various acrylic acid ester monomers such as methyl acrylate, ethyl acrylate, n-butyl acrylate, 2-methylhexyl acrylate, 2-ethylhexyl acrylate, and decyl acrylate can be mentioned. Among these, methyl methacrylate unit is preferable.
• the (meth)acrylic acid ester monomer unit can comprise one type of these units or can comprise two or more types of these units.
• the unsaturated dicarboxylic acid anhydride monomer unit units derived from various acid anhydride monomers such as maleic anhydride, itaconic anhydride, citraconic anhydride, and aconitic anhydride can be mentioned. Among these, maleic anhydride unit is preferable.
• the unsaturated dicarboxylic acid anhydride monomer unit can comprise one type of these units or can comprise two or more types of these units.
• the constitutional units of the copolymer according to the present invention is 45 to 85 mass % of the aromatic vinyl monomer unit, 5 to 45 mass % of the (meth)acrylic acid ester monomer unit, and 10 to 20 mass % of the unsaturated dicarboxylic acid anhydride monomer unit.
• the constitutional units of the copolymer is 50 to 80 mass % of the aromatic vinyl monomer unit, 8 to 38 mass % of the (meth)acrylic acid ester monomer unit, and 12 to 18 mass % of the unsaturated dicarboxylic acid anhydride monomer unit.
• Preferable content of the aromatic vinyl monomer unit is 85 mass % or less, since the effect of providing heat resistance to the methacrylic resin can be improved; and 80 mass % or less, since the effect of providing heat resistance can be further improved.
• Preferable content of the meth(acrylic) acid ester monomer unit is 45 mass % or less, since the heat stability can be improved and a molded product having a superior appearance can be obtained by molding the resin composition prepared by formulating the meth(acrylic) acid ester monomer unit in the methacrylic resin; and 38 mass % or less, since the heat stability can be further improved and a molded product having a further superior appearance can be obtained by molding the resin composition prepared by formulating the meth(acrylic) acid ester monomer unit in the methacrylic resin.
• Preferable content of the unsaturated dicarboxylic acid anhydride monomer unit is 20 mass % or less, since the compatibility with the methacrylic resin can be improved and a resin composition having a superior transparency and improved heat resistance can be prepared by formulating the unsaturated dicarboxylic acid anhydride monomer unit in the methacrylic resin; and 18 mass % or less, since the compatibility with the methacrylic resin can be further improved and a resin composition having a further superior transparency and improved heat resistance can be prepared by formulating the unsaturated dicarboxylic acid anhydride monomer unit in the methacrylic resin.
• preferable content of the aromatic vinyl monomer unit is 45 mass % or more, since the heat stability can be improved and a molded product having a superior appearance can be obtained by molding the resin composition prepared by formulating the aromatic vinyl monomer unit in the methacrylic resin; and 50 mass % or more, since the heat stability can be further improved and a molded product having a further superior appearance can be obtained by molding the resin composition prepared by formulating the aromatic vinyl monomer unit in the methacrylic resin.
• Preferable content of the meth(acrylic) acid ester monomer unit is 5 mass % or more, since the compatibility with the methacrylic resin can be improved and a resin composition having a superior transparency and improved heat resistance can be prepared by formulating the meth(acrylic) acid ester monomer unit in the methacrylic resin; and 8 mass % or more, since the compatibility with the methacrylic resin can be further improved and a resin composition having a further superior transparency and improved heat resistance can be prepared by formulating the meth(acrylic) acid ester monomer unit in the methacrylic resin.
• preferable content of the unsaturated dicarboxylic acid anhydride monomer unit is 10 mass % or more, since the compatibility with the methacrylic resin can be improved, a resin composition having a superior transparency can be prepared by formulating the unsaturated dicarboxylic acid anhydride monomer unit in the methacrylic resin, and the effect of providing heat resistance to the methacrylic resin can be improved; and 12 mass % or more, since the compatibility with the methacrylic resin can be further improved, a resin composition having a further superior transparency can be prepared by formulating the unsaturated dicarboxylic acid anhydride monomer unit in the methacrylic resin, and the effect of providing heat resistance to the methacrylic resin can be further improved.
• the copolymer of the present invention can contain a copolymerizable vinyl monomer unit other than the aromatic vinyl monomer unit, the (meth)acrylic acid ester monomer unit, and the unsaturated dicarboxylic acid anhydride monomer unit, by an amount which does not have an adverse effect to the effect of the present invention.
• the preferable amount is 5 mass % or less.
• the copolymerizable vinyl monomer unit units derived from vinyl cyanide monomers such as acrylonitrile and methacrylonitrile; vinyl carboxylic acid monomers such as acrylic acid and methacrylic acid; N-alkyl maleimide monomers such as N-methyl maleimide, N-ethyl maleimide, N-butyl maleimide, and N-cyclohexyl maleimide; N-aryl maleimide monomers such as N-phenyl maleimide, N-methylphenyl maleimide, and N-chlorophenyl maleimide can be mentioned.
• the copolymerizable vinyl monomer unit can comprise two or more types of these units.
• the copolymer of the present invention has a total light transmittance of 88% or more, the total light transmittance being measured in accordance with ASTM D1003 for a sample with 2 mm thickness.
• the total light transmittance is 89% or more, and more preferably 90% or more.
• the transparency of the resin composition prepared by formulating the copolymer in the methacrylic resin becomes superior.
• the total light transmittance is a measurement value obtained as follows.
• a mirror plate having a length of 90 mm, a width of 55 mm, and a thickness of 2 mm was prepared using an injection moulding machine (IS-50EPN, available from TOSHIBA MACHINE CO., LTD.), with the molding conditions of a cylinder temperature of 230° C. and a mold temperature of 40° C. Then, the mirror plate was subjected to the measurement in compliance with ASTM D1003, using a haze meter (NDH-1001DP, available from NIPPON DENSHOKU INDUSTRIES CO., LTD.).
• the copolymer of the present invention preferably has a weight average molecular weight (Mw) of 10 ⁇ 10 4 to 20 ⁇ 10 4 . More preferably, the weight average molecular weight (Mw) is 12 ⁇ 10 4 to 18 ⁇ 10 4 .
• Mw weight average molecular weight
• the weight average molecular weight (Mw) is a value converted to a molecular weight of polystyrene measured by gel permeation chromatography (GPC). The value measured is obtained by the following measuring conditions.
• the copolymer can be manufactured by known methods such as solution polymerization, bulk polymerization, and the like; and the solution polymerization is preferable.
• the solvent used in the solution polymerization is preferably nonpolymerizable, since it hardly produces by-products, and the adverse effect is less.
• the type of the solvent There is no particular limitation with respect to the type of the solvent.
• ketones such as acetone, methyl ethyl ketone, methyl isobutyl ketone, and acetophenone
• ethers such as tetrahydrofuran and 1,4-dioxane
• aromatic hydrocarbons such as toluene, ethyl benzene, xylene, and chlorobenzene
• methyl ethyl ketone and methyl isobutyl ketone are preferable.
• the addition amount of the solvent is preferably 10 to 100 parts by mass, more preferably 30 to 80 parts by mass, with respect to 100 parts by mass of the copolymer to be obtained.
• the addition amount is 10 parts by mass or more, it is preferable in view of controlling the reaction speed and the viscosity of the polymer solution.
• the addition amount is 100 parts by mass or less, it is preferable in view of obtaining the desired weight average molecular weight (Mw).
• the polymerizing process can be any one of the batch type polymerization method, semi-batch type polymerization method, and continuous polymerization method.
• the batch type polymerization method is preferable in view of obtaining the desired molecular weight range and transparency.
• radical polymerization method is preferable in view of manufacturing by a simple process with high productivity.
• polymerization initiator for example, known organic peroxides such as benzoyl peroxide, t-butyl peroxybenzoate, 1,1-bis(t-butyl peroxy)-2-methylcyclohexane, t-butyl peroxy isopropyl monocarbonate, t-butyl peroxy-2-ethylhexanoate, t-butyl peroxyacetate, dicumyl peroxide, and ethyl-3,3-di-(t-butyl peroxy)butylate; and known azo compounds such as azobisisobutyronitrile, azobiscyclohexanecarbonitrile, azobismethylpropionitrile, and azobismethylbutyronitrile; can be used. These polymerization initiators can be used by two or more types in
• the copolymer of the present invention has a total light transmittance of 88% or more, the total light transmittance being measured in accordance with ASTM D1003 for a sample with 2 mm thickness.
• the polymerization procedure so long as the copolymer satisfying the above condition is obtained.
• the polymerization need be carried out so that the composition distribution in the copolymer becomes small.
• the aromatic vinyl monomer and the unsaturated dicarboxylic acid anhydride monomer have high alternating copolymerization property, it is preferable to add the unsaturated dicarboxylic acid anhydride monomer separately so as to correspond with the polymerization speed of the aromatic vinyl monomer and the (meth)acrylic acid ester monomer.
• the polymerization speed can be controlled by adjusting polymerization temperature, polymerization period, and addition amount of the polymerization initiator. It is preferable to add the polymerization initiator separately, since the polymerization speed can be controlled easily.
• addition amount of the solvent and the addition amount of the chain transfer agent shall be adjusted in addition to the adjustment of polymerization temperature, polymerization period, and the addition amount of the polymerization initiator.
• the chain transfer agent There is no particular limitation regarding the chain transfer agent.
• known chain transfer agents such as n-dodecyl mercaptan, t-dodecyl mercaptan, and 2,4-diphenyl-4-methyl-1-pentene can be used.
• thermal stabilizers such as hindered phenol-based compounds, lactone-based compounds, phosphorus-based compounds, and sulfur-based compounds; light stabilizers such as hindered amine-based compounds and benzotriazole-based compounds; lubricants; plasticizers; colorants; anti-static agents; mineral oils; and the like can be added to the polymer solution as necessary. It is preferable that the addition amount of such additive is less than 0.2 parts by mass with respect to 100 parts by mass of the entire monomer unit. These additives can be used singly, or in a combination of two or more types.
• the method for collecting the copolymer of the present invention from the polymerization solution there is no particular limitation regarding the method for collecting the copolymer of the present invention from the polymerization solution.
• known devolatilization technique can be used.
• a method in which the polymerization solution is continuously fed to a twin-screw devolatilizing extruder using a gear pump, followed by devolatilization treatment of the polymerization solvent, unreacted monomers, and the like can be mentioned.
• the devolatilization component including the polymerization solvent, unreacted monomers, and the like can be collected by condensation using a condenser and the like. Then, the condensed solution can be purified using a distilling column, and the polymerization solvent can be recycled.
• the copolymer of the present invention thus obtained can be used as a heat resistance improving agent for the methacrylic resin.
• the method for preparing a resin composition by kneading and mixing the copolymer of the present invention and the methacrylic resin can be used.
• screw extruders such as a single screw extruder, a twin screw extruder having engaging flights and screws rotating in the same direction, a twin screw extruder having engaging flights and screws rotating in different directions, and a twin screw extruder having non-engaging or partially-engaging flights; a Banbury mixer; a ko-kneader; and a mixing mill can be mentioned.
• the resin composition prepared by the copolymer of the present invention and the methacrylic resin is preferably formulated with 5 to 50 mass % of the copolymer and 50 to 95 mass % of the methacrylic resin. By such, excellent balance can be achieved in the transparency, color phase, heat resistance, impact resistance, and moldability. More preferably, the resin composition is formulated with 10 to 30 mass % of the copolymer and 70 to 90 mass % of the methacrylic resin.
• the methacrylic resin is preferably formulated with 70 to 100 mass % of the meth(acrylic) acid ester monomer unit and 0 to 30 mass % of the aromatic vinyl monomer unit. By such, compatibility with the copolymer of the present invention can be improved, and the resin composition prepared would have excellent transparency, color phase, heat resistance, and moldability. More preferably, the methacrylic resin is formulated with 75 to 100 mass % of the meth(acrylic) acid ester monomer unit and 0 to 25 mass % of the aromatic vinyl monomer unit.
• the resin composition can be formulated with stabilizers, plasticizers, lubricants, antioxidants, ultraviolet absorbers, light stabilizers, colorants, and the like, so long as it does not adversely affect the effect of the present invention.
• the resin composition comprising the copolymer of the present invention and the methacrylic resin can achieve preservation of excellent transparency and improved heat resistance. Accordingly, the molded body made from the resin composition can be widely used also in the application where heat resistance is required. As an example of such application, car-mounted parts, parts of consumer electronics, and optical parts can be mentioned. Regarding the optical parts, the resin composition is particularly preferably used in the optical films such as a polarizing film protecting film, a retardation film, and an antireflection film.
• the in-plane phase difference (Re) calculated by the following (Equation 1) is 20 nm or less, preferably 10 nm or less, and more preferably 5 nm or less.
• the thickness phase difference (Rth) calculated by the following (Equation 2) is 50 nm or less, preferably 20 nm or less, and more preferably 5 nm or less.
• the in-plane phase difference (Re) is 20 nm or less and the thickness phase difference is 50 nm or less, it is preferable since the usage of the polarizing film protecting film for a polarizing plate of a liquid crystal display would not arise problems such as decrease in contrast of the liquid crystal display.
• nx, ny, and nz are obtained as follows.
• the direction in which the in-plane refractive index becomes largest is taken as the x-axis
• the direction perpendicular to the x-axis is taken as the y-axis
• the direction in the thickness of the film is taken as the z-axis.
• the nx, ny, and nz are each the refractive index in the x-axis direction, y-axis direction, and z-axis direction, respectively.
• d is the thickness of the film.
• the manufacturing method of the polarizing film protecting film there is no particular limitation regarding the manufacturing method of the polarizing film protecting film, and a known forming methods such as a melt extrusion film forming method and a solution casting film forming method can be used.
• a known forming methods such as a melt extrusion film forming method and a solution casting film forming method can be used.
• any forming method can be used so long as the optical anisotropy can be made small.
• a non-stretched film having a small optical anisotropy can be used as it is as the polarizing film protecting film.
• the film can be stretched to an extent complying with the desired optical anisotropy, and then the stretched film can be used as the polarizing film protecting film.
• the resin composition When the resin composition is used as a retardation film or an antireflection film, the resin composition is first molded into a film in a similar manner as the polarizing film protecting film, and then the stretching condition is adjusted to obtain the desired in-plane phase difference (Re) and the thickness phase difference (Rth).
• the stretched film When the stretched film is used as the retardation film or the antireflection film, the stretched film is often layered with another stretched film and is used as a ⁇ /2 plate to convert the vibration direction of the polarized light or a ⁇ /4 plate to convert a circularly polarized light into a linearly polarized light or to convert a linearly polarized light into a circularly polarized light. Therefore, the stretched film should have a suitable phase difference developing property; and the in-plane phase difference (Re) and the thickness phase difference (Rth) of the stretched film as well as the other stretched film to be laminated are adjusted to have a desired phase difference.
• a 20% maleic acid anhydride solution was prepared by dissolving maleic acid anhydride in methyl isobutyl ketone so that the maleic acid anhydride is contained by 20 mass %, and a 2% t-butyl peroxy-2-ethyl hexanoate solution was prepared by diluting t-butyl peroxy-2-ethyl hexanoate with methyl isobutyl ketone so that the t-butyl peroxy-2-ethyl hexanoate is contained by 2 mass %. These solutions were used in the polymerization.
• the temperature of the mixture was kept at 87° C., the 20% maleic acid anhydride solution was added separately at an addition speed of 1.8 kg/hour, and the 2% t-butyl peroxy-2-ethyl hexanoate solution was added separately at an addition speed of 375 g/hour.
• each of the solutions was added continuously for 8 hours.
• the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (30 g) was added.
• the 20% maleic acid anhydride solution was added separately keeping the addition speed of 1.8 kg/hour, and the temperature of the mixture was raised to 120° C. with a temperature raising speed of 8.25° C./hour taking 4 hours.
• the separate addition of the 20% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 18 kg.
• the mixture was kept at 120° C. for 1 hour, and the polymerization was completed.
• the polymerization solution was continuously fed to a twin-screw devolatilizing extruder using a gear pump, followed by devolatilization treatment of methyl isobutyl ketone, a small amount of unreacted monomers, and the like.
• the 20% maleic acid anhydride solution and the 2% t-butyl peroxy-2-ethyl hexanoate solution were prepared in a similar manner as A-1.
• each of the solutions was added continuously for 8 hours. Subsequently, the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (40 g) was added.
• the 20% maleic acid anhydride solution was added separately keeping the addition speed of 2.1 kg/hour, and the temperature of the mixture was raised to 120° C. with a temperature raising speed of 8° C./hour taking 4 hours. The separate addition of the 20% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 25.2 kg. After the temperature of the mixture was raised, the mixture was kept at 120° C.
• the 20% maleic acid anhydride solution and the 2% t-butyl peroxy-2-ethyl hexanoate solution were prepared in a similar manner as A-1.
• the temperature of the mixture was kept at 88° C.
• the 20% maleic acid anhydride solution was added separately at an addition speed of 2.55 kg/hour
• the 2% t-butyl peroxy-2-ethyl hexanoate solution was added separately at an addition speed of 375 g/hour.
• each of the solutions was added continuously for 8 hours.
• the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (40 g) was added.
• the 20% maleic acid anhydride solution was added separately keeping the addition speed of 2.55 kg/hour, and the temperature of the mixture was raised to 120° C. with a temperature raising speed of 8° C./hour taking 4 hours.
• the separate addition of the 20% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 30.6 kg.
• the mixture was kept at 120° C. for 1 hour, and the polymerization was completed.
• the polymerization solution was continuously fed to a twin-screw devolatilizing extruder using a gear pump, followed by devolatilization treatment of methyl isobutyl ketone, a small amount of unreacted monomers, and the like.
• the 20% maleic acid anhydride solution and the 2% t-butyl peroxy-2-ethyl hexanoate solution were prepared in a similar manner as A-1.
• the temperature of the mixture was kept at 88° C., the 20% maleic acid anhydride solution was added separately at an addition speed of 1.5 kg/hour, and the 2% t-butyl peroxy-2-ethyl hexanoate solution was added separately at an addition speed of 375 g/hour.
• each of the solutions was added continuously for 8 hours.
• the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (40 g) was added.
• the 20% maleic acid anhydride solution was added separately keeping the addition speed of 1.5 kg/hour, and the temperature of the mixture was raised to 120° C. with a temperature raising speed of 8° C./hour taking 4 hours.
• the separate addition of the 20% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 18 kg.
• the mixture was kept at 120° C. for 1 hour, and the polymerization was completed.
• the polymerization solution was continuously fed to a twin-screw devolatilizing extruder using a gear pump, followed by devolatilization treatment of methyl isobutyl ketone, a small amount of unreacted monomers, and the like.
• the 20% maleic acid anhydride solution and the 2% t-butyl peroxy-2-ethyl hexanoate solution were prepared in a similar manner as A-1.
• each of the solutions was added continuously for 8 hours. Subsequently, the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (40 g) was added.
• the 20% maleic acid anhydride solution was added separately keeping the addition speed of 2.85 kg/hour, and the temperature of the mixture was raised to 120° C. with a temperature raising speed of 8° C./hour taking 4 hours. The separate addition of the 20% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 34.2 kg. After the temperature of the mixture was raised, the mixture was kept at 120° C.
• the 20% maleic acid anhydride solution and the 2% t-butyl peroxy-2-ethyl hexanoate solution were prepared in a similar manner as A-1.
• the temperature of the mixture was kept at 88° C.
• the 20% maleic acid anhydride solution was added separately at an addition speed of 1.4 kg/hour
• methyl methacrylate was added separately at an addition speed of 56 g/hour
• the 2% t-butyl peroxy-2-ethyl hexanoate solution was added separately at an addition speed of 300 g/hour.
• each of the solutions was added continuously for 10 hours.
• the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (60 g) was added.
• the 20% maleic acid anhydride solution was added separately keeping the addition speed of 1.4 kg/hour, methyl methacrylate was added separately keeping the addition speed of 56 g/hour, and the temperature of the mixture was raised to 124° C. with a temperature raising speed of 4° C./hour taking 9 hours.
• the separate addition of the 20% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 25.2 kg, and the separate addition of methyl methacrylate was terminated when the accumulated amount of the separate addition reached 1 kg.
• the mixture was kept at 124° C. for 1 hour, and the polymerization was completed.
• the polymerization solution was continuously fed to a twin-screw devolatilizing extruder using a gear pump, followed by devolatilization treatment of methyl isobutyl ketone, a small amount of unreacted monomers, and the like. Subsequently, the resultant was extruded as a strand and was cut into pellets of the copolymer (A-6). In a similar manner as A-1, the copolymer A-6 thus obtained was subjected to measurement of composition, molecular weight, and total light transmittance. The results are shown in Table 1.
• the 20% maleic acid anhydride solution and the 2% t-butyl peroxy-2-ethyl hexanoate solution were prepared in a similar manner as A-1.
• the temperature of the mixture was kept at 88° C.
• the 20% maleic acid anhydride solution was added separately at an addition speed of 2.8 kg/hour
• styrene was added separately at an addition speed of 0.5 kg/hour
• the 2% t-butyl peroxy-2-ethyl hexanoate solution was added separately at an addition speed of 300 g/hour.
• each of the solutions was added continuously for 6 hours.
• the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (20 g) was added.
• the 20% maleic acid anhydride solution was added separately keeping the addition speed of 2.8 kg/hour
• styrene was added separately keeping the addition speed of 0.5 kg/hour
• the temperature of the mixture was raised to 118° C. with a temperature raising speed of 10° C./hour taking 3 hours.
• the separate addition of the 20% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 25.2 kg
• the separate addition of styrene was terminated when the accumulated amount of the separate addition reached 4.5 kg.
• the mixture was kept at 118° C. for 1 hour, and the polymerization was completed.
• the polymerization solution was continuously fed to a twin-screw devolatilizing extruder using a gear pump, followed by devolatilization treatment of methyl isobutyl ketone, a small amount of unreacted monomers, and the like. Subsequently, the resultant was extruded as a strand and was cut into pellets of the copolymer (A-7).
• the copolymer A-7 thus obtained was subjected to measurement of composition, molecular weight, and total light transmittance. The results are shown in Table 1.
• the 20% maleic acid anhydride solution and the 2% t-butyl peroxy-2-ethyl hexanoate solution were prepared in a similar manner as A-1.
• the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (20 g) was added.
• the 20% maleic acid anhydride solution was added separately keeping the addition speed of 1.68 kg/hour, and the temperature of the mixture was raised to 120° C. with a temperature raising speed of 6.4° C./hour taking 5 hours.
• the separate addition of the 20% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 25.2 kg. After the temperature of the mixture was raised, the mixture was kept at 120° C. for 1 hour, and the polymerization was completed.
• the polymerization solution was continuously fed to a twin-screw devolatilizing extruder using a gear pump, followed by devolatilization treatment of methyl isobutyl ketone, a small amount of unreacted monomers, and the like. Subsequently, the resultant was extruded as a strand and was cut into pellets of the copolymer (A-8).
• the copolymer A-8 thus obtained was subjected to measurement of composition, molecular weight, and total light transmittance. The results are shown in Table 1.
• the 20% maleic acid anhydride solution and the 2% t-butyl peroxy-2-ethyl hexanoate solution were prepared in a similar manner as A-1.
• each of the solutions was added continuously for 8 hours. Subsequently, the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (40 g) was added.
• the 20% maleic acid anhydride solution was added separately keeping the addition speed of 2.1 kg/hour, and the temperature of the mixture was raised to 120° C. with a temperature raising speed of 8° C./hour taking 4 hours. The separate addition of the 20% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 25.2 kg. After the temperature of the mixture was raised, the mixture was kept at 120° C.
• the 20% maleic acid anhydride solution and the 2% t-butyl peroxy-2-ethyl hexanoate solution were prepared in a similar manner as A-1.
• the temperature of the mixture was kept at 87° C., the 20% maleic acid anhydride solution was added separately at an addition speed of 0.75 kg/hour, and the 2% t-butyl peroxy-2-ethyl hexanoate solution was added separately at an addition speed of 375 g/hour.
• each of the solutions was added continuously for 12 hours.
• the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (30 g) was added.
• the 20% maleic acid anhydride solution was added separately keeping the addition speed of 0.75 kg/hour, and the temperature of the mixture was raised to 120° C. with a temperature raising speed of 8.25° C./hour taking 4 hours.
• the separate addition of the 20% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 12 kg.
• the mixture was kept at 120° C. for 1 hour, and the polymerization was completed.
• the polymerization solution was continuously fed to a twin-screw devolatilizing extruder using a gear pump, followed by devolatilization treatment of methyl isobutyl ketone, a small amount of unreacted monomers, and the like.
• the 20% maleic acid anhydride solution and the 2% t-butyl peroxy-2-ethyl hexanoate solution were prepared in a similar manner as A-1.
• each of the solutions was added continuously for 8 hours. Subsequently, the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (40 g) was added.
• the 20% maleic acid anhydride solution was added separately keeping the addition speed of 2.1 kg/hour, and the temperature of the mixture was raised to 120° C. with a temperature raising speed of 8° C./hour taking 4 hours. The separate addition of the 20% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 25.2 kg. After the temperature of the mixture was raised, the mixture was kept at 120° C.
• the 20% maleic acid anhydride solution and the 2% t-butyl peroxy-2-ethyl hexanoate solution were prepared in a similar manner as A-1.
• each of the solutions was added continuously for 6 hours. Subsequently, the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (10 g) was added.
• the 20% maleic acid anhydride solution was added separately keeping the addition speed of 2.5 kg/hour, and the temperature of the mixture was raised to 120° C. with a temperature raising speed of 16° C./hour taking 2 hours. The separate addition of the 20% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 20 kg. After the temperature of the mixture was raised, the mixture was kept at 120° C. for 1 hour, and the polymerization was completed.
• the polymerization solution was continuously fed to a twin-screw devolatilizing extruder using a gear pump, followed by devolatilization treatment of methyl isobutyl ketone, a small amount of unreacted monomers, and the like. Subsequently, the resultant was extruded as a strand and was cut into pellets of the copolymer (B-3).
• the copolymer B-3 thus obtained was subjected to measurement of composition, molecular weight, and total light transmittance. The results are shown in Table 2.
• a 10% maleic acid anhydride solution was prepared by dissolving maleic acid anhydride in methyl isobutyl ketone so that the maleic acid anhydride is contained by 10 mass %, and a 2% t-butyl peroxy-2-ethyl hexanoate solution was prepared by diluting t-butyl peroxy-2-ethyl hexanoate with methyl isobutyl ketone so that the t-butyl peroxy-2-ethyl hexanoate is contained by 2 mass %. These solutions were used in the polymerization.
• the temperature of the mixture was kept at 90° C., the 10% maleic acid anhydride solution was added separately at an addition speed of 1.5 kg/hour, and the 2% t-butyl peroxy-2-ethyl hexanoate solution was added separately at an addition speed of 300 g/hour.
• each of the solutions was added continuously for 8 hours.
• the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (40 g) was added.
• the 10% maleic acid anhydride solution was added separately keeping the addition speed of 1.5 kg/hour, and the temperature of the mixture was raised to 120° C. with a temperature raising speed of 7.5° C./hour taking 4 hours.
• the separate addition of the 10% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 18 kg.
• the mixture was kept at 120° C. for 1 hour, and the polymerization was completed.
• the polymerization solution was continuously fed to a twin-screw devolatilizing extruder using a gear pump, followed by devolatilization treatment of methyl isobutyl ketone, a small amount of unreacted monomers, and the like.
• the 20% maleic acid anhydride solution and the 2% t-butyl peroxy-2-ethyl hexanoate solution were prepared in a similar manner as A-1.
• each of the solutions was added continuously for 8 hours. Subsequently, the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (40 g) was added.
• the 20% maleic acid anhydride solution was added separately keeping the addition speed of 3.75 kg/hour, and the temperature of the mixture was raised to 120° C. with a temperature raising speed of 8° C./hour taking 4 hours. The separate addition of the 20% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 45 kg. After the temperature of the mixture was raised, the mixture was kept at 120° C.
• the 20% maleic acid anhydride solution and the 2% t-butyl peroxy-2-ethyl hexanoate solution were prepared in a similar manner as A-1.
• the temperature of the mixture was kept at 92° C.
• the 20% maleic acid anhydride solution was added separately at an addition speed of 0.76 kg/hour
• the 2% t-butyl peroxy-2-ethyl hexanoate solution was added separately at an addition speed of 250 g/hour.
• each of the solutions was added continuously for 15 hours.
• the separate addition of the 2% t-butyl peroxy-2-ethyl hexanoate solution was terminated, and t-butyl peroxy isopropyl monocarbonate (60 g) was added.
• the 20% maleic acid anhydride solution was added separately keeping the addition speed of 0.76 kg/hour, and the temperature of the mixture was raised to 128° C. with a temperature raising speed of 4° C./hour taking 9 hours.
• the separate addition of the 20% maleic acid anhydride solution was terminated when the accumulated amount of the separate addition reached 18.24 kg.
• the mixture was kept at 128° C. for 1 hour, and the polymerization was completed.
• the polymerization solution was continuously fed to a twin-screw devolatilizing extruder using a gear pump, followed by devolatilization treatment of methyl isobutyl ketone, a small amount of unreacted monomers, and the like.
• a 20 liter continuous stirred tank reactor equipped with an agitator, a 40 liter tower-type plug flow reactor, and a devolatilization tank equipped with a preheater were connected in series.
• a mixture solution comprising methyl methacrylate (98 parts by mass), ethyl acrylate (2 parts by mass), and ethyl benzene (18 parts by mass), 1,1-bis(t-butylperoxy)-cyclohexane (0.02 parts by mass, available from NOF CORPORATION as PERHEXA C), n-dodecyl mercaptan (0.3 parts by mass, available from Kao Corporation as THIOKALCOL 20), octadecyl-3-(3,5-di-t-butyl-4-hydroxyphenyl) propionate (0.1 parts by mass, available from Ciba Specialty Chemicals Inc.
• IRGANOX 1076 were added to prepare a raw material solution.
• the raw material solution was introduced into the continuous stirred tank reactor at a speed of 6 kg/hour.
• the temperature of the continuous stirred tank reactor was set to 120° C.
• the rotation number of the agitator was 200 rpm.
• the reaction solution was continuously taken out from the continuous stirred tank reactor, and was introduced into the tower-type plug flow reactor.
• the tower-type plug flow reactor was regulated to have a temperature gradient from 130° C. to 150° C. in the direction towards the flow.
• the reaction solution was heated with the preheater, while being introduced into the devolatilization tank.
• the devolatilization tank was regulated to have a temperature of 240° C.
• a 20 liter continuous stirred tank reactor equipped with an agitator, a 40 liter tower-type plug flow reactor, and a devolatilization tank equipped with a preheater were connected in series.
• a mixture solution comprising methyl methacrylate (78 parts by mass), styrene (22 parts by mass), and ethyl benzene (12 parts by mass), 1,1-bis(t-butylperoxy)-cyclohexane (0.02 parts by mass, available from NOF CORPORATION as PERHEXA C), n-dodecyl mercaptan (0.3 parts by mass, available from Kao Corporation as THIOKALCOL 20), octadecyl-3-(3,5-di-t-butyl-4-hydroxyphenyl) propionate (0.1 parts by mass, available from Ciba Specialty Chemicals Inc.
• IRGANOX 1076 were added to prepare a raw material solution.
• the raw material solution was introduced into the continuous stirred tank reactor at a speed of 6 kg/hour.
• the temperature of the continuous stirred tank reactor was set to 125° C.
• the rotation number of the agitator was 200 rpm.
• the reaction solution was continuously taken out from the continuous stirred tank reactor, and was introduced into the tower-type plug flow reactor.
• the tower-type plug flow reactor was regulated to have a temperature gradient from 130° C. to 150° C. in the direction towards the flow.
• the reaction solution was heated with the preheater, while being introduced into the devolatilization tank.
• the devolatilization tank was regulated to have a temperature of 240° C.
• copolymers (A-1) to (A-9) or the copolymers (B-1) to (B-6) were blended with the methacrylic resins (C-1) to (C-2) by the formulation ratio (mass %) provided in Table 4 and Table 5, using a Henschel mixer. Subsequently, a twin screw extruder (TEM-35B, available from TOSHIBA MACHINE CO., LTD.) was used to perform melt kneading with a cylinder temperature of 230° C., and a pelletized resin composition was obtained.
• TEM-35B available from TOSHIBA MACHINE CO., LTD.
• the resin composition was subjected to the following evaluations. The results of evaluations are shown in Table 4 and Table 5.
• the total light transmittance and the haze were measured as follows. First, a mirror plate having a length of 90 mm, a width of 55 mm, and a thickness of 2 mm was prepared using an injection molding machine (IS-50EPN, available from TOSHIBA MACHINE CO., LTD.), with the molding conditions of a cylinder temperature of 230° C. and a mold temperature of 40° C. Then, the mirror plate was subjected to the measurement in compliance with ASTM D1003, using a haze meter (NDH-1001DP, available from NIPPON DENSHOKU INDUSTRIES CO., LTD.).
• the Charpy impact strength was measured in accordance with JIS K7111-1:2006.
• the Vicat softening temperature was measured in accordance with JIS K7206:1999.
• Method 50 load: 50N, temperature raising speed 50° C./hour
• the test piece having the size of 10 mm ⁇ 10 mm and 4 mm thickness was used.
• HDT & VSP testing apparatus available from Toyo Seiki Seisaku-sho, Ltd. was used as the measuring apparatus.
• Samples of cylinder-shaped molded product having a diameter of 30 mm and a height of 50 mm were prepared by the number of 50, using an injection molding machine (IS-50EPN, available from TOSHIBA MACHINE CO., LTD.), with the molding conditions of a cylinder temperature of 230° C. and a mold temperature of 40° C. Then, number of samples having a defective appearance such as a silver streak, a flow mark, a gas burning, an air void and the like, was counted by visual observation.
• the criteria for the evaluation were as follows.
• Example 1 and 2 and Comparative Examples 1 and 2 were dried at 90° C. for 2 hours, followed by extrusion at 260° C. using a 40 mm ⁇ single screw extruder and a 300 mm width T-die to give a sheet-form melt resin.
• the sheet-form melt resin thus obtained was crimped with a flexible roll, and was cooled with a cooling roll. Accordingly, a film having a width of 250 mm and a thickness of 100 ⁇ 5 ⁇ m was obtained. The following evaluation was performed with the film obtained. Results of the evaluation are shown in Table 6.
• Test pieces were cut out from the non-stretched film. Falling ball impact test was conducted with the test pieces in accordance with the following conditions, and the impact energy at which 50% of the test pieces broke was measured.
• Test Piece non-stretched film having the size of 50 mm length ⁇ 50 mm width ⁇ 100 ⁇ 5 ⁇ m thickness
• Plumb Bob iron ball of 11 mm diameter, 5.45 g weight
• the film was pinched with a ring (inner diameter: 43 mm), and was fixed by 4 clips placed at upper, lower, left, and right positions.
• the non-stretched film was stretched in accordance with the following conditions.
• Test Piece non-stretched film having the size of 90 mm ⁇ 90 mm ⁇ 100 ⁇ 5 ⁇ m thickness
• the in-plane phase difference Re(590) and the thickness phase difference Rth were measured with the non-stretched film and the stretched film, by using the apparatus described below. Here, the ones which broke during the stretching due to lack of film strength were determined as unacceptable, since they were unmeasureable.
• a copolymer for improving heat resistance of a methacrylic resin which can achieve preservation of excellent transparency of the methacrylic resin and improvement in heat resistance, and can provide a molded product having excellent appearance, by adding the copolymer to the methacrylic resin, can be provided.

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