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    • 1. 发明授权
    • Resin film
    • US10800912B2
    • 2020-10-13
    • US16066853
    • 2016-12-27
    • KURARAY CO., LTD.
    • Hiroshi OzawaYasuhito Kitade
    • B32B27/30C08L33/08C08L33/10C08L33/12C08J5/18C08L33/06C08L101/00B29C45/00B29K433/04B29L7/00
    • A resin film comprising a resin (A) and a multi-layered particle (B), the multi-layered particle comprising a layer (a) made of a polymer comprising 80 to 99.99% by mass of a methyl methacrylate unit, 0.01 to 2% by mass of a crosslinkable monomer unit and 0 to 19.99% by mass of additional copolymerizable monomer units, a layer (b) made of a polymer comprising 70 to 99.8% by mass of an alkyl acrylate unit, 0.2 to 10% by mass of a crosslinkable monomer unit and 0 to 29.8% by mass of additional copolymerizable monomer units, and a layer (c) made of a polymer comprising 80 to 100% by mass of a methyl methacrylate unit and 0 to 20% by mass of additional copolymerizable monomer units, wherein an amount of the layer (a) is 5 to 15 parts by mass, an amount of the layer (b) is 40 to 60 parts by mass and an amount of the layer (c) is 35 to 50 parts by mass, based on 100 parts by mass of the total amount of the layer (a), the layer (b) and the layer (c), and the layer (a), the layer (b) and the layer (c) are arranged in this order from the center of the particle toward the outer surface of the particle, and a volume-based average particle diameter is 90 to 150 nm.
    • 7. 发明申请
    • METHOD FOR PRODUCING (METH)ACRYLIC RESIN COMPOSITION
    • 生产(甲基)丙烯酸树脂组合物的方法
    • US20150158963A1
    • 2015-06-11
    • US14411735
    • 2013-06-28
    • KURARAY CO., LTD.
    • Hiroshi OzawaShouji TanakaYasuhito Kitade
    • C08F220/18
    • C08F220/18C08F2/01C08F2/02C08F2/38C08F6/005C08L33/12
    • A method of producing a (meth)acrylic resin composition. The method comprises a step of continuously feeding a reaction raw material including a chain transfer agent, a radical polymerization initiator and a monomer mixture comprising 80 to 100% by mass of methyl methacrylate and 20 to 0% by mass of an alkyl acrylate to a tank reactor through two or more feeding ports; a step of bulk polymerizing the monomer mixture in the tank reactor until a polymerization conversion of 40 to 70% by mass to prepare a reaction product; and a step of removing the monomer mixture from the reaction product. The perfect mixing time (θM [hr]) of the tank reactor, the half-life (τ1/2 [hr]) of the radical polymerization initiator at the temperature in the tank reactor, the stirring power (PV [kW/m3]) of the tank reactor, the mean residence time (θ [hr]) of the reaction raw material in the tank reactor, and the concentration (I [ppm]) of the radical polymerization initiator in the reaction raw material satisfy the following relationships: θM>τ1/2, and PV×θ×I×τ1/2
    • 一种(甲基)丙烯酸树脂组合物的制造方法。 该方法包括将含有80〜100质量%的甲基丙烯酸甲酯和20〜0质量%的丙烯酸烷基酯的反应原料连续进料到包含链转移剂,自由基聚合引发剂和单体混合物的步骤, 反应器通过两个或多个进料口; 在罐式反应器中本体聚合单体混合物直至聚合转化率为40〜70质量%以制备反应产物的步骤; 以及从反应产物中除去单体混​​合物的步骤。 罐式反应器的完美混合时间(&amp; M; hr),釜反应器温度下自由基聚合引发剂的半衰期(τ1/ 2 [hr]),搅拌功率(PV [kW / m3]),反应原料在反应釜中的平均停留时间(&amp; tt; [hr])和反应原料中自由基聚合引发剂的浓度(I [ppm])满足 以下关系:&amp; t; M>τ1/ 2,PV×&Thetas;×I×τ1/ 2 <4。
    • 8. 发明授权
    • Process for producing (meth)acrylic resin composition
    • US10184015B2
    • 2019-01-22
    • US15553714
    • 2016-02-26
    • KURARAY Co., Ltd.
    • Hiroshi OzawaYasuhito KitadeShouji Tanaka
    • C08F6/28C08F20/14C08F2/02C08F6/10C08F220/14
    • A method for producing a (meth)acrylic resin composition, comprising: continuously feeding reaction starting materials to a tank reactor, the reaction starting materials comprising a polymerizable monomer component, a chain transfer agent and a radical polymerization initiator, the polymerizable monomer component comprising 50 to 100% by mass of methyl methacrylate, 0 to 20% by mass of an acrylic acid alkyl ester and 0 to 30% by mass of an additional monomer; conducting bulk polymerization of the polymerizable monomer component at a polymerization conversion ratio of 40 to 70% by mass to obtain a liquid containing a (meth)acrylic resin; continuously feeding the resulting liquid to a vented extruder to separate volatile component from the (meth)acrylic resin; conducting distillation using an atmospheric distillation column to separate the volatile component into a high boiling fraction (C1) and a low boiling fraction (A1); and conducting distillation using a vacuum distillation column having a pressure of −50 kPaG to −101 kPaG at the top of the vacuum distillation column to separate the high boiling fraction (C1) into a high boiling fraction (C2) and a low boiling fraction (A2); reusing the low boiling fraction (A1) and the low boiling fraction (A2) as part of the reaction starting materials.