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    • 3. 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。
    • 6. 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.