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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。
    • 5. 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.
    • 8. 发明申请
    • METHACRYLIC RESIN COMPOSITION
    • 甲基丙烯酸树脂组合物
    • US20150299449A1
    • 2015-10-22
    • US14441096
    • 2013-11-08
    • KURARAY CO., LTD.
    • Hiroshi OzawaToru Takahashi
    • C08L33/12F21V8/00
    • C08L33/12C08F220/14C08L53/00C08L2201/10C08L2203/20C08L2205/025G02B1/04G02B6/0066Y10T428/1036Y10T428/1059C08L33/10C08F2220/1825C08F2220/185
    • A methacrylic resin composition comprising 10 to 99 parts by mass of a methacrylic resin (A) comprising 80% by mass or more of a methyl methacrylate unit, and 90 to 1 part by mass of a block copolymer (B) comprising 10 to 60% by mass of a methacrylic acid ester polymer block (b1) and 90 to 40% by mass of an acrylic acid ester polymer block (b2), wherein the total of the methacrylic resin (A) and the block copolymer (B) is 100 parts by mass, wherein a weight-average molecular weight Mw(A) of the methacrylic resin (A), a maximum weight-average molecular weight Mw(b1) of the methacrylic acid ester polymer block (b1) and a maximum weight-average molecular weight Mw(b2) of the acrylic acid ester polymer block (b2) satisfy (1): 0.5≦Mw(A)/Mw(b1)≦2.5 and (2): 40000≦Mw(b2)≦120000.
    • 一种甲基丙烯酸系树脂组合物,其含有10〜99质量份含有甲基丙烯酸甲酯单元80质量%以上的甲基丙烯酸系树脂(A)和90〜1质量份的含有10〜60重量% 的甲基丙烯酸酯聚合物嵌段(b1)和90〜40质量%的丙烯酸酯聚合物嵌段(b2),其中甲基丙烯酸系树脂(A)和嵌段共聚物(B)的合计为100份 ,其中甲基丙烯酸系树脂(A)的重均分子量Mw(A),甲基丙烯酸酯聚合物嵌段(b1)的最大重均分子量Mw(b1)和最大重均分子量 丙烯酸酯聚合物嵌段(b2)的重量Mw(b2)满足(1):0.5&nlE; Mw(A)/ Mw(b1)&nlE; 2.5和(2):40000&nlE; Mw(b2)&nlE; 120000。
    • 9. 发明申请
    • (METH) ACRYLIC RESIN COMPOSITION
    • (METH)丙烯酸树脂组合物
    • US20150148508A1
    • 2015-05-28
    • US14397366
    • 2013-04-22
    • KURARAY CO., LTD.
    • Takuro NiimuraHiroyuki KonishiHiroshi OzawaHidemi KuritaHideyuki Tamura
    • C08J5/00
    • C08J5/00B29C45/0001C08F220/18C08J2333/12C08L33/12
    • A (meth)acrylic resin composition comprising not less than 99.5% by mass of (meth)acrylic resin composed of 80 to 100% by mass of a structural unit derived from methyl methacrylate and 0 to 20% by mass of a structural unit derived from acrylic acid ester, wherein a difference between YI4 and YI1 is not more than 3, in which the YI4 is a yellowness index at optical path length 200 mm of an article obtained by injection molding of the (meth)acrylic resin composition at a cylinder temperature of 280° C. and a molding cycle of 4 minutes, and the YI1 is a yellowness index at optical path length 200 mm of an article obtained by injection molding of the (meth)acrylic resin composition at a cylinder temperature of 280° C. and a molding cycle of 1 minute; and the (meth)acrylic resin composition has a melt flow rate under conditions of 230° C. and 3.8 kg load of not less than 25 g/10 min.
    • 一种(甲基)丙烯酸树脂组合物,其包含不小于99.5质量%的由(甲基)丙烯酸树脂组成的(甲基)丙烯酸树脂,其由衍生自甲基丙烯酸甲酯的结构单元为80〜100质量%,衍生自甲基丙烯酸甲酯的结构单元为0〜20质量% 丙烯酸酯,其中YI4和YI1之间的差不大于3,其中YI4是在(3)丙烯酸树脂组合物在气缸温度下注射成型获得的物品的光程长度200mm处的黄度指数 为280℃,成型周期为4分钟,YI1为在(280℃)下,在280℃的温度下注射成型(甲基)丙烯酸树脂组合物得到的制品的光程长度为200mm处的黄度指数。 和1分钟的成型周期; (甲基)丙烯酸树脂组合物在230℃,3.8kg负荷条件下的熔体流动速率不低于25g / 10分钟。