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    • 1. 发明授权
    • Continuous solvent-free polymerization of vinyl derivatives
    • 乙烯基衍生物的连续无溶剂聚合
    • US4042768A
    • 1977-08-16
    • US603367
    • 1975-08-11
    • Ernst-Willi MullerManfred Wicke
    • Ernst-Willi MullerManfred Wicke
    • C08F2/00C08F2/02C08F12/00C08F12/08C08F212/00C08F220/00C08F220/10C08F6/26C08F220/14C08F220/42
    • C08F12/08
    • A process for the polymerization of aromatic vinyl compounds and their copolymerization with alkyl esters or nitriles of acrylic and/or methacrylic acid, wherein1. in a first stage, the monomer or monomers is or are continuously introduced at excess pressure into a first reaction zone and polymerized there to a degree of conversion of 5 - 40% by weight at a temperature of from 80.degree. to 170.degree. C;2. in a second stage, the reaction mixture is conducted at constant pressure into a second reaction zone designed for conducting highly viscous melts, the mixture flowing through this reaction zone at a rate which is 1.1 to 5 times the intrinsic rate, and polymerized there to a degree of conversion of 40 to 95% at temperatures of from 120.degree. to 250.degree. C, the excess pressure in the first and second stage being chosen so that the monomer or monomers is or are liquid, and the polymer is continuously removed from this zone with release of the pressure; and3. in a third stage, unreacted monomer is removed by evaporation, the pressure being chosen so that the monomer or monomers is or are evaporated, and the polymer is discharged as a melt.
    • 芳族乙烯基化合物聚合的方法及其与丙烯酸和/或甲基丙烯酸的烷基酯或腈的共聚合,其中1.在第一阶段,单体或单体中或连续地将其引入到第一反应区内 并且在80〜170℃的温度下,以重量的比例聚合为5〜40%的转化度; 2.在第二阶段,将反应混合物在恒定压力下进入设计用于引导高粘度熔体的第二反应区,混合物以本征速率的1.1至5倍的速率流过该反应区,并在那里聚合 在120至250℃的温度下,转化率为40-95%,选择第一和第二阶段中的过量压力使得单体或单体为液体,并且将聚合物从 该区释放压力; 3.在第三阶段,通过蒸发除去未消除的单体,压力由于单体或单体蒸发而蒸发,聚合物作为熔体被排出。