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    • 3. 发明申请
    • PROCESS FOR PREPARING ALKYL ESTERS OF (METH)ACRYLIC ACID
    • (甲基)丙烯酸的烷基酯的制备方法
    • US20060205972A1
    • 2006-09-14
    • US11276601
    • 2006-03-07
    • Anthony CLYMOArmin DIEFENBACHERThorsten FRIESEHans MARTAN
    • Anthony CLYMOArmin DIEFENBACHERThorsten FRIESEHans MARTAN
    • C07C69/52
    • C07C67/08C07C67/54C07C69/54
    • A process is described for continuously preparing alkyl esters of (meth)acrylic acid by reacting (meth)acrylic acid and alkanols having from 1 to 5 carbon atoms in homogeneous, liquid, solvent-free phase at elevated temperature and in the presence of an acidic esterification catalyst, in which the (meth)acrylic acid, the alkanol and the acidic esterification catalyst are fed to a reaction zone (5, 6), the water formed during a residence time is removed rectificatively as a constituent of an alkanol-comprising mixture in a rectification unit III attached to the reaction zone (5, 6), the distillate obtained here is separated into an alkanol-comprising organic phase and a water-comprising aqueous phase, the organic phase is recycled into the rectification unit III and the aqueous phase is discharged, and a reaction mixture (21) is discharged from the reaction zone (5, 6), which comprises feeding the reaction mixture (21) discharged from the reaction zone (5, 6) to a catalyst removal unit V and separating it in the catalyst removal unit V into a top stream (56) comprising the alkyl ester of (meth)acrylic acid and depleted in acidic esterification catalyst, and a bottom stream (54) comprising the predominant portion of the acidic esterification catalyst and depleted in water, and introducing the top stream (56) comprising the alkyl ester of (meth)acrylic acid into a rectification unit I and, with addition of water, separating it into a top stream (23) comprising the alkyl ester of (meth)acrylic acid, and a bottom stream (52).
    • 描述了一种通过使(甲基)丙烯酸和具有1至5个碳原子的链烷醇在均相,液体,无溶剂相中在升高的温度和酸性存在下连续制备(甲基)丙烯酸的烷基酯的方法 其中将(甲基)丙烯酸,链烷醇和酸性酯化催化剂加入到反应区(5,6)中,在停留时间内形成的水作为含链烷醇的混合物的组分被精馏除去 在连接到反应区(5,6)的精馏单元III中,将此处获得的馏出物分离成含链烷醇的有机相和含水的水相,将有机相再循环到精馏单元III中, 将反应混合物(21)从反应区(5,6)排出,其中包括将从反应区(5,6)排出的反应混合物(21)进料到催化剂r 表示单元V并将其在催化剂去除单元V中分离成包含(甲基)丙烯酸的烷基酯和贫化的酸性酯化催化剂的顶部流(56),以及包含主要部分酸性的底部流(54) 酯化催化剂和耗尽水,并将包含(甲基)丙烯酸的烷基酯的顶部流(56)引入精馏单元I中,并加入水将其分离成包含烷基酯的顶部流(23) 的(甲基)丙烯酸和底部流(52)。