首页> 外国专利> Preparing alkyl ester of (meth)acrylic acid comprises supplying (meth)acrylic acid, alkanol and catalyst to reaction zone, adding discharged mixture to separation unit, initiating the ester into rectification unit and isolating streams

Preparing alkyl ester of (meth)acrylic acid comprises supplying (meth)acrylic acid, alkanol and catalyst to reaction zone, adding discharged mixture to separation unit, initiating the ester into rectification unit and isolating streams

机译:制备(甲基)丙烯酸的烷基酯包括将(甲基)丙烯酸,链烷醇和催化剂供应至反应区,将排出的混合物添加至分离单元,将酯引发至精馏单元中并分离物流。

摘要

Continuous preparation of alkyl ester of (meth)acrylic acid (A) comprises supplying (meth)acrylic acid, 1-5C alkanol and acid esterifying catalyst (a) to a reaction zone (5,6), adding the discharged reaction mixture from the zone to a catalyst separation unit (V), separating depleted main stream (56) and depleted sump stream (54) of (A) and (a), initiating (A) containing main stream into a rectification unit (I) and isolating streams of (A). Continuous preparation of alkyl ester of (meth) acrylic acid (A) comprises reaction of (meth) acrylic acid and 1-5C alkanol in homogeneous, liquid, solvent-free phase with increased temperature and in presence of a acidic esterifying catalyst, where (meth)acrylic acid, alkanol and acid esterified catalyst are supplied to a reaction zone (5,6) (that water formed during a retention time are separated rectificative as a component of a alkanol comprising mixture in one of the reaction zone mounted rectification unit (III), in which obtained distillate is isolated in a alkanol containing organic and a water containing aqueous phase, the organic phase is led back into the rectification unit (III) and the aqueous phase is removed, and a reaction mixture (21) are discharged from the reaction zone), where the reaction mixture discharged from the reaction zone is added to a catalyst separation unit (V) and the alkyl ester of (meth)acrylic acid containing in and at acidic esterified catalyst depleted main stream (56) and the predominant part of the acid esterified catalyst containing and at water depleted sump stream (54) are separated in the catalyst separation unit (V) and alkyl ester of (meth)acrylic acid containing main stream is initiated into a rectification unit (I) and the alkyl ester of (meth)acrylic acid containing in main stream (23) and a sump stream (52) are isolated under addition of water.
机译:连续制备(甲基)丙烯酸的烷基酯(A)包括将(甲基)丙烯酸,1-5C链烷醇和酸酯化催化剂(a)供应至反应区(5,6),从反应区中加入排出的反应混合物。区域到达催化剂分离单元(V),分离(A)和(a)的贫化主流(56)和贫化废液流(54),将包含主流的(A)引入精馏单元(I)并分离物流(A)。 (甲基)丙烯酸(A)的烷基酯的连续制备包括在升高的温度和酸性酯化催化剂的存在下,(甲基)丙烯酸与1-5C链烷醇在均相,液态,无溶剂相中在升高的温度下反应,其中(将甲基)丙烯酸,链烷醇和酸酯化的催化剂供应至反应区(5,6)(在保留时间内形成的水在安装于反应区的精馏单元之一中作为构成链烷醇的成分的精馏分离出来。 III),其中将得到的馏出物分离在含有机链烷醇和含水水相中,将有机相引回到精馏单元(III)中,除去水相,并排出反应混合物(21)从反应区排出的反应混合物,其中从反应区排出的反应混合物被加入到催化剂分离单元(V)中,并且在酸性酯化催化剂中和在酸性酯化催化剂处含有(甲基)丙烯酸的烷基酯。进料的主流(56)和含有贫化的水的污水流(54)的大部分的酯化的催化剂在催化剂分离单元(V)中分离,含(甲基)丙烯酸的主流的烷基酯被引发成在加水的情况下,分离出精馏单元(I)和主流(23)和污水流(52)中所含的(甲基)丙烯酸的烷基酯。

著录项

  • 公开/公告号DE102005010588A1

    专利类型

  • 公开/公告日2006-05-24

    原文格式PDF

  • 申请/专利权人 BASF AG;

    申请/专利号DE20051010588

  • 申请日2005-03-08

  • 分类号C07C67/54;C07C67/08;C07C69/54;

  • 国家 DE

  • 入库时间 2022-08-21 21:20:24

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