首页> 外国专利> Continuous preparation of unsaturated carboxylic acid anhydride comprises anhydrating aliphatic carboxylic acid anhydride with carboxylic acid in rectification column, recycling the non-reacted educt in reaction medium and collecting

Continuous preparation of unsaturated carboxylic acid anhydride comprises anhydrating aliphatic carboxylic acid anhydride with carboxylic acid in rectification column, recycling the non-reacted educt in reaction medium and collecting

机译:连续制备不饱和羧酸酐的方法包括在精馏塔中将脂肪族羧酸酐与羧酸脱水,将未反应的离析物在反应介质中再循环并收集。

摘要

Continuous preparation of unsaturated carboxylic acid anhydride (A) comprises anhydrating an aliphatic carboxylic acid anhydride with a carboxylic acid (B) in a rectification column (2) with an upper, middle and lower region, where the sump of the column contains an inert boiled oil. The educt is provided into the column in a stoichiometric ratio, where the carboxylic acid is emerging out from top of the column, as a by product, the non-reacted educt is led back into the reaction medium, and (A) is collected over the side outlet, preferably in between the middle- and lower part of the column. Continuous preparation of unsaturated carboxylic acid anhydride (A) of formula R-C(O)-O-C(O)-R comprises anhydrating an aliphatic carboxylic acid anhydride with a carboxylic acid (B) of formula R-COOH in a rectification column with an upper- (2a), middle- (2b) and lower- (2c) region, where the sump of the column contains an inert boiled oil. The educt is provided into the column in a stoichiometric ratio, where the carboxylic acid is emerging out from top of the column, as a by product, the non-reacted educt is led back into the reaction medium, and (A) is collected over the side outlet, preferably in between the middle- and lower part of the column. R : 2-12C-unsaturated organic remainder.
机译:连续制备不饱和羧酸酐(A)包括在具有上部,中部和下部区域的精馏塔(2)中将脂肪族羧酸酐与羧酸(B)进行脱水,其中塔的集水槽包含惰性沸腾的油。将离析物以化学计量比提供到塔中,其中羧酸从塔顶出来,作为副产物,未反应的离析物被引回到反应介质中,并收集(​​A)侧出口,最好在塔的中下部之间。式RC(O)-OC(O)-R的不饱和羧酸酐(A)的连续制备包括在塔顶精馏塔中将脂肪族羧酸酐与式R-COOH的羧酸(B)脱水(2a),中(2b)和下(2c)区域,其中塔的集液槽包含惰性沸腾的油。将离析物以化学计量比提供到塔中,其中羧酸从塔顶出来,作为副产物,未反应的离析物被引回到反应介质中,并收集(​​A)侧出口,最好在塔的中下部之间。 R:2-12C-不饱和有机剩余物。

著录项

  • 公开/公告号DE102006029320B3

    专利类型

  • 公开/公告日2007-10-11

    原文格式PDF

  • 申请/专利权人 ROEHM GMBH;

    申请/专利号DE20061029320

  • 发明设计人 SIEGERT HERMANN;BROELL DIRK;

    申请日2006-06-23

  • 分类号C07C51/54;C07C57/03;C07C57/04;C07C57/07;B01J29/04;B01J39/14;C07C51/56;

  • 国家 DE

  • 入库时间 2022-08-21 20:29:16

相似文献

  • 专利
  • 外文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号