首页> 外国专利> PROCESS AND APPARATUS FOR THE PRODUCTION OF CARBOXYLIC ACID ESTERS USING AN ION-EXCHANGE RESIN IN THE ESTERIFICATION ZONE

PROCESS AND APPARATUS FOR THE PRODUCTION OF CARBOXYLIC ACID ESTERS USING AN ION-EXCHANGE RESIN IN THE ESTERIFICATION ZONE

机译:在酯化区中使用离子交换树脂生产羧酸酯的方法和装置

摘要

Esterification is carried out in a column reactor (14) in which there is a plurality of esterification trays (15) each having predetermined liquid hold-up and containing a charge of a solid esterification catalyst thereon. e.g. an ion exchange resin containing a -SO3H and/or -COOH groups. A liquid phase containing the carboxylic acid component, e.g. a fatty acid mixture, flows down the column reactor from one esterification tray to the next downward one against an upflowing alcohol vapour stream, e.g. methanol vapour. Relatively dry alcohol vapour is injected (21) into the bottom of the column reactor. Water of esterification is removed from the top of the column reactor in the vapour stream (26), whilst ester product is recovered (23) from the sump of the reactor. As the liquid flows down the trays it encounters progressively drier alocohol and the esterification equilibrium reaction is driven further and further towards 100% ester formation. A polishing reactor (304) operated under liquid phase conditions may follow the column reactor, the ester-containing product from which is mixed with further alcohol before admission to the polishing reactor.
机译:酯化在塔式反应器(14)中进行,其中有多个酯化塔板(15),每个酯化塔板(15)具有预定的液体滞留量,并在其上包含一定量的固体酯化催化剂。例如含有-SO 3 H和/或-COOH基团的离子交换树脂。含有羧酸组分的液相,例如一种脂肪酸混合物,在塔式反应器中从一个酯化塔板向下流到下一个向下的酯化塔板上,逆着一个向上流动的醇蒸气流,例如。甲醇蒸气。将相对干燥的醇蒸气注入(21)到塔反应器的底部。从蒸气流(26)中的塔式反应器的顶部除去酯化水,同时从反应器的池中回收酯产物(23)。当液体向下流过塔板时,它会遇到逐渐干燥的酒精,并且酯化平衡反应越来越快地朝着100%的酯形成方向发展。在液相条件下操作的抛光反应器(304)可以在柱反应器之后,在进入抛光反应器之前,将含酯的产物与另外的醇混合。

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