首页> 外国专利> The preparation process of copper based catalysts, catalysts so prepared and production process of ethyl acetate from ethanol.

The preparation process of copper based catalysts, catalysts so prepared and production process of ethyl acetate from ethanol.

机译:铜基催化剂的制备方法,如此制备的催化剂和由乙醇制备乙酸乙酯的方法。

摘要

"The process of preparation of catalysts based on copper catalysts thus prepared and process of production of ethyl acetate from ethanol.It is described a process for preparing catalysts based on copper supported on zirconia, useful for the production of ethyl acetate from ethanol.The catalysts of the invention have an increased conversion assintu00e1tica ethanol ethyl acetate with the increase of the concentration of the species of copper oxide is reduced in low temperature.The process of obtaining ethyl acetate comprises directing a stream (2) of ethanol fresh for a reactor (7) loaded with the catalyst of the invention.Under the reaction conditions at temperatures between 180 and 360 C 198 198 C, the pressure between 1 and 2 atmospheres and factor of residence time 100 to 200 kg - catatalisador.Min / kg ethanol, obtaining a stream (8) of the product at the outlet of the reactor (7) which is cooled in a heat exchanger system (9), where it is separated the liquid product, and the product gas stream (18).The current (10). The current (10) mainly produces acetaldehyde, the current (16) and a hydrogen stream (14), which can be recycled to the reactor (7).Acetaldehyde may alternatively be stored in the tank (17).The liquid stream (18) containing the desired products and sub products are refined in (19) and the ethyl acetate product is stored in the tank (21).While the current of by-products is directed to the tank (23).
机译:“这样制备的基于铜催化剂的催化剂的制备方法和由乙醇制备乙酸乙酯的方法。它描述了一种基于氧化锆负载的铜基催化剂的制备方法,该方法可用于由乙醇制备乙酸乙酯。本发明的催化剂具有增加的转化率,随着低温下氧化铜种类浓度的增加,乙醇乙酸乙酯的转化率降低。获得乙酸乙酯的过程包括将新鲜的乙醇料流(2)引导至装有本发明催化剂的反应器(7)。在温度为180-360℃> 198.198℃的反应条件下,压力为1-2个大气压,停留时间为100-200kg。最小/千克乙醇,在反应器(7)的出口获得产物流(8),该产物流在热交换器系统(9)中冷却,在其中分离出液态产物, d产品气流(18)。气流(10)。料流(10)主要产生乙醛,料流(16)和氢气流(14),可将其循环到反应器(7)中,也可以将乙醛存储在罐(17)中,而液流(18)在步骤(19)中精制含有所需产物和副产物的)并将乙酸乙酯产物储存在罐(21)中。同时将副产物流引导至罐(23)中。

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