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Reactor and continuously performed with it process for preparation of ethylene glycol carbonate or propylene glycol carbonate

机译:反应器及其连续进行制备碳酸乙二醇酯或碳酸丙二醇酯的方法

摘要

A bubble column reactor is described which is characterised by a degree of slenderness as a ratio of height to diameter of 2 to 50, a feed for the ethylene glycol carbonate (EGC) or propylene glycol carbonate (PGC) already present and serving as reaction medium, at the lower end of the bubble column, one or more addition sites for the starting materials CO2 and ethylene oxide (EOX) or propylene oxide (POX) above the feed for the reaction medium, an outlet for the reaction mixture at the upper end of the bubble column, a divider attached thereto for the emerging reaction mixture for division into reaction mixture to be taken and worked up on the one hand and into reaction mixture to be recycled on the other hand and further a return line for the supply of the reaction mixture to be recycled. This bubble column reactor can be employed in an advantageous manner in a process for the continuous preparation of EGC or PGC, which is carried out in the temperature range from 100 to 200@C, in the pressure range from 5 to 200 bar and at a molar ratio of 1.01 to 1.5 mol of CO2 per mol of alkylene oxide in EGC or PGC which is already present as a reaction medium in an amount which is 7- to 350-fold the newly formed EGC or PGC.
机译:描述了一种鼓泡塔反应器,其特征在于细长度为高度与直径之比为2至50,已经存在并用作反应介质的碳酸乙二醇乙二醇酯(EGC)或碳酸丙二醇酯(PGC)的进料在鼓泡塔的下端,在反应介质进料上方的一个或多个起始原料CO2和环氧乙烷(EOX)或环氧丙烷(POX)的加成位点,在上端为反应混合物的出口在鼓泡塔的塔顶,一个连接到其上的分隔器用于流出的反应混合物,该混合物一方面被分离为待取和处理的反应混合物,另一方面被分离为要再循环的反应混合物,并且进一步具有用于供给该反应混合物的返回管线。反应混合物进行再循环。该鼓泡塔反应器可以以有利的方式用于连续制备EGC或PGC的方法中,该方法在100至200℃的温度范围,5至200巴的压力范围内和在已经作为反应介质存在的EGC或PGC中,每摩尔环氧烷烃的摩尔比为1.01至1.5摩尔CO2,是新形成的EGC或PGC的7至350倍。

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