碳酸二甲酯
酯交换
甲醇
碳酸丙烯酯
催化作用
碳酸盐
氢氧化物
化学
高压灭菌器
离子交换
无机化学
离子
有机化学
电极
物理化学
电化学
作者
Axel Pyrlik,Wolfgang F. Hoelderich,Karsten Müller,Wolfgang Arlt,Julia Strautmann,Daniela Kruse
标识
DOI:10.1016/j.apcatb.2011.09.033
摘要
The transesterification of propylene carbonate with methanol to form dimethyl carbonate has been carried out in the presence of strong basic ion exchange resins as heterogeneous catalysts at low temperatures. Experiments have been carried out in a 75 mL autoclave as well as in a continuous flow fixed bed reactor. Temperatures were varied between −20 and 40 °C without any additional pressure. The molar ratio of methanol and propylene carbonate was adjusted between 8:1 and 4:1. The ion exchange resins showed a high activity even below 0 °C when OH− is used as counter ion. Leaching tests resulted in a complete hold of the conversion after removing the catalyst. In the continuous reactor the catalysts suffered from a rather fast deactivation within one week due to the transformation of the counter ion hydroxide to carbonate. However, a regeneration of the catalyst using different basic liquids was possible resulting in a complete recovery of its catalytic activity.
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