反应蒸馏
二氧环烷
间歇精馏
蒸馏
乙二醇
化学
化学工程
水溶液
沸点
连续蒸馏
甲醛
共沸蒸馏
阳离子聚合
工艺工程
分馏塔
材料科学
有机化学
分馏
工程类
作者
Hong Li,Chuanhui Wu,Qingyu Zhang,Xingang Li,Xin Gao
标识
DOI:10.1021/acs.iecr.9b00331
摘要
The traditional manufacturing process of 1,3-dioxolane requires high investment and energy consumption. A reactive distillation with pressure-swing distillation process is proposed as an attractive candidate based on the process simulation results in this work. To simulate the reactive distillation process, the kinetics experiments of formaldehyde aldolization with ethylene glycol were performed over NKC-9 cationic-exchange resin catalyst at 353–368 K. Byproducts were observed, and the batch distillation experiment were carried out to determine the boiling point temperatures ranking. A calculation strategy of aqueous and ethanediolic formaldehyde solutions was developed to solve the vapor–liquid equilibrium. The sensitivity analysis result shows that the yield of 1,3-dioxolane could be improved to 0.995 in the reactive distillation column, and high-purity 1,3-dioxolane (99.9 wt %) can be obtained in the following pressure-swing distillation process. The research achievements provides a new 1,3-dioxolane production process, which has an advantage in equipment integration.
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