Extractive Distillation with Ionic Liquids: A Review

被引:282
|
作者
Lei, Zhigang [1 ]
Dai, Chengna [1 ]
Zhu, Jiqin [1 ]
Chen, Biaohua [1 ]
机构
[1] Beijing Univ Chem Technol, State Key Lab Chem Resource Engn, Beijing 100029, Peoples R China
关键词
extractive distillation; ionic liquids; predictive thermodynamic models; structure-property relations; separation mechanism; process simulation and optimization; review; ISOBARIC VAPOR-LIQUID; DILUTION ACTIVITY-COEFFICIENTS; MODIFIED UNIFAC DORTMUND; PLUS ETHANOL+1-ETHYL-3-METHYLIMIDAZOLIUM TRIFLUOROMETHANESULFONATE; MULTICOMPONENT SEPARATION PROCESSES; DIFFERENT THERMODYNAMIC PROPERTIES; NONEQUILIBRIUM STAGE MODEL; PRESSURE CARBON-DIOXIDE; EXCESS MOLAR VOLUMES; INFINITE DILUTION;
D O I
10.1002/aic.14537
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Extractive distillation is commonly used for the separation of azeotropic or close-boiling mixtures in the chemical industry. During the past decade, the use of ionic liquids (ILs) as entrainers has received considerable attention due to their unique advantages when applied in extractive distillation. This work is devoted to providing an easy-to-read and comprehensive review on the recent progress made by chemical engineers, focusing on the issues of predictive thermodynamic models, structure-property relations, separation mechanisms, and process simulation and optimization. This review spans from the molecular level to the industrial scale, to provide a theoretical insight into the molecular interactions between ILs and the components to be separated. Moreover, a comprehensive database on the vapor-liquid equilibria and activity coefficients at infinite dilution concerning ILs is provided as Supporting Information. Concluding remarks are made on the unsolved scientific issues with respect to this promising special distillation technology. (C) 2014 American Institute of Chemical Engineers
引用
收藏
页码:3312 / 3329
页数:18
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