Improvements on anhydrous ethanol production by extractive distillation using ionic liquid as solvent

被引:36
作者
Figueroa, J. J. [1 ]
Lunelli, B. Hoss [1 ]
Maciel Filho, R. [1 ]
Wolf Maciel, M. R. [1 ]
机构
[1] Univ Estadual Campinas, Sch Chem Engn, Lab Optimizat Design & Adv Control, Ave Albert Einstein,500,Cidade Univ Zeferino Vaz, BR-13083852 Campinas, SP, Brazil
来源
CHISA 2012 | 2012年 / 42卷
基金
巴西圣保罗研究基金会;
关键词
Biofuels; ionic liquids; azeotrope; extractive distillation; VAPOR-PRESSURE MEASUREMENT; TERNARY-SYSTEMS; PHASE-BEHAVIOR; WATER; SEPARATION; BINARY; PLUS; EQUILIBRIA; MIXTURES; CHLORIDE;
D O I
10.1016/j.proeng.2012.07.493
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Biorefineries use a variety of separation methods in order to produce high value co-products from different feed streams. The ionic liquids (IL) represent new classes of non-volatile selective solvents with large solubility, low solution viscosities, low toxicity. In this work, a computational study on extractive distillation using ionic liquids aiming to improve the properties of separation and lower energy consumption compared to conventional extraction agents, showing significant potential for this application, was developed. The ternary vapor liquid equilibrium data were taken from literature and the process was modeled and simulated using Aspen Plus TM process simulation environment. Computed results showed that 1-Butyl-3-methylimidazolium methyl sulfate ([emim][mSO4]) consumes lesser energy per kilogram of anhydrous ethanol, obtaining an ethanol purity of 0.995 (in mass) and an ethanol percentage recovery of 99.9 wt%. (C) 2012 Published by Elsevier Ltd.
引用
收藏
页码:1016 / 1026
页数:11
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