Modeling and simulation of butanol separation from aqueous solutions using pervaporation

被引:34
作者
Ei-Zanati, E. [1 ]
Abdel-Hakim, E.
El-Ardi, O.
Fahmy, M.
机构
[1] Natl Res Ctr, Cairo, Egypt
[2] Cairo Univ, Cairo, Egypt
关键词
pervaporation; influencing parameters; butanol; membrane separation; modeling and simulation;
D O I
10.1016/j.memsci.2006.01.029
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A study was conducted to separate butanol from an aqueous solution using pervaporation. A specially designed and manufactured cell was used to separate the butanol from butanol/water solutions of different butanol concentrations (6-8-11-16-20-50) g/l. A 250 cm(3) butanol mixture at 33 degrees C was used to feed the cell, while the pressure of permeation side was about similar to 0 bar. Results revealed that butanol concentration changes non-linearly during the first 3 h, and then proceeds linearly. The percentage of butanol removal increases with increasing feed concentration. The permeability of the used membrane was determined experimentally. A resistance in series model was used to simulate the pervaporation step. The butanol concentration in the feed during the pervaporation step was predicted by using the developed model. There is a fair agreement between butanol concentration in feeding tank of pervaporation cell both experimentally and predicted from the developed model. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:278 / 283
页数:6
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