Zeolite NaA membranes supported on alumina hollow fibers: Effect of support resistances on pervaporation performance

被引:66
作者
Shao, Jia [1 ,2 ]
Zhan, Zhiying [1 ]
Li, Jiangang [1 ]
Wang, Zhengbao [1 ]
Li, Kang [2 ]
Yan, Yushan [1 ,3 ]
机构
[1] Zhejiang Univ, Dept Chem & Biol Engn, MOE Engn Res Ctr Membrane & Water Treatment Techn, Hangzhou 310027, Zhejiang, Peoples R China
[2] Univ London Imperial Coll Sci Technol & Med, Dept Chem Engn & Chem Technol, London SW7 2AZ, England
[3] Univ Delaware, Dept Chem Engn, Newark, DE 19716 USA
基金
中国国家自然科学基金;
关键词
Zeolite membrane; Hollow fiber support; Pervaporation flux; Support resistance; TUBULAR SUPPORTS; CLEAR SOLUTION; INNER-SIDE; ETHANOL; SEPARATION; MIXTURES; GROWTH; LAYER; FLUX;
D O I
10.1016/j.memsci.2013.09.049
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Porous Al2O3 hollow fibers with different asymmetric macrostructures, i.e single or double finger-like layer, have been prepared by a phase inversion/sintering technique. Such hollow fibers are used as supports to synthesize zeolite NaA membranes with high separation factors ( > 10,000) in the pervaporation of ethanol/water solution (90 wt%, 75 degrees C). Different zeolite thicknesses are achieved by means of extending the crystallization time and increasing the number of synthesis cycles. Influences of both the zeolite layer thickness and support layer macrostructures on pervaporation properties of zeolite NaA/Al2O3 supported membranes are investigated. The results indicate that variations of support macrostructures have a more noticeable effect on the pervaporation flux than zeolite layer thickness. There is an approximate linear dependence of the pervaporation flux of the supported membrane on the support porosity despite the fact that these hollow fibers are produced with different preparation conditions. When the support porosity increases to 69%, a pervaporation flux of 11.1 kg m(-2) h(-1) is achieved. 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:10 / 17
页数:8
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