Analysis of permeate pressure build-up effects on separation performance of asymmetric hollow fiber membranes

被引:8
|
作者
Kundu, Prodip [1 ]
Zakaria, Rabitah [1 ]
Chakma, Amit [1 ]
Feng, Xianshe [1 ]
机构
[1] Univ Waterloo, Dept Chem Engn, Waterloo, ON N2L 3G1, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Membranes; Separations; Hollow fiber; Pressure build-up; Potted length; Permeance; MULTICOMPONENT GAS SEPARATION; POLYSULFONE MEMBRANES; CELLULOSE TRIACETATE; COMPOSITE MEMBRANES; SILICONE-RUBBER; CARBON-DIOXIDE; SIMULATION; ENRICHMENT; TRANSPORT; MIXTURES;
D O I
10.1016/j.ces.2013.10.003
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The study rectifies some perceptions about pressure build-up in hollow fiber membranes. It is a general intuition that operating at higher pressures permeates more gases, and sometimes the membrane module is tested or characterized at lower pressures to reduce gas consumption. It is also perceived that higher pressure build-up occurs at higher feed pressures, and membrane performance deteriorates at higher feed pressures. In this study, the apparent and intrinsic permeances of H-2 and N-2 in asymmetric cellulose acetate based hollow fiber membranes were evaluated from gas permeation experiments and numerical analysis. It was shown that though the permeate pressure build-up increases as the feed pressure increases, the effect of the permeate pressure build-up on the membrane performance is actually reduced at higher feed pressures. Membrane performs close to its intrinsic separation properties if it is operated at high feed pressures, under which conditions the effect of pressure build-up on the membrane performance is minimized. The pressure build-up effect was further investigated by evaluating the percentage loss in the driving force due to permeate pressure build-up, and it was found that percentage loss in driving force is less at higher feed pressures than that at lower feed pressures. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:849 / 856
页数:8
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