Steady vs unsteady membrane gas separation processes

被引:19
作者
Castel, Christophe [1 ]
Wang, Lei [1 ]
Corriou, Jean Pierre [1 ]
Favre, Eric [1 ]
机构
[1] Univ Lorraine, CNRS, LRGP, 1 Rue Grandville, F-54001 Nancy, France
关键词
Membrane; Separations; Unsteady; Processes; Gas; Purity; Recovery; VACUUM SWING PERMEATION; CARBON-DIOXIDE CAPTURE; OPERATING-CONDITIONS; NATURAL-GAS; ACID GASES; STATE; MIXTURES; RECYCLE; COUNTERCURRENT; OPTIMIZATION;
D O I
10.1016/j.ces.2018.03.013
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Nowadays, membrane processes are together with cryogeny, absorption and adsorption considered to be a key technology for gas separation applications. Process selectivity is of primary importance in order to respect the specifications but can in some cases be limited due to a too low membrane selectivity. Parallel to improvements in the membrane selectivity of certain materials, unsteady membrane operations can also be attempted in order to achieve a higher separation selectivity, but this strategy remains largely unexplored. A novel, simple, unsteady-state process, complementary to the strategies already proposed by the previous authors, is reported in this study. A systematic comparison of steady state, short-class (i.e. with time lag) and long-class (i.e. pseudo steady-state) processes is described for O-2/N-2 (PPO membrane), He/Kr (PEMA membrane) and H-2/CO2 (polyimide and a reverse selective PEBAX membrane) separations. Based on a selectivity composition path chart, the maximal purity or process selectivity achievable by steady and unsteady processes was compared. The new long-class process was shown to offer similar or increased selectivity compared to steady-state operation, at the expense of a lower productivity. Finally, the applicability to industrial separations and the remaining challenges are also discussed. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:136 / 147
页数:12
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