Porous polyethersulfone hollow fiber membrane in gas-liquid contacting processes

被引:15
作者
Bakeri, Gh [1 ]
Ismail, A. F. [2 ]
Rahimnejad, M. [1 ]
Matsuura, T. [2 ,3 ]
机构
[1] Babol Noshirvani Univ Technol, Fac Chem Engn, Babol Sar, Iran
[2] Univ Teknol Malaysia, Adv Membrane Technol Res Ctr AMTEC, Skudai 81310, Johor, Malaysia
[3] Univ Ottawa, Ind Membrane Res Inst, Dept Chem & Biol Engn, Ottawa, ON K1N 6N5, Canada
关键词
PES hollow fiber membrane; Membrane structure; Membrane contactor; CO2; absorption; MASS-TRANSFER; POLY(ETHER IMIDE); PHASE-SEPARATION; CO2; ABSORPTION; CARBON-DIOXIDE; PERFORMANCE; MORPHOLOGY; RESISTANCE; SOLVENTS; MODEL;
D O I
10.1016/j.cherd.2013.11.008
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Porous polyethersulfone hollow fiber membranes were fabricated via dry-wet phase inversion method with the polymer concentration in the spinning dope either 13 wt% or 15 wt%. The fabricated hollow fiber membranes were characterized by different test methods and the performance of membranes in contactor applications was tested by CO2 absorption. The mean pore size, effective surface porosity and membrane porosity decreased while the membrane density and Liquid Entry Pressure (LEPw) increased as polymer concentration increased. The CO2 absorption flux of the fabricated membranes was measured in two cases; i.e. when the absorbent, distilled water, was in the lumen side or in the shell side. The CO2 flux for the membrane, fabricated from 13 wt% PES solution, was compared with some commercial and in-house made membranes. The former membrane had 111% higher flux than a commercial PTFE membrane. (C) 2013 The Institution of Chemical Engineers. Published by Elsevier &V All rights reserved.
引用
收藏
页码:1381 / 1390
页数:10
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