Effect of porosity on mass transfer of gas absorption in a hollow fiber membrane contactor

被引:11
|
作者
Zhang, Weidong [1 ]
Hao, Zisu [1 ]
Chen, Geng [1 ]
Li, Jiang [1 ]
Li, Zhushi [1 ]
Wang, Zihao [1 ]
Ren, Zhongqi [1 ]
机构
[1] Beijing Univ Chem Technol, State Key Lab Chem Resource Engn, Beijing Key Lab Membrane Sci & Technol, Beijing 100029, Peoples R China
基金
国家高技术研究发展计划(863计划); 中国国家自然科学基金;
关键词
Hollow fiber membrane contactor; Porosity; Mathematical modeling; Mass transfer; Membrane gas absorption; SOLVENT-EXTRACTION; LIQUID CONTACTORS; TRANSFER BEHAVIOR; CARBON-DIOXIDE; CO2; ABSORPTION; MODULES; PERFORMANCE; MODEL; FLOW;
D O I
10.1016/j.memsci.2014.06.059
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A mathematical model was proposed to elucidate the mass transfer of a hollow fiber membrane absorption process taking the effect of membrane porosity into account. This model was derived based on the mass transfer differential equation and discretized considering the micropores On the membrane wall. The model was numerically solved by using upwind difference technique, and the solute concentration profiles were obtained. Effects of porosity under various conditions, including membrane pore size, fiber length, pH of absorbent and liquid velocity on the mass transfer process, were quantitatively investigated. The results indicated that the porosity plays an important role in forming the solute concentration profile, and thus influenced the mass transfer performance. Low porosity (or high pH and liquid velocity, or low fiber length) corresponded to the heterogeneous profiles, while opposite conditions led to the homogeneous profiles. The model gave calculation results in good agreement with experimental results. (C) 2014 Elsevier B.V. All rights reserved,
引用
收藏
页码:399 / 410
页数:12
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