Modeling CO2-facilitated transport across a diethanolamine liquid membrane

被引:27
作者
Bao, LH
Trachtenberg, MC
机构
[1] Carbozyme Inc, Dept Res & Dev, Monmouth Jct, NJ 08852 USA
[2] Sapients Inst, Monmouth Jct, NJ 08852 USA
基金
美国国家航空航天局;
关键词
contained liquid membrane; gas separation; mass transfer model; facilitated transport process;
D O I
10.1016/j.ces.2005.05.056
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
We compared experimental and model data for the facilitated transport of CO2 from a CO2-air mixture across an aqueous solution of diethanolamine (DEA) via a hollow fiber, contained liquid membrane (HFCLM) permeator. A two-step carbamate formation model was devised to analyze the data instead of the one-step mechanism used by previous investigators. The effects of DEA concentration, liquid membrane thickness and feed CO2 concentration were also studied. With a 20% (wt) DEA liquid membrane and feed of 15% CO2 in CO2-air mixture at atmosphere pressure, the permeance reached 1.51E-8 mol/m(2) s Pa with a CO2/N-2 selectivity of 115. Model predictions compared well with the experimental results at CO2 concentrations of industrial importance. Short-term stability of the HFCLM permeator performance was examined. The system was stable during 5-days of testing. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:6868 / 6875
页数:8
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