Evaluating mixture adsorption models using molecular simulation

被引:32
|
作者
Swisher, Joseph A. [1 ,2 ]
Lin, Li-Chiang [1 ,2 ]
Kim, Jihan [1 ,2 ]
Smit, Berend [2 ,3 ]
机构
[1] Univ Calif Berkeley, Dept Chem & Biomol Engn, Berkeley, CA 94720 USA
[2] Univ Calif Berkeley, Lawrence Berkeley Natl Lab, Div Mat Sci, Berkeley, CA 94720 USA
[3] Univ Calif Berkeley, Dept Chem, Berkeley, CA 94720 USA
关键词
adsorption; gas; simulation; molecular; computer simulations (MC and MD); thermodynamics; classical; zeolites; METAL-ORGANIC FRAMEWORKS; ADSORBED SOLUTION THEORY; CARBON-DIOXIDE ADSORPTION; MONTE-CARLO SIMULATIONS; MIXED-GAS ADSORPTION; ACTIVATED CARBON; BINARY-MIXTURES; HETEROGENEOUS SURFACES; NANOPOROUS MATERIALS; NONIDEAL MIXTURES;
D O I
10.1002/aic.14058
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The design of adsorption-based separation processes using novel adsorbents requires reliable data for the adsorption of fluid mixtures on candidate adsorbents. Due to the difficulty of generating sufficient data across possible operating conditions, process designs generally rely on interpolation of pure-component data using a model, most commonly ideal adsorbed solution theory (IAST), and related theories. There are many cases where IAST fails to provide an adequate description of mixture adsorption, usually due to the fact that practical adsorbents do not have uniform surfaces. We have evaluated the use of a segregated version of IAST, where competition is assumed to occur at isolated adsorption sites. This simple modification can provide the correct description of adsorption across a large range of pressures using ideal isotherm models. We also demonstrate the importance of identifying multiple sites even for weakly adsorbing components to provide the correct behavior at high pressure. (c) 2013 American Institute of Chemical Engineers AIChE J, 59: 3054-3064, 2013
引用
收藏
页码:3054 / 3064
页数:11
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