Effect of pore-network connectivity on multicomponent adsorption of large molecules

被引:2
作者
Ismadji, S [1 ]
Bhatia, SK [1 ]
机构
[1] Univ Queensland, Dept Chem Engn, Brisbane, Qld 4072, Australia
关键词
D O I
10.1002/aic.690490108
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The effect of pore-network connectivity on binary liquid-phase adsorption equilibria using the ideal adsorbed solution theory (LAST) was studied. The liquid-phase binary adsorption experiments used ethyl propionate, ethyl butyrate, and ethyl isovalerate as the adsorbates and commercial activated carbons Filtrasorb-400 and Norit ROW 0.8 as adsorbents. As the single-component isotherm, a modified Dubinin-Radushkevich equation was used. A comparison with experimental data shows that incorporating the connectivity of the pore network and considering percolation processes associated with different molecular sizes of the adsorptives in the mixture, as well as their different corresponding accessibility, can improve the prediction of binary adsorption equilibria using the LAST Selectivity of adsorption for the larger molecule in binary systems increases with an increase in the pore-network coordination number, as well with an increase in the mean pore width and in the spread of the pore-size distribution.
引用
收藏
页码:65 / 81
页数:17
相关论文
共 34 条
[1]   Nonideal adsorption equilibria described by pure component isotherms and virial mixture coefficients [J].
Appel, WS ;
LeVan, MD ;
Finn, JE .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (12) :4774-4782
[2]  
CHENG YT, 1990, MATER SCI REP, V5, P45, DOI DOI 10.1016/S0920-2307(05)80007-6
[3]   ADSORPTION OF BINARY AND TERNARY HYDROCARBON-GAS MIXTURES ON ACTIVATED CARBON - EXPERIMENTAL-DETERMINATION AND THEORETICAL PREDICTION OF THE TERNARY EQUILIBRIUM DATA [J].
COSTA, E ;
SOTELO, JL ;
CALLEJA, G ;
MARRON, C .
AICHE JOURNAL, 1981, 27 (01) :5-12
[4]   ADSORPTION OF GAS-MIXTURES IN MICROPORES - EFFECT OF DIFFERENCE IN SIZE OF ADSORBATE MOLECULES [J].
DUNNE, J ;
MYERS, AL .
CHEMICAL ENGINEERING SCIENCE, 1994, 49 (17) :2941-2951
[5]   Theory for multicomponent adsorption equilibrium: Multispace adsorption model [J].
Gusev, V ;
OBrien, JA ;
Jensen, CRC ;
Seaton, NA .
AICHE JOURNAL, 1996, 42 (10) :2773-2783
[6]   COMPARING VARIOUS MULTICOMPONENT ADSORPTION EQUILIBRIUM-MODELS [J].
HU, XJ ;
DO, DD .
AICHE JOURNAL, 1995, 41 (06) :1585-1592
[7]   The use of liquid phase adsorption isotherms for characterization of activated carbons [J].
Ismadji, S ;
Bhatia, SK .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2001, 244 (02) :319-335
[8]   Characterization of activated carbons using liquid phase adsorption [J].
Ismadji, S ;
Bhatia, SK .
CARBON, 2001, 39 (08) :1237-1250
[9]   A modified pore-filling isotherm for liquid-phase adsorption in activated carbon [J].
Ismadji, S ;
Bhatia, SK .
LANGMUIR, 2001, 17 (05) :1488-1498
[10]   Investigation of network connectivity in activated carbons by liquid phase adsorption [J].
Ismadji, S ;
Bhatia, SK .
LANGMUIR, 2000, 16 (24) :9303-9313