Influence of isotherm inflection on diffusion in silicalite

被引:93
作者
Krishna, R [1 ]
Vlugt, TJH [1 ]
Smit, B [1 ]
机构
[1] Univ Amsterdam, Dept Chem Engn, NL-1018 WV Amsterdam, Netherlands
关键词
zeolite diffusion; dual-site Langmuir isotherm; configurational bias Monte Carlo techniques; fick diffusivity; Maxwell-Stefan theory; thermodynamic correction factor;
D O I
10.1016/S0009-2509(98)00538-7
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Adsorption isotherms of benzene, p-xylene, n-hexane, II-heptane and branched alkanes in silicalite show inflection behaviour; this behaviour is adequately modelled using a dual-site Langmuir model. In this model we make a distinction between two sites with different sorption characteristics: (I)site A which refer to the intersections between the straight channels and the zig-zag channels, and site B which refers to the channel interiors (straight or zig-zag channels). Using the Maxwell-Stefan theory of diffusion in zeolites, the influence of the isotherm inflection on the Fick diffusivity of pure components in silicalite is shown to be characterized by two extrema. For a mixture of n-hexane and 3-methyl pentane, the dual-site Langmuir model for the mixture predicts a curious maximum in the loading of the branched alkane; this mixture behaviour is confirmed by Configurational-Bias Monte Carlo simulations. The Maxwell-Stefan theory is used to demonstrate the possibility of separating the hydrocarbon isomers by permeation across a silicalite membrane. (C) 1999 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:1751 / 1757
页数:7
相关论文
共 21 条
[1]   Separations of cyclic, branched, and linear hydrocarbon mixtures through silicalite membranes [J].
Funke, HH ;
Argo, AM ;
Falconer, JL ;
Noble, RD .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (01) :137-143
[2]   PHASE-TRANSITION AND STRUCTURAL HETEROGENEITY - BENZENE ADSORPTION ON SILICALITE [J].
GUO, CJ ;
TALU, O ;
HAYHURST, DT .
AICHE JOURNAL, 1989, 35 (04) :573-578
[3]   PROBLEMS AND PITFALLS IN THE USE OF THE FICK FORMULATION FOR INTRAPARTICLE DIFFUSION [J].
KRISHNA, R .
CHEMICAL ENGINEERING SCIENCE, 1993, 48 (05) :845-861
[4]   MULTICOMPONENT SURFACE-DIFFUSION OF ADSORBED SPECIES - A DESCRIPTION BASED ON THE GENERALIZED MAXWELL-STEFAN EQUATIONS [J].
KRISHNA, R .
CHEMICAL ENGINEERING SCIENCE, 1990, 45 (07) :1779-1791
[5]   Review article number 50 - The Maxwell-Stefan approach to mass transfer [J].
Krishna, R ;
Wesselingh, JA .
CHEMICAL ENGINEERING SCIENCE, 1997, 52 (06) :861-911
[6]   Sorption-induced diffusion-selective separation of hydrocarbon isomers using silicalite [J].
Krishna, R ;
Smit, B ;
Vlugt, TJH .
JOURNAL OF PHYSICAL CHEMISTRY A, 1998, 102 (40) :7727-7730
[7]   THE MAXWELL-STEFAN DESCRIPTION OF MASS-TRANSPORT ACROSS ZEOLITE MEMBRANES [J].
KRISHNA, R ;
VANDENBROEKE, LJP .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1995, 57 (02) :155-162
[8]  
Krishna R., 1993, Gas Sep. Purify, V7, P91, DOI DOI 10.1016/0950-4214(93)85006-H
[9]   SORBATE IMMOBILIZATION IN MOLECULAR-SIEVES - RATE-LIMITING STEP FOR N-HEXANE UPTAKE BY SILICALITE-I [J].
MICKE, A ;
BULOW, M ;
KOCIRIK, M ;
STRUVE, P .
JOURNAL OF PHYSICAL CHEMISTRY, 1994, 98 (47) :12337-12344
[10]  
RUTHVEN DM, 1984, PRINCIPLES ADSORPTIO, P91