Separation modeling of linear and branched C6 alkane permeation through silicalite-1 membranes

被引:16
作者
Zhu, W [1 ]
Kapteijn, F [1 ]
Moulijn, JA [1 ]
机构
[1] Delft Univ Technol, DelfChemTech, NL-2628 BL Delft, Netherlands
关键词
silicalite-1; permeation modeling; Maxwell-Stefan equations; multi-component diffusion; ideal adsorbed solution theory;
D O I
10.1016/S1383-5866(03)00042-X
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The component fluxes of binary mixtures through MFI-type membranes are strongly affected by the adsorption behaviour of the permeating species. An equilibrium adsorption study with the novel TEOM (tapered element oscillating microbalance) technique has shown a quantitative difference in the pure component isotherms of linear and branched C-6 alkanes in silicalite-1 crystals, wherein the branched isomers show a two-step adsorption behaviour. The concentration-dependent diffusivity is significantly affected by the dual-site nature of the adsorption. Configurational-entropy effects tend to favor the adsorption of linear over branched alkanes in isomer mixtures in silicalite-1 because linear molecules "pack" more efficiently in the structure. A permeation model, based on single-component parameters and accounting for these configurational-entropy effects, is used to predict the fluxes of binary mixtures across a silicalite-1 membrane. Good agreement with the available experimental data indicates the strength of the proposed model approach. (C) 2003 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:223 / 230
页数:8
相关论文
共 24 条
[1]   Zeolite membranes -: state of their development and perspective [J].
Caro, J ;
Noack, M ;
Kölsch, P ;
Schäfer, R .
MICROPOROUS AND MESOPOROUS MATERIALS, 2000, 38 (01) :3-24
[2]   Separations of C4 and C6 isomers in ZSM-5 tubular membranes [J].
Coronas, J ;
Noble, RD ;
Falconer, JL .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (01) :166-176
[3]   Separation of C6 isomers by vapor permeation and pervaporation through ZSM-5 membranes [J].
Flanders, CL ;
Tuan, VA ;
Noble, RD ;
Falconer, JL .
JOURNAL OF MEMBRANE SCIENCE, 2000, 176 (01) :43-53
[4]   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
[5]  
GORA L, UNPUB
[6]   Separation of hexane isomers through nonzeolite pores in ZSM-5 zeolite membranes [J].
Gump, CJ ;
Noble, RD ;
Falconer, JL .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (07) :2775-2781
[7]   The generalized Maxwell-Stefan model for diffusion in zeolites: sorbate molecules with different saturation loadings [J].
Kapteijn, F ;
Moulijn, JA ;
Krishna, R .
CHEMICAL ENGINEERING SCIENCE, 2000, 55 (15) :2923-2930
[8]   One-component permeation maximum: Diagnostic tool for silicalite-1 membranes? [J].
Kapteijn, F ;
van de Graaf, JM ;
Moulijn, JA .
AICHE JOURNAL, 2000, 46 (05) :1096-1100
[9]   Permeation of hexane isomers across ZSM-5 zeolite membranes [J].
Krishna, R ;
Paschek, D .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (07) :2618-2622
[10]   Separation of hydrocarbon mixtures using zeolite membranes: a modelling approach combining molecular simulations with the Maxwell-Stefan theory [J].
Krishna, R ;
Paschek, D .
SEPARATION AND PURIFICATION TECHNOLOGY, 2000, 21 (1-2) :111-136