A unified approach of gas, liquid and supercritical solvent transport through microporous membranes

Abstract The main objective of this study is the determination and description of mass transfer mechanisms of fluids under various states—gas, liquid and supercritical—through microporous inorganic membranes. The work was focused on the permeation of CO 2 through membranes whose selective layer is constituted by MFI zeolite, a material with particular properties of porosity, crystalline structure and adsorption. To describe the evolution that experiences the fluid inside the microporous medium as a function of pressure and temperature, models based on the formulation of Maxwell–Stefan were selected. As a whole, it appears whatever the state of the fluid the transfer mechanisms are the same. The transfer of fluid results from a combination of diffusive mechanism and interaction with the membrane surface. It is well in agreement with the fact that the proximity between the pore size and molecules enables one to foresee.

[1]  K. Kusakabe,et al.  Morphology and gas permeance of ZSM-5-type zeolite membrane formed on a porous α-alumina support tube , 1996 .

[2]  L. Cot,et al.  Fundamentals of inorganic membrane science and technology , 1996 .

[3]  Freek Kapteijn,et al.  Measurement and modeling of the transient adsorption, desorption and diffusion processes in microporous materials , 1999 .

[4]  Marie-Pierre Belleville,et al.  Progress in enzymatic membrane reactors ¿ a review , 2004 .

[5]  L. Riekert Rates of sorption and diffusion of hydrocarbons in zeolites , 1971 .

[6]  H. Pfeifer,et al.  Single-file diffusion and reaction in zeolites , 1992 .

[7]  R. Krishna A unified approach to the modelling of intraparticle diffusion in adsorption processes , 1993 .

[8]  F. Kapteijn,et al.  Diffusivities of light alkanes in a silicalite-1 membrane layer , 2000 .

[9]  F. Kapteijn,et al.  Transport and separation properties of a silicalite-1 membrane—I. Operating conditions , 1999 .

[10]  J. Falconer,et al.  Parallel pathways for transport in ZSM-5 zeolite membranes , 1998 .

[11]  O. Talu,et al.  Adsorption Equilibria of C1 to C4 Alkanes, CO2, and SF6 on Silicalite , 1998 .

[12]  Freek Kapteijn,et al.  Permeation characteristics of a metal-supported silicalite-1 zeolite membrane , 1996 .

[13]  A. Dixon,et al.  Theory of gas diffusion and permeation in inorganic molecular-sieve membranes , 1995 .

[14]  V. Choudhary,et al.  Adsorption of methane, ethane, ethylene, and carbon dioxide on silicalite-l , 1996 .

[15]  Y. Shindo,et al.  GAS DIFFUSION IN MICROPOROUS MEDIA IN KNUDSEN''S REGIME , 1983 .

[16]  S. Sarrade,et al.  Nanofiltration membrane behavior in a supercritical medium , 1996 .

[17]  Jörg Kärger,et al.  Diffusion in Zeolites and Other Microporous Solids , 1992 .

[18]  James Wei,et al.  Diffusion mechanism of hydrocarbons in zeolites—I. Theory , 1992 .

[19]  Permeation of supercritical fluids through a MFI zeolite membrane , 2001 .

[20]  José Sánchez,et al.  The application of transient time-lag method for the diffusion coefficient estimation on zeolite composite membranes , 2001 .

[21]  F. Kapteijn,et al.  Permeation of weakly adsorbing components through a silicalite-1 membrane , 1999 .

[22]  Freek Kapteijn,et al.  Temperature dependence of one‐component permeation through a silicalite‐1 membrane , 1997 .

[23]  C. E. Webster,et al.  A Method for Characterizing Effective Pore Sizes of Catalysts , 1999 .

[24]  J. Dalmon,et al.  Experimental study and numerical simulation of hydrogen/isobutane permeation and separation using MFI-zeolite membrane reactor , 2000 .

[25]  S. Sarrade,et al.  AN OVERVIEW ON MICROPOROUS MEMBRANE BEHAVIOUR IN VARIOUS FLUID STATE ENVIRONMENTS : APPLICATIONS TO SEPARATION AND REACTION , 2002 .

[26]  José Sánchez,et al.  Control of transport properties with a microporous membrane reactor to enhance yields in dehydrogenation reactions , 1995 .