Gas transport and separation with ceramic membranes. Part I. Multilayer diffusion and capillary condensation

Multilayer diffusion and capillary condensation of propylene on supported γ-alumina films greatly improved the permeability and selectivity. Multilayer diffusion, occurring at relative pressures of 0.4 to 0.8 strongly increased the permeability of 6 times the Knudsen permeability, yielding permeabilities of 3.2 × 10−5 mol/m2-sec-Pa. The occurrence of a maximum in the permeability coincides with blocking of the pore by adsorbate (capillary condensation). This point could be predicted, employing adsorption data and the slit shape form of the pore. Separation factors of 27 were obtained with a N2---N3H6 mixture and a supported γ-alumina film, with C3H6 the preferentially permeating component. This very effective separation is due to pore blocking by adsorbate. The separation factor increased to 85 after modification of the system with magnesia by the reservoir method. However, the permeability of propylene decreased by a factor of 20 to 1.6 × 10−6 mol/m2-sec-Pa.

[1]  A. J. Burggraaf,et al.  The preparation and characterization of alumina membranes with ultrafine pores: 2. The formation of supported membranes , 1985 .

[2]  C. L. Yaws,et al.  Physical properties: A guide to the physical, thermodynamic, and transport property data of industrially important chemical compounds , 1977 .

[3]  Kew-Ho Lee,et al.  The transport of condensible vapors through a microporous vycor glass membrane , 1986 .

[4]  H. Tamon,et al.  Interpretation of surface flow phenomenon of adsorbed gases by hopping model , 1981 .

[5]  S. Hwang,et al.  Transport of capillary condensate , 1975 .

[6]  E. Gilliland,et al.  Rates of flow through microporous solids , 1958 .

[7]  M. Fuji,et al.  SEPARATION OF ALCOHOL/WATER GASEOUS MIXTURES BY AN IMPROVED CERAMIC MEMBRANE , 1986 .

[8]  P. Eberly,et al.  Diffusion of benzene and inert gases through porous media at elevated temperatures and pressures , 1965 .

[9]  K. J. Sladek,et al.  Diffusion on Surfaces. I. Effect of Concentration on the Diffusivity of Physically Adsorbed Gases , 1974 .

[10]  H. Tamon,et al.  WATER TRANSFER COEFFICIENT IN ADSORPTIVE POROUS BODY , 1983 .

[11]  A. Burggraaf,et al.  Gas separation mechanisms in microporous modified γ-al2o3 membranes , 1988 .

[12]  W. Steele Adsorption surface area and porosity: By S. J. Gregg and K. S. W. Sing. Academic Press, New York, 1982. 2nd. ed., 312 pp. $44.50. , 1983 .

[13]  A. Burggraaf,et al.  Synthesis of ceramic membranes , 1992 .

[14]  A. Burggraaf,et al.  Synthesis of ceramic membranes , 1992 .

[15]  H. Tamon,et al.  Flow mechanism of adsorbate through porous media in presence of capillary condensation , 1981 .

[16]  A. Burggraaf,et al.  Gas transport and separation with ceramic membranes. Part II: Synthesis and separation properties of microporous membranes , 1992 .

[17]  M. Asaeda,et al.  Separation of alcohol/water gaseous mixtures by thin ceramic membrane. , 1986 .

[18]  A. Burggraaf,et al.  Gas and surface diffusion in modified γ-alumina systems , 1989 .