Influence of alkali cations on permeation properties of Y-type zeolite membranes

Abstract NaY-type zeolite membranes were synthesized on the outer surface of an α-alumina support tube by a hydrothermal process. The membranes were ion-exchanged with 0.01–0.50 mol/l aqueous solutions of KCl, RbCl or CsCl at 80 °C for 4 h. Gas permeation properties of the ion-exchanged membranes were determined at 35 °C for single component systems of CO 2 and N 2 and for an equimolar mixture, thereof. The CO 2 /N 2 separation factor for permeation increased with increasing ion-exchange degree, which was dependent on the cation species. When the membrane was treated in a 0.50 mol/l solution of KCl, RbCl and CsCl, the ion-exchange degree reached 96, 78 and 62%, respectively. The CO 2 /N 2 separation factors of the Y-type zeolite membranes ion-exchanged with K, Rb and Cs were 55, 47 and 46%, respectively, at a permeation temperature of 35 °C. The NaY-type zeolite membranes, which were impregnated with Cs ions, showed the highest CO 2 /N 2 separation factor of 149 at 35 °C. These results suggest that the CO 2 /N 2 separation factor was largely determined by the affinity between the membranes and the permeants.

[1]  K. Kusakabe,et al.  Gas Permeation Properties of Ion-Exchanged Faujasite-Type Zeolite Membranes , 1999 .

[2]  K. Kusakabe,et al.  Microporous Inorganic Membranes for Gas Separation , 1999 .

[3]  H. Kita,et al.  Synthesis of a zeolite NaA membrane for pervaporation of water/organic liquid mixtures , 1995 .

[4]  J. Dalmon,et al.  The hindering effect of adsorbed components on the permeation of a non-adsorbing component through a microporous silicalite membrane: the potential barrier theory , 1999 .

[5]  F. Kapteijn,et al.  Binary permeation through a silicalite‐1 membrane , 1999 .

[6]  H. Hattori,et al.  IR and TPD (temperature-programmed desorption) studies of carbon dioxide on basic site active for 1-butene isomerization on alkali-added zeolite X , 1997 .

[7]  George Xomeritakis,et al.  Growth, microstructure, and permeation properties of supported zeolite (MFI) films and membranes prepared by secondary growth , 1999 .

[8]  K. Aoki,et al.  Separation of Gases with an A-Type Zeolite Membrane , 2000 .

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

[10]  K. Kusakabe,et al.  The separation of CO2 using Y-type zeolite membranes ion-exchanged with alkali metal cations , 2001 .

[11]  K. Kusakabe,et al.  Preparation of MFI-Type Zeolite Membranes and Their Use in Separating n-Butane and i-Butane , 1997 .

[12]  Tsutomu Inoue,et al.  NaY zeolite membrane for the pervaporation separation of methanol–methyl tert-butyl ether mixtures , 1997 .

[13]  K. Kusakabe,et al.  Separation of carbon dioxide from nitrogen using ion-exchanged faujasite-type zeolite membranes formed on porous support tubes , 1998 .

[14]  Takahiro Kuroda,et al.  Formation of a Y-Type Zeolite Membrane on a Porous α-Alumina Tube for Gas Separation , 1997 .

[15]  J. Falconer,et al.  Alkali-free ZSM-5 membranes : Preparation conditions and separation performance , 1999 .

[16]  H. Kita,et al.  Tubular-type pervaporation module with zeolite NaA membrane☆ , 1997 .