Multicomponent hydrogen/hydrocarbon separation by MFI-type zeolite membranes

Separation of an eight-component simulated refinery gas mixture including h ydrogen (similar to 84 mol %) and Eight hydrocarbons (C-1 - C-4, 7.5 simila r to 0.3 mol %) by alpha-alumina-supported polycrystalline MFI zeolite memb ranes was studied at 25 - 500 degrees C and feed pressures of 0.1 - 0.4 MPa . The zeolite membrane showed excellent separation properties for rejection of hydrogen from the hydrogen/hydrocarbon mixture at < 1000 degrees C. At room temperature and atmospheric pressure on both feed and permeate sides, hydrogen permeation rate is almost zero, while the hydrocarbon permeation r ate is 2-4 X 10(-4) mol.m(-2).s(-1). The zeolite membrane outperforms the m icroporous carbon membrane in terms of both selectivity and permeance for h ydrocarbons over hydrogen. At 500 degrees C the zeolite membrane becomes pe rmselective for hydrogen over hydrogen (C-1-C-4). In the whole temperature range iso-butane is nonpermeable (with a permeance below the GC analysis li mit) through the zeolite membrane. Separation results of the zeolite membra ne can be characterized by a solution-diffusion model considering competiti ve adsorption of hydrocarbons over hydrogen and configurational diffusion i n the zeolite pores. The MFI-type zeolite membranes showed promise for appl ications in separation processes for hydrogen concentration/purification fr om various hydrogen/hydrocarbon mixtures (at lower temperatures) and in mem brane reactors for dehydrogenation reactions (at high temperatures).