Asymmetric effects in catalytic membranes

A catalytic membrane hybrid system based on a cermet membrane with a channel size 〈d〉 of ～0.12 μm has been produced using sol-gel processing. A layer of a superfine methanol conversion catalyst with the composition Cr₂O₃ · Al₂O₃ · ZnO has been formed on the inner surface of the channels, and a thin oxide coating of composition P_0.03Ti_0.97O_{2 ± δ} with a homogeneous porous structure and 〈d〉 ～ 2 nm has been formed on the geometric membrane surface. The methanol conversion rate and the gas permeability of the membrane depend considerably on the methanol vapor and gas (H₂, He, CO₂, Ar, CH₄) flow directions. When methanol vapor diffuses toward the mesoporous layer, the catalytic activity is one order of magnitude higher and the gas permeability coefficients are 3–8 times lower than in the case of the reverse flow of the gaseous molecules. The temperature dependence of the gas permeability taking into account the possible types of mass transfer in porous solids suggests that, when the gases move toward the mesoporous coating consisting of phosphorus-modified titanium oxide, surface flow and activated diffusion dominate, whereas the reverse gas motion is dominated by free molecular flow.