Porous membrane for use in reaction process

Claim 2

A porous membrane for use in a chemical reaction process, the porous membrane comprising a porous support formed with interconnected micropores having an average pore size of 0.5 μm to 30 μm and having a catalytic component uniformly distributed therein, and at least one porous thin layer integrally formed on the porous support and formed with interconnected micropores having an average pore size less than 100 nm (1000 Å) and less than that of the micropores in the porous support, wherein the porous support is arranged as a catalytic layer in the chemical reaction process to effect catalytic reaction of fluid applied thereto, and the porous thin layer is arranged as a gas separation layer to effect Knudsen diffusion for separating a specific product fluid from the reaction fluid.

Claim 3

A porous membrane as recited in claim 1 wherein the catalytic component is molybdenum sulfide.

Claim 4

A porous membrane as recited in claim 2, wherein the catalytic component is a supported precious metal catalyst.

Claim 5

A porous membrane as recited in claim 3, wherein the supported precious metal catalyst is platinum-alumina or palladium-silica-alumina.

Claim 6

A porous membrane as reacted in claim 1 wherein the porous support is made of an inorganic raw material.

Claim 7

A porous membrane as recited in claim 5, wherein the porous support is made of alumina, silica-alumina, zirconia, zeolite, porous glass or carbon.

Claim 8

A porous membrane as recited in claim 1, wherein the porous support and the porous thin layer are each made of an inorganic raw material.

Claim 9

A porous membrane as recited in claim 7, wherein the porous thin layer is less than 500 μm thick.

Claim 10

A porous membrane as recited in claim 7, wherein the porous support is made of alumina, silica-alumina, mullite, cordierite, zirconia or carbon and the porous thin layer is made of alumina, silica-alumina, zirconia, zeolite, porous glass or carbon.

Claim 11

A porous membrane as recited in claim 1, wherein the porous thin layer is less than 500 μm thick.

Claim 12

A porous membrane for use in a chemical reaction process, the porous membrane comprising a porous support formed with interconnected micropores having an average pore size of 0.5 μm to 30 μm, a first porous thin layer integrally formed on the porous support and formed with interconnected micropores having an average pore size of 0.5 μm to 30 μm and having a catalytic component uniformly distributed therein, and a second porous thin layer integrally formed on the first porous thin layer and formed with interconnected micropores having an average pore size less than 100 nm (1000 Å) and less than that of the micropores in the first porous thin layer, wherein the first porous thin layer is arranged as a catalytic layer in the chemical reaction process to effect catalytic reaction of fluid applied thereto through the porous support, and the second porous thin layer is arranged as a gas separation layer to effect Knudsen diffusion for separating a specific product from the reaction fluid.

Claim 13

A porous membrane for use in a chemical reaction process, the porous membrane comprising a porous support formed with interconnected micropores having an average pore size of 0.5 μm to 30 μm, a first porous thin layer integrally formed on the porous support and formed with interconnected micropores having an average pore size of 0.5 μm to 30 μm and having a catalytic component uniformly distributed therein, and a second porous thin layer integrally formed on the first porous thin layer and formed with interconnected micropores having an average pore size less than 100 nm (1000 Å) and less than that of the micropores in the first porous thin layer, wherein the first porous thin layer is arranged as a catalytic layer in the chemical reaction process to effect catalytic reaction of fluid applied thereto through the porous support, and the second porous thin layer is arranged as a gas separation layer to effect Knudsen diffusion for separating a specific product from the reaction fluid.

Claim 14

A porous membrane for use in a chemical reaction process, the porous membrane comprising a porous support having first and second surfaces and being formed with interconnected micropores having an average pore size of 0.5 μm to 30 μm, a first porous thin layer integrally formed on said first surface of the porous support and formed with interconnected micropores having an average pore size of 0.5 μm to 30 μm and having a catalytic component uniformly distributed therein, and a second porous thin layer integrally formed on said second surface of the porous support and formed with interconnected micropores having an average pore size less than 100 nm (1000 Å) and less than that of the micropores in the first porous thin layer, wherein the first porous thin layer is arranged as a catalytic layer in the chemical reaction process to effect catalytic reaction of fluid applied thereto, and the second porous thin layer is arranged as a gas separation layer to effect Knudsen diffusion for separating a specific product from the reaction fluid applied thereto through the porous support.

Claim 15

A porous membrane for use in a chemical reaction process, the porous membrane comprising a porous support having first and second surfaces and being formed with interconnected micropores having an average pore size of 0.5 μm to 30 μm, a first porous thin layer integrally formed on said first surface of the porous support and formed with interconnected micropores having an average pore size of 0.5 μm to 30 μm and having a catalytic component uniformly distributed therein, and a second porous thin layer integrally formed on said second surface of the porous support and formed with interconnected micropores having an average pore size less than 100 nm (1000 Å) and less than that of the micropores in the first porous thin layer, wherein the first porous thin layer is arranged as a catalytic layer in the chemical reaction process to effect catalytic reaction of fluid applied thereto, and the second porous thin layer is arranged as a gas separation layer to effect Knudsen diffusion for separating a specific product from the reaction fluid applied thereto through the porous support.