Gas-permselective composite membranes and process for the production thereof

Claim 2

A gas-permselective composite membrane comprising: a heat-resistant porous polymeric membrane; and a thin layer of cross-linked structure provided on one side of said membrane, said thin layer being prepared by plasma polymerizing, at an atmosphere of 1.0 Torr or less under glow discharge of from 20 to 80 W, a compound selected from the group consisting of 4-methyl-1-pentene, 4-methyl-2-pentene, 2,4,4-trimethyl-1-pentene, 4,4-dimethyl-1-pentene, tert-butylamine, and their fluorine-containing derivatives, or from the group consisting of vinyl trimethylsilane, hexamethyldisilazane, dimethylaminotrimethylsilane, and trimethylsilylimidazole.

Claim 3

The composite membrane as claimed in claim 1, wherein the thin layer of cross-linked structure has a thickness of 0.3 micron or less.

Claim 4

The composite membrane as claimed in claim 1, wherein a siloxane compound is cross-linked in the pores of the heat-resistant porous polymeric membrane

Claim 5

The composite membrane according to claim 3, wherein the membrane support has an unsymmetrical structure comprised of one surface layer which contains the siloxane compound cross-linked by plasma and a reverse surface layer which does not contain any siloxane compound.

Claim 6

The composite membrane according to claim 4, wherein the siloxane compound which is cross-linked is a silicone oil.

Claim 7

The composite membrane as claimed in claim 1, wherein the heat-resistant porous polymeric membrane is made of a polytetrafluoroethylene, and has a structure comprising fibers and knots.

Claim 8

The composite membrane according to claim 1, wherein the thin-layer cross-linked structure contains a main chain and side chains, and branches comprising recurring methyl groups are linked to the main chain and side chains.

Claim 9

A process for producing a gas-permselective membrane, comprising the steps of: providing a heat-resistant porous polymeric membrane as a support; feeding a compound selected from the group consisting of 4-methyl-1-pentene, 4-methyl-2-pentene, 2,4,4-trimethyl-1-pentene, 4,4-dimethyl-1-pentene, tert-butylamine, and their flourine-containing derivatives, or from the group consisting of vinyl trimethylsilane, hexamethyldisilazane, dimethylaminotrimethylsilane, and trimethylsilylimidazole, said compound being fed into an atmosphere of 1.0 Torr or less under glow discharge of from 20 to 80 W in order to polymerize the compound and form a thin membrane; and depositing the thin membrane on the heat-resistant porous polymeric membrane.

Claim 10

A process for producing a gas-permselective membrane, comprising the steps of: providing a heat-resistant porous polymeric membrane as a support; feeding a compound selected from the group consisting of 4-methyl-1-pentene, 4-methyl-2-pentene, 2,4,4-trimethyl-1-pentene, 4,4-dimethyl-1-pentene, tert-butylamine, and their flourine-containing derivatives, or from the group consisting of vinyl trimethylsilane, hexamethyldisilazane, dimethylaminotrimethylsilane, and trimethylsilylimidazole, said compound being fed into an atmosphere of 1.0 Torr or less under glow discharge of from 20 to 80 W in order to polymerize the compound and form a thin membrane; and depositing the thin membrane on the heat-resistant porous polymeric membrane.

Claim 11

The process as claimed in claim 8 wherein a siloxane compound is cross-linked in the pores of the heat-resistant porous polymeric membrane by cross-linking in a plasma atmosphere of unpolymerizable gas at a pressure of 1.0 Torr or less.

Claim 12

The process as claimed in claim 9, wherein uncured siloxane is extracted and removed from the surface of the heat-resistant porous polymeric membrane support which does not come into contact with the plasma used to cross-link the siloxane.

Claim 13

The process according to claim 10, wherein the siloxane compound which is subjected to cross-linking is a silicone oil.

Claim 14

The process according to claim 11, wherein the membrane support is impregnated with the silicone oil, the membrane suppport is heated, an excess of the silicone oil which appears on the surface of the membrane support is removed, the membrane support is cooled, and the membrane support is exposed to the plasma to effect cross-linking of the silicone oil.