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An air dehydration membrane is made of a hydrophilic polymer having a permeability for water vapor which is greater than its permeability for air, and having low selectivity between oxygen and nitrogen. The membrane has a hydrophilic coating, which itself may be a polymer. The coating does not affec

An air dehydration membrane is made of a hydrophilic polymer having a permeability for water vapor which is greater than its permeability for air, and having low selectivity between oxygen and nitrogen. The membrane has a hydrophilic coating, which itself may be a polymer. The coating does not affect the selectivity of the coated membrane with respect to oxygen and nitrogen, but does increase selectivity of the membrane with respect to water vapor. A preferred material for the membrane is polysulfone. Preferred materials for the coating are poly vinyl alcohol and Triton X-100. The membrane is selected such that the dominant mechanism for gas flow through the membrane is Knudsen flow. The membranes are made at low cost, and can outperform existing commercial membranes in either volumetric productivity or product recovery.

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What is claimed is: 1. An air dehydration membrane comprising a hydrophilic polymer having a permeability for water vapor which is greater than its permeability for air, said hydrophilic polymer also showing low selectivity between oxygen and nitrogen, the polymer having a hydrophilic coating, wher

What is claimed is: 1. An air dehydration membrane comprising a hydrophilic polymer having a permeability for water vapor which is greater than its permeability for air, said hydrophilic polymer also showing low selectivity between oxygen and nitrogen, the polymer having a hydrophilic coating, wherein the coating is chosen such that the coating does not affect the selectivity of the coated membrane with respect to oxygen and nitrogen, but does increase selectivity of the membrane with respect to water vapor, wherein the membrane in an uncoated condition has a permeability for air in a range of about 2.5-20횞10-4 cm3/cm2쨌sec쨌cmHg, and wherein the membrane is selected such that a dominant mechanism for gas flow through the membrane is Knudsen flow. 2. The membrane of claim 1, wherein the hydrophilic polymer is polysulfone. 3. The membrane of claim 2, wherein the polymer is present in a concentration of about 40% to about 65% by weight. 4. The membrane of claim 1, wherein the coating is selected from the group consisting of poly vinyl alcohol and a non-ionic surfactant. 5. The membrane of claim 2, wherein the coating is selected from the group consisting of poly vinyl alcohol and a non-ionic surfactant. 6. The membrane of claim 5, wherein the membrane has the form of a hollow fiber. 7. The membrane of claim 6, wherein the fiber has a bore side and a shell side, and wherein the coating is formed on the bore side. 8. A method of making an air dehydration membrane, comprising: a) forming a polysulfone polymer into a hollow fiber, the fiber having a bore side and a shell side, the polymer having a permeability for air in a range of about 2.5-20횞10-4 cm3/cm2쨌sec쨌cmHg, and wherein the polymer is constructed such that gas flow through the polymer is primarily Knudsen flow, b) coating the bore side of the fiber with a solution selected from the group consisting of poly vinyl alcohol and a non-ionic surfactant, and c) drying the coated fiber. 9. The method of claim 8, wherein step (a) includes blowing a gas through an annular die so as to form the hollow fiber. 10. The method of claim 8, wherein step (a) includes combining the polymer with a solvent and a non-solvent to form a spin dope, and extruding the spin dope to form the hollow fiber. 11. The method of claim 10, wherein the solvent is selected to be n-methyl-pyrrolidinone, and wherein the non-solvent is selected to be tri-ethylene glycol. 12. The method of claim 10, wherein the solvent and non-solvent are selected to be present in a ratio of about 2.0 to about 4.0 of solvent to non-solvent. 13. The method of claim 10, wherein the polymer is present in a concentration of about 40% to about 65% by weight. 14. The method of claim 10, wherein step (a) includes the step of removing solvent and non-solvent from the fiber. 15. The method of claim 8, wherein step (b) includes selecting a concentration of the solution of poly vinyl alcohol to be about 4%. 16. The method of claim 8, wherein step (c) includes air drying and heat treating the coated fiber. 17. The membrane of claim 1, wherein the coating consists essentially of an aqueous solution of poly vinyl alcohol. 18. The membrane of claim 1, wherein the coating consists essentially of an aqueous solution of a surfactant. 19. The method of claim 8, wherein the coating step comprises coating the bore side of the fiber with a solution which consists essentially of an aqueous solution of poly vinyl alcohol. 20. The method of claim 8, wherein the coating step comprises coating the bore side of the fiber with a solution which consists essentially of an aqueous solution of a surfactant.