Surface modified gas separation membranes

Claim 2

A process of separating a gas mixture comprising the steps of: (a) using a membrane fabricated from a polymer selected from the group consisting of polysulfone, polyethersulfone, polystyrene, polyarylate, polycarbonate, ethyl cellulose, styrene-acrylonitrile copolymer, ABS, and poly(4-vinylanisole-4-vinylpyridine), in which the membrane is first formed by extruding, molding, or casting said polymer followed by surface treating the formed membrane by exposure to gaseous fluorine or a combination of gaseous fluorine and sulfur dioxide under conditions such that at least 10 percent of the hydrogen groups at only the membrane surface are replaced by fluorine, thereby minimizing the treatment depth at the membrane surface and resulting in an increase in the selectivity of the treated over the untreated membrane of at least about 10 percent with a minimal decrease in permeability of the treated over the untreated membrane, and contacting the treated side of the membrane with a feed gas mixture under pressure, (b) maintaining a pressure differential across the membrane such that a portion of the feed gas mixture permeates through the membrane from the high pressure side to the low pressure side of the membrane, and (c) removing the permeated gas from the low pressure side of the membrane.

Claim 3

The method of claim 1 wherein the feed gas contains one of the gases chosen from the group of oxygen, nitrogen, methane, or carbon dioxide.

Claim 4

The method of claim 1 wherein the membrane used is asymmetric or a composite.

Claim 5

The method of claim 1 wherein the membrane used is in hollow fiber form.

Claim 6

The method of claim 1 wherein the separation factor for carbon dioxide/methane is 10 or greater.

Claim 7

The method of claim 1 wherein the separation factor for oxygen/nitrogen is 3 or greater.

Claim 8

A process of separating a gas mixture comprising the steps of: a. using a membrane fabricated from a polymer selected from the group consisting of polysulfone, polyethersulfone, polystyrene, polyarylate, polycarbonate, ethyl cellulose, styrene-acrylonitrile copolymer, ABS, and poly(4-vinylanisole-4-vinylpyridine), in which the membrane is first formed by extruding, molding, or casting said polymer followed by surface treating the formed membrane by exposure to gaseous fluorine or a combination of gaseous fluorine and sulfur dioxide under conditions such that at least 10 percent of the hydrogen groups at only the membrane surface are replaced by fluorine, thereby minimizing the treatment depth at the membrane surface and resulting in an increase in the selectivity of the treated over the untreated membrane of at least about 10 percent with a minimal decrease in permeability of the treated over the untreated membrane by exposing the formed membrane to gaseous fluorine at a concentration of between about 4 to about 50 percent by volume at a temperature between about 15 to about 80 degrees Celsius for a treatment time of less than about 60 minutes, and contacting the treated side of the membrane with a feed gas mixture under pressure, b. maintaining a pressure differential across the membrane such that a portion of the feed gas mixture permeates through the membrane from the high pressure side to the low pressure side of the membrane, and c. removing the permeated gas from the low pressure side of the membrane.

Claim 9

A process of separating a gas mixture comprising the steps of: a. using a membrane fabricated from a polymer selected from the group consisting of polysulfone, polyethersulfone, polystyrene, polyarylate, polycarbonate, ethyl cellulose, styrene-acrylonitrile copolymer, ABS, and poly(4-vinylanisole-4-vinylpyridine), in which the membrane is first formed by extruding, molding, or casting said polymer followed by surface treating the formed membrane by exposure to gaseous fluorine or a combination of gaseous fluorine and sulfur dioxide under conditions such that at least 10 percent of the hydrogen groups at only the membrane surface are replaced by fluorine, thereby minimizing the treatment depth at the membrane surface and resulting in an increase in the selectivity of the treated over the untreated membrane of at least about 10 percent with a minimal decrease in permeability of the treated over the untreated membrane by exposing the formed membrane to gaseous fluorine at a concentration of between about 4 to about 50 percent by volume at a temperature between about 15 to about 80 degrees Celsius for a treatment time of less than about 60 minutes, and contacting the treated side of the membrane with a feed gas mixture under pressure, b. maintaining a pressure differential across the membrane such that a portion of the feed gas mixture permeates through the membrane from the high pressure side to the low pressure side of the membrane, and c. removing the permeated gas from the low pressure side of the membrane.

Claim 10

A process of separating a gas mixture comprising the steps of: a. using a membrane fabricated from a polymer selected from the group consisting of polysulfone, polyethersulfone, polystyrene, polycarbonate, ethyl cellulose, styreneacrylonitrile copolymer, ABS, and poly(4-vinylanisole-4-vinylpyridine), in which the membrane is first formed by extruding, molding, or casting said polymer followed by surface treating the formed membrane by exposure to gaseous fluorine or a combination of gaseous fluorine and sulfur dioxide under conditions such that at least 10 percent of the hydrogen groups at only the membrane surface are replaced by fluorine, thereby minimizing the treatment depth at the membrane surface and resulting in an increase in the selectivity of the treated over the untreated membrane of at least about 10 percent with a minimal decrease in permeability of the treated over the untreated membrane, and contacting the treated side of the membrane with a feed gas mixture under pressure, b. maintaining a pressure differential across the membrane such that a portion of the feed gas mixture permeates through the membrane from the high pressure side to the low pressure side of the membrane, and c. removing the permeated gas from the low pressure side of the membrane.

Claim 11

A process of separating a gas mixture comprising the steps of: a. using a membrane fabricated from a polymer selected from the group consisting of polysulfone, polyethersulfone, polystyrene, polycarbonate, ethyl cellulose, styreneacrylonitrile copolymer, ABS, and poly(4-vinylanisole-4-vinylpyridine), in which the membrane is first formed by extruding, molding, or casting said polymer followed by surface treating the formed membrane by exposure to gaseous fluorine or a combination of gaseous fluorine and sulfur dioxide under conditions such that at least 10 percent of the hydrogen groups at only the membrane surface are replaced by fluorine, thereby minimizing the treatment depth at the membrane surface and resulting in an increase in the selectivity of the treated over the untreated membrane of at least about 10 percent with a minimal decrease in permeability of the treated over the untreated membrane, and contacting the treated side of the membrane with a feed gas mixture under pressure, b. maintaining a pressure differential across the membrane such that a portion of the feed gas mixture permeates through the membrane from the high pressure side to the low pressure side of the membrane, and c. removing the permeated gas from the low pressure side of the membrane.