Composite membranes and their manufacture and use

Claim 2

A process for forming a composite hollow fiber membrane for fluid separation comprising: (i) coating a preformed porous hollow fiber substrate with a membrane-forming material and a solvent therefor by applying said composition to said porous hollow fiber substrate; (ii) conveying the porous hollow fiber substrate coated with said composition through a gaseous atmosphere to evaporate some but not all of the solvent in said composition from the surface of said coated porous hollow fiber substrate; (iii) conveying such partially dried coated porous hollow fiber substrate whose coated surface has made no contact with a solid surface from the time said membrane-forming composition solution was applied to the surface of the porous hollow fiber substrate into a liquid coagulation bath wherein the membrane-forming material is coagulated on the surface of said porous hollow fiber substrate and the solvent for said membrane-forming material is dissolved in the liquid coagulation bath; and (iv) recovering a composite hollow fiber membrane having a coating with a thin, substantially smooth membrane separation layer, having a thickness down to about 500 angstroms, on said porous substrate, said thin, smooth membrane separation layer being essentially free of voids and pinholes.

Claim 3

A process for forming a composite hollow fiber membrane as claimed in claim 1, wherein said solvent solution comprises one or more solvents for the membrane-forming material.

Claim 4

A process for forming a composite hollow fiber membrane as claimed in claim 1, wherein said solvent solution comprises one or more solvents for the membrane-forming material and one or more non-solvents for the membrane-forming material.

Claim 5

A process for forming a composite hollow fiber membrane as claimed in claim 1, wherein the temperature of said membrane-forming composition is from about 0° C. to about 70° C.

Claim 6

A process for forming a composite hollow fiber membrane as claimed in claim 1, wherein the temperature of said membrane-forming composition is ambient temperature.

Claim 7

A process for forming a composite hollow fiber membrane as claimed in claim 1, wherein drying step (ii) is for about 1 to 80 seconds.

Claim 8

A process for forming a composite hollow fiber membrane is claimed in claim 1, wherein drying step (ii) is for about 10 to 20 seconds.

Claim 9

A process for forming a composite hollow fiber membrane as claimed in claim 1, wherein the temperature of said liquid coagulation bath is from about 0° C. to about 75° C.

Claim 10

A process for forming a composite hollow fiber membrane as claimed in claim 1, wherein the temperature of said liquid coagulation bath is ambient temperature.

Claim 11

A process for forming a composite hollow fiber membrane as claimed in claim 1, wherein the membrane-forming material comprises from about 0.25 to about 10 weight percent of the membrane-forming composition.

Claim 12

The process of claim 1, wherein the membrane-forming material is cellulose acetate.

Claim 13

The process of claim 1, wherein the membrane-forming material is brominated polyphenylene oxide.

Claim 14

The process of claim 1, wherein the membrane-forming material is tetramethyl bisphenol-A polysulfone polymer.

Claim 15

The process of claim 1, wherein the preformed porous hollow fiber substrate surface has bene prewet before coming into contact with said membrane-forming composition.

Claim 16

The process of claim 1 wherein the porous hollow fiber substrate is polysulfone.

Claim 17

The process of claim 1 in which said thin separation layer has a thickness down to about 700 angstroms.

Claim 18

A composite hollow fiber membrane for fluid separation comprising a coating and a porous hollow fiber substrate, said composite hollow fiber membrane produced by: (i) coating a preformed porous hollow fiber substrate with a membrane-forming composition comprising a solution containing a membrane-forming material and a solvent therefor by applying said composition to said porous hollow fiber substrate; (ii) conveying the porous hollow fiber substrate coated with said composition through a gaseous atmosphere to evaporate some but not all of the solvent in said composition from the surface of said coated porous hollow fiber substrate; (iii) conveying such partially dried coated porous hollow fiber substrate whose coated surface has made no contact with a solid surface from the time it left said membrane-forming composition solution was applied to the surface of the porous hollow fiber substrate into a liquid coagulation bath wherein the membrane-forming material is coagulated on the surface of said porous hollow fiber substrate and the solvent for said membrane-forming material is dissolved in the liquid coagulation bath; and (iv) recovering a composite hollow fiber membrane having a coating with a thin, substantially smooth membrane separation layer, having a thickness down to about 500 angstroms, on said porous substrate, said thin, smooth membrane separation layer being essentially free of voids and pinholes.

Claim 19

A composite hollow fiber membrane for fluid separation comprising a coating and a porous hollow fiber substrate, said composite hollow fiber membrane produced by: (i) coating a preformed porous hollow fiber substrate with a membrane-forming composition comprising a solution containing a membrane-forming material and a solvent therefor by applying said composition to said porous hollow fiber substrate; (ii) conveying the porous hollow fiber substrate coated with said composition through a gaseous atmosphere to evaporate some but not all of the solvent in said composition from the surface of said coated porous hollow fiber substrate; (iii) conveying such partially dried coated porous hollow fiber substrate whose coated surface has made no contact with a solid surface from the time it left said membrane-forming composition solution was applied to the surface of the porous hollow fiber substrate into a liquid coagulation bath wherein the membrane-forming material is coagulated on the surface of said porous hollow fiber substrate and the solvent for said membrane-forming material is dissolved in the liquid coagulation bath; and (iv) recovering a composite hollow fiber membrane having a coating with a thin, substantially smooth membrane separation layer, having a thickness down to about 500 angstroms, on said porous substrate, said thin, smooth membrane separation layer being essentially free of voids and pinholes.

Claim 20

A composite hollow fiber membrane for fluid separation as claimed in claim 17, wherein the membrane-forming composition used to produce said composite hollow fiber membrane comprises a membrane-forming material and one or more solvents for the membrane-forming material.

Claim 21

A composite hollow fiber membrane for fluid separation as claimed in claim 17, wherein the membrane-forming composition used to produce said composite membrane comprises a membrane-forming material and one or more non-solvents for the membrane-forming material.

Claim 22

A composite hollow fiber membrane for fluid separation as claimed in claim 17, wherein the membrane-forming material is cellulose acetate.

Claim 23

A composite hollow fiber membrane for fluid separation as claimed in claim 17, wherein the membrane-forming material is brominated polyphenylene oxide.

Claim 24

A composite hollow fiber membrane for fluid separation as claimed in claim 17, wherein the membrane-forming material is tetramethyl bisphenol-A polysulfone polymer.

Claim 25

A composite hollow fiber membrane for fluid separation as claimed in claim 17, wherein the porous hollow fiber substrate is polysulfone.

Claim 26

The composite hollow fiber membrane of claim 17 in which said thin separation layer has a thickness down to about 700 angstroms.

Claim 27

A process for separating at least one fluid in a fluid mixture from at least one other fluid in said fluid mixture by selective permeation which comprises contacting the fluid mixture with a selectively permeable composite hollow fiber membrane comprising a coating and a porous hollow fiber substrate, said composite hollow fiber membrane produced by: (i) coating a preformed porous hollow fiber substrate with a membrane-forming composition comprising a solution containing a membrane-forming material and a solvent therefor by applying said composition to said porous hollow fiber substrate; (ii) conveying the porous hollow fiber substrate coated with said composition through a gaseous atmosphere to evaporate some but not all of the solvent in said composition from the surface of said coated porous hollow fiber substrate; (iii) conveying such partially dried coated porous hollow fiber substrate whose coated surface has made no contact with a solid surface from the time said membrane-forming composition solution was applied to the surface of the porous hollow fiber substrate into a liquid coagulation bath wherein the membrane-forming material is coagulated on the surface of said porous hollow fiber substrate and the solvent for said membrane-forming material is dissolved in the liquid coagulation bath; and (iv) recovering a composite membrane having a coating with a thin, substantially smooth membrane separation layer, having a thickness down to about 500 angstroms, on said porous substrate, said thin, smooth membrane separation layer being essentially free of voids and pinholes.

Claim 28

A process for separating at least one fluid in a fluid mixture from at least one other fluid in said fluid mixture by selective permeation which comprises contacting the fluid mixture with a selectively permeable composite hollow fiber membrane comprising a coating and a porous hollow fiber substrate, said composite hollow fiber membrane produced by: (i) coating a preformed porous hollow fiber substrate with a membrane-forming composition comprising a solution containing a membrane-forming material and a solvent therefor by applying said composition to said porous hollow fiber substrate; (ii) conveying the porous hollow fiber substrate coated with said composition through a gaseous atmosphere to evaporate some but not all of the solvent in said composition from the surface of said coated porous hollow fiber substrate; (iii) conveying such partially dried coated porous hollow fiber substrate whose coated surface has made no contact with a solid surface from the time said membrane-forming composition solution was applied to the surface of the porous hollow fiber substrate into a liquid coagulation bath wherein the membrane-forming material is coagulated on the surface of said porous hollow fiber substrate and the solvent for said membrane-forming material is dissolved in the liquid coagulation bath; and (iv) recovering a composite membrane having a coating with a thin, substantially smooth membrane separation layer, having a thickness down to about 500 angstroms, on said porous substrate, said thin, smooth membrane separation layer being essentially free of voids and pinholes.

Claim 29

A process for separating at least one fluid in a fluid mixture from at least one other fluid in said fluid mixture as claimed in claim 25, wherein the membrane-forming composition used to produce said composite hollow fiber membrane comprises a membrane-forming material and a solvent solution therefor.

Claim 30

A process for separating at least one gas in a gaseous mixture from at least one other gas in said gaseous mixture as claimed in claim 25, wherein the membrane-forming composition used to produce said composite hollow fiber membrane comprises a membrane-forming material and one or more solvents for the membrane-forming material.

Claim 31

A process for separating at least one fluid in a fluid mixture from at least one other fluid in said fluid mixture as claimed in claim 25, wherein the membrane-forming composition used to produce said composite hollow fiber membrane comprises a membrane-forming material, one or more solvents for the membrane-forming material and one or more non-solvents for the membrane-forming material.

Claim 32

A process for separating at least one fluid in a fluid mixture from at least one other fluid in said fluid mixture as claimed in claim 25, wherein said porous hollow fiber substrate is polysulfone.

Claim 33

A process for separating at least one fluid in a fluid mixture from at least one other fluid in said fluid mixture as claimed in claim 25, wherein the membrane-forming material is cellulose acetate.

Claim 34

A process for separating at least one fluid in a fluid mixture from at least one other fluid in said fluid mixture as claimed in claim 25, wherein the membrane-forming material is brominated polyphenylene oxide.

Claim 35

A process for separating at least one fluid in a fluid mixture from at least one other fluid in said fluid mixture as claimed in claim 25, wherein the membrane-forming material is tetramethyl bisphenol-A polysulfone polymer.

Claim 36

The process of claim 25 in which said thin separation layer has a thickness down to about 700 angstroms.