Hollow fiber membranes and methods for forming same

Patent metadata

Field	Value
Publication number	US-9289730-B2
Application number	US-201313945459-A
Country	US
Kind code	B2
Filing date	Jul 18, 2013
Priority date	Jul 18, 2013
Publication date	Mar 22, 2016
Grant date	Mar 22, 2016

Abstract

The invention provides improved hollow fiber membranes having at least two layers, and methods for forming the same. The methods include co-extruding a first composition, a second composition, and a third composition to form a dual layer hollow fiber membrane. The first composition includes a glassy polymer; the second composition includes a polysiloxane; and the third composition includes a bore fluid. The dual layer hollow fiber membranes include a first layer and a second layer, the first layer being a porous layer which includes the glassy polymer of the first composition, and the second layer being a polysiloxane layer which includes the polysiloxane of the second composition.

First claim

The invention claimed is:

1. A method of forming a hollow fiber membrane comprising two layers, said method comprising co-extruding a first composition, a second composition, and a third composition to form a dual layer hollow fiber membrane,
said first composition comprising a glassy polymer,
said second composition comprising a polysiloxane, and
said third composition comprising a bore fluid,

wherein the dual layer hollow fiber membrane comprises a first layer and a second layer, the first layer being a porous layer comprising the glassy polymer of the first composition, and the second layer being a polysiloxane layer comprising the polysiloxane of the second composition.

2. The method according to claim 1 , wherein the first layer is an inner layer, and the second layer is an outer layer in direct contact with the inner layer; and
the polysiloxane is polydimethylsiloxane (PDMS) or
the polysiloxane is a silicone-polyimide block copolymer.

3. The method according to claim 2 , wherein the glassy polymer is selected from the group consisting of cellulose acetate, polysulfones, regenerated cellulose, cellulose triacetate, polyether sulfone, polyetherimide, polyvinylidenefluoride, aromatic polyamides, aliphatic polyamides, polyimides, polyamide-imides, polyetherimides, polyetheresters, polysulfones, polyvinylidenechloride, polybenzimidazoles, polybenzoxazoles, polyacrylonitrile, polyamide esters, and polyesters, and combinations, copolymers, and substituted polymers thereof.

4. The method according to claim 2 , wherein the bore fluid comprises N-methylpyrrolidone and water.

5. The method according to claim 2 , wherein the second composition further comprises porous silica particles.

6. The method according to claim 5 , wherein the porous silica particles are selected from fumed silica, aluminosilicates, and combinations thereof.

7. The method according to claim 2 , wherein the polysiloxane is an air, moisture, and/or heat curable PDMS and the second composition further comprises a solvent within which the PDMS is soluble.

8. The method according to claim 7 , wherein the solvent is a hydrocarbon solvent.

9. The method according to claim 8 , wherein the solvent is hexane or heptane.

10. The method according to claim 7 , wherein the second composition comprises:
10-80 wt % PDMS; and
30-90 wt % solvent.

11. The method according to claim 10 , wherein the second composition comprises:
45-55 wt % PDMS; and
45-55 wt % solvent.

12. The method according to claim 11 , wherein the solvent is hexane.

13. The method according to claim 2 , wherein the hollow fiber membrane is capable of separating carbon dioxide and/or nitrogen gas from a liquid or gaseous mixture.

14. The method according to claim 2 , wherein, following co-extruding, an intermediate to the dual layer hollow fiber membrane is contacted with an aqueous solution.

15. The method according to claim 14 , wherein the temperature of the aqueous solution is 15° C. to 60° C.

16. The method according to claim 2 , further comprising forming on the dual layer hollow fiber membrane one or more additional layers.

17. The method according to claim 16 , wherein at least one of the one or more additional layers or the polysiloxane layer itself comprises a material capable of gas separation.

18. The method according to claim 2 , wherein, during co-extruding,
the first composition is extruded at a flow rate, f 1 , of 180 to 600 mL/h;
the second composition is extruded at a flow rate, f 2 , where the ratio of f 2 :f 1 is 1:30 to 1:10; and
the third composition is extruded at a flow rate, f 3 , where the ratio of f 3 :f 1 is 1:3 to 1:2.

19. A method of forming a hollow fiber membrane comprising two layers, said method comprising co-extruding a first composition, a second composition, and a third composition to form a dual layer hollow fiber membrane,
said first composition comprising a glassy polymer,
said second composition comprising a polysiloxane, and
said third composition comprising a bore fluid,

wherein the dual layer hollow fiber membrane comprises a first layer and a second layer, the first layer being a porous layer comprising the glassy polymer of the first composition, and the second layer being a polysiloxane layer comprising the polysiloxane of the second composition and the second layer has an average thickness of less than 1 μm.

20. The method according to claim 19 , wherein the first layer is an inner porous layer comprised of the glassy polymer, and the second layer is comprised of an outer polysiloxane layer in direct contact with the inner layer.

Assignees

• Gen Electric

Inventors

• Bhandari Dhaval Ajit
• Mccloskey Patrick Joseph
• Howson Paul Edward
• Narang Kristi Jean
• Koros William

Classifications

• B01D71/027

  Silicium oxide · CPC title

• B01D53/228

  characterised by specific membranes · CPC title

• B29D23/001

  Pipes; Pipe joints (pleated hoses B29D23/18) · CPC title

• B01D2257/102

  Nitrogen · CPC title

• B01D71/70 Primary

  Polymers having silicon in the main chain, with or without sulfur, nitrogen, oxygen or carbon only · CPC title