Method of separating a gas using at least one membrane in contact with an organosilicon fluid

Patent metadata

Field	Value
Publication number	US-9731245-B2
Application number	US-201314413231-A
Country	US
Kind code	B2
Filing date	Sep 25, 2013
Priority date	Sep 26, 2012
Publication date	Aug 15, 2017
Grant date	Aug 15, 2017

Abstract

The present invention relates to a method of removing a gas from a mixture. The method includes contacting a silicone membrane with a feed mixture including at least a first gas component and contacting a second side of the membrane with an organosilicon sweep liquid, producing a retentate mixture depleted in the first gas component and an organosilicon sweep liquid enriched in the first gas component. The invention also provides methods of removing a gas from a liquid, and methods of regenerating and recycling an organosilicon sweep liquid.

First claim

We claim:

1. A method of removing a gas from a mixture, the method comprising:
contacting a first side of a first dense silicone membrane, wherein the first dense silicone membrane is a free-standing membrane, with a feed mixture comprising a first gas component and at least one of a second gas component and a first liquid component; and
contacting a second side of the membrane with a sweep liquid consisting essentially of an organosilicon fluid consisting essentially of a silane, a polysilane, a siloxane, a polysiloxane or a combination of two or more of a silane, a polysilane, a siloxane, and a polysiloxane, to produce a permeate mixture on the second side of the membrane and a retentate mixture on the first side of the membrane, wherein the permeate mixture is enriched in the first gas component, and the retentate mixture is depleted in the first gas component.

2. The method of claim 1 , wherein the first dense silicone membrane is a nonporous silicone membrane.

3. The method of claim 1 , wherein the first dense silicone membrane is a hollow fiber membrane module comprising a bundle of hollow fibers, wherein the fibers collectively have a bore side and a shell side, wherein at least one of
the first side of the hollow fiber membrane is the bore side and the second side of the hollow fiber membrane is the shell side, and
the first side of the hollow fiber membrane is the shell side and the second side of the hollow fiber membrane is the bore side.

4. The method of claim 1 , wherein the organosilicon fluid comprises at least one of an organosiloxane and an organosilane.

5. The method of claim 1 , wherein the organosilicon fluid comprises at least one at least one silicon-bonded hydroxy group, at least one silicon-bonded ether, at least one silicon-bonded polyether, or a combination thereof.

6. The method of claim 5 , wherein the silicon-bonded hydroxy group, silicon-bonded ether, or at least one silicon-bonded polyether is bonded to a non-terminal-silicon.

7. The method of claim 1 , wherein the feed mixture comprises water vapor and the permeate mixture is enriched in water vapor.

8. A method of removing a gas from a mixture, the method comprising:
contacting a first side of a first dense silicone membrane with a feed mixture comprising a first gas component and at least one of a second gas component and a first liquid component; and
contacting a second side of the membrane with a sweep liquid consisting essentially of an organosilicon fluid consisting essentially of a silane, a polysilane, a siloxane, a polysiloxane or a combination of two or more of the silane, the polysilane, the siloxane, and the polysiloxane, wherein the silane, the polysilane, the siloxane, the polysiloxane or the combination of two or more of the silane, the polysilane, the siloxane, and the polysiloxane comprises at least one of a hydroxy group, an ether group, an acrylate group, a methacrylate group, an acrylamide group, a methacrylamide group, and a polyether group, to produce a permeate mixture on the second side of the membrane and a retentate mixture on the first side of the membrane, wherein the permeate mixture is enriched in the first gas component, and the retentate mixture is depleted in the first gas component.

9. The method of claim 8 , wherein the first dense silicone membrane is a hollow fiber membrane module comprising a bundle of hollow fibers, wherein the fibers collectively have a bore side and a shell side, wherein at least one of
the first side of the hollow fiber membrane is the bore side and the second side of the hollow fiber membrane is the shell side, and
the first side of the hollow fiber membrane is the shell side and the second side of the hollow fiber membrane is the bore side.

10. The method of claim 8 , wherein the organosilicon fluid comprises at least one of an organosiloxane and an organosilane.

11. The method of claim 8 , wherein the organosilicon fluid comprises at least one at least one silicon-bonded hydroxy group, at least one silicon-bonded ether, at least one silicon-bonded polyether, or a combination thereof.

12. The method of claim 11 , wherein the silicon-bonded hydroxy group, silicon-bonded ether, or at least one silicon-bonded polyether is bonded to a non-terminal-silicon.

13. The method of claim 8 , wherein the feed mixture comprises carbon dioxide and at least one of nitrogen and methane and the permeate mixture is enriched in carbon dioxide.

14. The method of claim 8 , wherein the feed mixture comprises water vapor and the permeate mixture is enriched in water vapor.

15. The method of claim 8 , wherein the first dense silicone membrane is a free-standing membrane.

16. A method of removing a gas from a liquid, the method comprising:
contacting a first side of a first dense silicone membrane with a gaseous stream; and
contacting a second side of the membrane with a liquid consisting essentially of an organosilicon fluid consisting essentially of a first gas component and a silane, a polysilane, a siloxane, a polysiloxane or a combination of two or more of the silane, polysilane, siloxane, and polysiloxane and where the silane, polysilane, siloxane, polysiloxane or the combination of two or more of the silane, polysilane, siloxane, and polysiloxane comprises at least one of a hydroxy group, an ether group, an acrylate group, a methacrylate group, an acrylamide group, a methacrylamide group, and a polyether group, to produce a gaseous permeate mixture on the first side of the membrane and a retentate organosilicon fluid on the second side of the membrane, wherein the permeate mixture is enriched in the first gas component, and the retentate organosilicon fluid is depleted in the first gas component.

Assignees

• Dow Corning

Inventors

• Ahn Dongchan
• Greiner Aaron
• Hrabal James
• Lichtor Alexandra

Classifications

• B01D69/04

  Tubular membranes · CPC title

• B01D2252/205

  Other organic compounds not covered by B01D2252/00 - B01D2252/20494 · CPC title

• B01D53/1425

  Regeneration of liquid absorbents · CPC title

• B01D2257/102

  Nitrogen · CPC title

• B01D2257/104

  Oxygen · CPC title