Composite separation membranes and the preparation and use thereof

• US 4,767,422 A
• Filed: 04/08/1987
• Issued: 08/30/1988
• Est. Priority Date: 04/08/1987
• Status: Expired due to Term

• Current Assignee: L'Air Liquide SA
• Original Assignee: Union Carbide Corporation (Dow, Inc.)
• Inventors: Kharas, Gregory, Bikson, Benjamin, Giglia, Salvatore
• Primary Examiner(s): SPITZER, ROBERT H
• Application Number:
  US07/035,783
• Time in Patent Office: 510 Days
• Field of Search: 55/16, 55/68, 55/158, 55/209
• US Class Current: 95/51
• CPC Class Codes: B01D 67/0088 Physical treatment with compounds, e.g. swelling, coating or impregnation

Abstract

Composite membranes are post-treated by contact with a volatile solvent, with or without minute amounts of additives, followed by solvent evaporation, to repair defects in the thin separation layer thereof.

Claims

1. A process for repairing a composite membrane suitable for gas, pervaporation or prestructure separations comprising a separation layer that determines the separation characteristics of the membrane and a porous support layer, said separation layer containing imperfections therein, said process consisting essentially of:

(a) contacting said separation layer with a volatile post-treatment solution system comprising a volatile solvent having essentially non-solvent or mild swelling characteristics with respect to the composite membrane materials, said solvent containing minute amounts of non-volatile additives as it contacts and fills said imperfections; and

(b) evaporating said volatile solvent from the composite membrane, said minute amounts of additives remaining in and serving to plug preferentially and essentially said imperfections only,

whereby the post-treatment process serves to effectively repair the separation layer of the composite membrane, enhancing the selectivity thereof and enabling advantageous combinations of selectivity and permeability to be achieved by the use thereof.

2. The process of claim 1 in which the volatile solution system is contacted with the separation layer of the composite membrane that is incorporated into a separatory module.

3. The process of claim 2 in which said volatile solution system is brought into contact with the permeate side of the separatory module and including applying a differential pressure from the permeate to the feed side of the separatory module.

4. The process of claim 3 in which the pressure differential is applied by the drawing of a vacuum on the feed side of the separatory module.

5. The process of claim 2 in which said volatile solution system is brought into contact with the feed side of the separatory module and including applying a differential pressure from the feed side to the permeate side of the separator module.

6. The process of claim 5 in which the pressure differential is applied by the drawing of a vacuum on the permeate side of the separatory module.

7. The process of claim 1 in which the volatile solvent is evaporated from one side of the composite membrane only.

8. The process of claim 1 in which the composite membrane is in hollow fiber form.

9. The process of claim 8 in which the separation layer of the composite membrane comprises a polymeric material.

10. The process of claim 8 in which said support layer comprises polysulfone.

11. The process of claim 1 in which said volatile solution system consists essentially of volatile solvent only, the solvent containing minute amounts of additives through the leaching thereof from the materials of said composite membrane itself.

12. The process of claim 1 in which said volatile solution system used to contact the separation layer comprises a volatile solvent and a small amount of non-volatile additives incorporated therein.

13. The process of claim 12 in which said additives comprise dissolved polymer.

14. The process of claim 12 in which said additives comprise suspended colloidal particles.

15. The process of claim 12 in which said additives comprise dissolved low molecular weight, essentially non-volatile additives.

16. The process of claim 1 in which said combination of steps (a) and (b) are carried out consecutively more than once.

17. A post-treated composite membrane suitable for gas, pervaporation or prestructure separations comprising a separation layer that determines the separation characteristics of the membrane and a porous support layer, said separation layer containing imperfections that are plugged by minute amounts of additives, said composite membrane having been post-treated for the repair of said imperfections by a process consisting essentially of:

(a) contacting said separation layer with a volatile post-treatment solution system comprising a volatile solvent having essentially non solvent or mild swelling characteristics with respect to the composite membrane materials, said solvent containing minute amounts of non-volatile additives as it contacts and fills said imperfections; and

(b) evaporating said volatile solvent from the composite membrane, said minute amounts of additives remaining in and serving to plug preferentially and essentially said imperfections only, whereby the post-treatment process serves to repair the separation layer of the composite membrane, enhancing the selectivity thereof and enabling advantageous combinations of selectivity and permeability to be achieved by the use thereof.

18. The composite membrane of claim 17 in which the post-treatment process is carried out following incorporation of said composite membrane into a separatory module.

19. The composite membrane of claim 18 in which the composite membrane is in hollow fiber form.

20. The composite membrane of claim 19 in which the separation layer thereof comprises a polymeric material.

21. The composite membrane of claim 20 in which said volatile solution system has a solubility parameter of at least about 1.5 units higher or lower than that of the composite membrane materials.

22. An improved process for the separation of a more permeable component of a fluid feed mixture from a less permeable component thereof by gas, pervaporation or perstructure separations, including contacting said feed mixture with the feed side of a composite membrane suitable for gas, pervaporation or prestructure separation operations, and separately withdrawing said more permeable component as a permeate stream and said less permeable component as a non-permeate stream, said composite membrane having a separation layer that determines the separation characteristics of the membrane and a porous support layer, said composite membrane having been post-treated by a process consisting of:

(a) contacting said separation layer with a volatile post-treatment solution system comprising a volatile solvent having essentially non-solvent or mild swelling characteristics with respect to the composite membrane materials, said solvent containing minute amounts of non-volatile additives as it contacts and fills said imperfections; and

(b) evaporating said volatile solvent from the composite membrane, said minute amounts of additives remaining in and serving to plug preferentially and essentially said imperfections only, whereby the post-treatment process serves to repair the separation layer of the composite membrane, enhancing the selectivity thereof and enabling advantageous combinations of selectivity and permeability to be achieved in said separation process.

23. The process of claim 22 in which said post-treatment process is carried out following incorporation of said composite membrane into a separatory module.

24. The process of claim 22 in which the composite membrane is in hollow fiber form.

25. The process of claim 22 in which said feed mixture comprises a mixture of carbon dioxide and methane.

26. The process of claim 22 in which said feed mixture comprises ammonia purge gas and said permeate gas comprises hydrogen.

27. The process of claim 22 in which said feed mixture comprises air and said permeate gas comprises oxygen.

28. The process of claim 22 in which said feed mixture comprises a mixture of alcohol and water and the permeate is a gas comprising water.