Designed selectivity gas permeable membranes

• US 6,406,517 B1
• Filed: 09/08/2000
• Issued: 06/18/2002
• Est. Priority Date: 09/08/2000
• Status: Expired due to Fees

• Current Assignee: Cms Technologies Holdings, Inc.
• Original Assignee: Cms Technologies Holdings, Inc.
• Inventors: Shanbhag, Purushottam V., Avery, Daniel Lee
• Primary Examiner(s): Spitzer, Robert H.
• Application Number:
  US09/658,187
• Time in Patent Office: 648 Days
• Field of Search: 95/45, 95/47--55, 96/4, 96/13, 96/14, 555/24, 55D/IG.5
• US Class Current: 95/45
• CPC Class Codes: B01D 2323/12 Specific ratios of components used
• CPC Class Codes: B01D 53/228 characterised by specific membranes
• CPC Class Codes: B01D 67/0002 Organic membrane manufacture
• CPC Class Codes: B01D 69/141 Heterogeneous membranes, e.g. containing dispersed material; Mixed matrix membranes
• CPC Class Codes: B01D 71/06 Organic material
• CPC Class Codes: B01D 71/32 containing fluorine atoms
• CPC Class Codes: B01D 71/44 Polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds, not provided for in a single one of groups B01D71/26-B01D71/42
• CPC Class Codes: Y10S 55/05 Methods of making filter

Abstract

The separation factor with respect to a gas binary of a selectively gas permeable membrane of a fluoropolymer can be increased by fabricating the membrane from a composition of a blend of the fluoropolymer with a nonfugitive, nonpolymeric fluorinated adjuvant. The composition can be made by dissolving the adjuvant and the polymer in a suitably compatible solvent then forming the membrane from the solution for example by casting, dipping, or spraying the solution on a substrate and devolatilizing the solvent. The extent of the selectivity increase varies widely with the combination of fluoropolymer and adjuvant and largely increases in direct relation with the proportion of adjuvant in the membrane composition. Novel membranes of fluoropolymers adapted for separation of chemically aggressive gases can be made to have higher selectivity than previously available from the adjuvant free fluoropolymers

Claims

1. A process for separating gases present in a gas mixture comprising contacting the gas mixture with one side of a selectively gas permeable membrane having a membrane separation factor with respect to two gases in the mixture, the membrane comprising a blend of a major fraction of a fluoropolymer of which a nonporous membrane exhibits a fluoropolymer separation factor with respect to the two gases, and an amount of a nonfugitive, nonpolymeric fluorinated adjuvant having an atmospheric boiling point at least about 200°

C., the amount being effective to make the membrane separation factor greater than the fluoropolymer separation factor.

2. The process of claim 1 in which the two gases are chlorine and hydrogen.

3. The process of claim 1 in which one of the two gases is hydrogen fluoride.

4. A membrane composition for separation of components of a mixture including a more preferentially permeable gas and a less preferentially permeable gas of a binary gas combination comprising a nonporous gas permeable membrane of a blend comprising about 50-99 wt % of a fluoropolymer and an amount of a nonfugitive, nonpolymeric fluorinated adjuvant effective to produce a separation factor of the membrane with respect to the two gases of the binary gas combination greater than the separation factor of a membrane consisting essentially of the fluoropolymer.

5. The composition of claim 4 in which the fluoropolymer comprises at least one monomer selected from the group consisting of tetrafluoroethylene, chlorotrifluoroethylene, perfluoro-2,2-dimethyl-1,3-dioxole, 2,2,4-trifluoro-5-trifluoromethyl-1,3-dioxole, hexafluoropropylene, vinylidene fluoride, and a perfluoroalkylvinyl ether.

6. The composition of claim 5 in which the monomer is perfluoro-2,2-dimethyl-1,3-dioxole.

7. The composition of claim 6 in which the adjuvant is perfluoroperhydrophenanthrene.

8. The composition of claim 4 in which the adjuvant is a pertluorinated hydrocarbon having a molecular weight of about 500-3000.

9. The composition of claim 8 in which the adjuvant is perfluoroperhydrophenanthrene.

10. The composition of claim 4 in which the adjuvant is a fluorinated liquid selected from the group consisting of FC-70, perfluoroalkylether and a mixture of them.

11. The composition of claim 4 in which the fluoropolymer is a copolymer comprising copolymerized perfluoro-2,2-dimethyl-1,3-dioxole and chlorotrifluoroethylene and in which the adjuvant comprises perfluoroperhydrophenanthrene.

12. A gas separation device comprising a selectively gas permeable membrane having a membrane separation factor with respect to two gases, the membrane comprising a blend of a major fraction of a fluoropolymer of which a nonporous membrane exhibits a fluoropolymer separation factor with respect to the two gases, and an amount of a nonfugitive, nonpolymeric fluorinated adjuvant effective to make the membrane separation factor greater than the fluoropolymer separation factor.

13. The device of claim 12 in which the selectively gas permeable membrane comprises a blend of about 50-99 wt % of a fluoropolymer comprising at least one monomer selected from the group consisting of tetrafluoroethylene, chlorotrifluoroethylene, perfluoro-2,2-dimethyl- 1,3 -dioxole, 2,2,4-trifluoro-5-trifluoromethyl-1,3-dioxole, hexafluoropropylene, vinylidene fluoride, and a perfluoroalkylvinyl ether, and a complementary amount of perfluoroperhydrophenanthrene and in which the selectively gas permeable membrane is supported by a porous substrate adjacent to the selectively gas permeable membrane.

14. The device of claim 13 in which the porous substrate comprises expanded polytetrafluoroethylene.

15. A process for making a gas separation membrane comprising the steps of mixing a fluoropolymer comprising a monomer selected from the group consisting of tetrafluoroethylene, chlorotrifluoroethylene, perfluoro-2,2-dimethyl-1,3-dioxole, 2,2,4-trifluoro-5-trifluoromethyl- 1,3-dioxole hexafluoropropylene, vinylidene fluoride and a perfluoroalkylvinyl ether, and a nonfugitive, nonpolymeric fluorinated adjuvant to obtain a uniform composition of which the fluoropolymer comprises a major fraction, and fabricating a nonporous gas permeable membrane of about 0.05-50 μ

m thickness from the composition.

16. The process of claim 15 in which the mixing step comprises blending the fluoropolymer and the adjuvant in a liquid solution comprising a fluorinated solvent.

17. The process of claim 16 in which the mixing step comprises dissolving the fluoropolymer in a first fluorinated solvent to form a first solution of about 0.5-10 wt. % fluoropolymer in the first fluorinated solvent and dissolving the adjuvant in a second fluorinated solvent to form a second solution of about 0.5-10 wt. % of the adjuvant in the second fluorinated solvent, and combining an amount of the first solution with an amount of the second solution to form the liquid solution of the uniform composition dissolved in the fluorinated solvent.

18. The process of claim 17 in which the fabricating step comprises evaporating the fluorinated solvent from the liquid solution to produce a substantially solvent free membrane of the composition.

19. The process of claim 18 in which the fabricating step further comprises spraying the liquid solution onto a surface of a porous substrate prior to evaporating the fluorinated solvent.