Polymer membranes on the basis of polyvinylidene fluoride, a process for the production thereof and their use

• US 5,151,193 A
• Filed: 11/02/1990
• Issued: 09/29/1992
• Est. Priority Date: 02/15/1989
• Status: Expired due to Fees

• Current Assignee: Fraunhofer Gesellschaft Zur Foerderung Der Angewandten Forsching E.V.
• Original Assignee: Fraunhofer Gesellschaft Zur Foerderung Der Angewandten Forsching E.V.
• Inventors: Grobe, Anneliese, Chmiel, Horst
• Primary Examiner(s): SPEAR JR, FRANK
• Application Number:
  US07/613,861
• Time in Patent Office: 697 Days
• Field of Search: 210/490, 210/500.42, 210/500.41, 210/500.23, 210/651, 210/652, 427/245, 427/246, 264/41, 264/49
• US Class Current: 210/651
• CPC Class Codes: B01D 67/0088 Physical treatment with compounds, e.g. swelling, coating or impregnation
• CPC Class Codes: B01D 71/34 Polyvinylidene fluoride
• CPC Class Codes: B01D 71/5222 Polyetherketone, polyetheretherketone, or polyaryletherketone
• CPC Class Codes: C08J 2471/00 Characterised by the use of polyethers obtained by reactions forming an ether link in the main chain; Derivatives of such polymers
• CPC Class Codes: C08J 7/0427 with only one layer of a composition containing a polymer binder with more layers C08J7/042
• CPC Class Codes: C08L 2666/14 Macromolecular compounds according to C08L59/00 - C08L87/00; Derivatives thereof
• CPC Class Codes: C08L 27/16 Homopolymers or copolymers or vinylidene fluoride

Abstract

The present invention relates to polymer membranes on the basis of polyviidene fluoride (PVDF), a process for the production thereof and their use for ultrafiltration. The membranes are produced according to known techniques from homogeneous solutions containing 5 to 30% by weight of PVDF and 0.01 to 30% by weight of sulfonic acids and/or their salts, obtainable by sulfonation of the polyetheretherketones of formula (I) and/or subsequent neutralization of the sulfonic acids. The membranes are then treated with methanolic solutions containing 0.1 to 5% by weight of the above-mentioned sulfonic acids and/or their salts. This process supplies membranes having excellent hydrophilic properties, high thermal and mechanical stabilities and high trans-membrane flows.

--(--O--p--C.sub.6 H.sub.4 --O--p--C.sub.6 H.sub.4 --CO--p--C.sub.6 H.sub.4

--)_n -- (I)

Claims

1. A process for the production of polymer membranes on the basis of polyvinylidene fluoride (PVDF), wherein a homogeneous solution L1 containing

a) 5 to 30% by weight of PVDF and

b) 0.01 to 30% by weight of at least one sulfonic acid (PEEKSO₃ H) salt obtained by sulfonating the polyetheretherketone (PEEK, poly(oxy-1,4-phenyleneoxy-1,4-phenylene-carbonyl-1,4-phenylene)) of formula (I)

View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31, 32, 33, 34, 35)

2. The process according to claim 1, wherein homogeneous solution L1 contains

a) 5 to 30% by weight of PVDF and

b) 0.01 to 1% by weight of the sulfonic acid PEEKSO₃ H or their salts.

3. The process according to claim 1, wherein sulfonic acid PEEKSO₃ H or salt used was obtained by sulfonating polyether etherketone PEEK of formula (I), wherein n represents values between 35 and 350.

4. The process according to claim 3, wherein sulfonic acid PEEKSO₃ H or salt used was obtained by sulfonating polyetheretherketone of formula (I), wherein n represents values between 50 and 300.

5. The process according to claim 1 wherein the sulfonic acid PEEKSO₃ H or salts used has a sulfur content of 1 to 9% by weight, based upon the sulfonic acid PEEKSO₃ H.

6. The process according to claim 5, wherein the sulfonic acid PEEKSO₃ H or salt used has a sulfur content of 2 to 7% by weight, based upon the sulfonic acid PEEKSO₃ H.

7. The process according to claim 1 wherein homogeneous solution L1 has a solids content is 20 to 40% by weight.

8. The process according to claim 7, wherein homogeneous solution L1 has a solids content of 30% by weight.

9. The process according to claim 1 wherein the sodium salt PEEKSO₃ Na of the sulfonic acid PEEKSO₃ H is used.

10. The process according to claim 1 wherein the ammonium salt PEEKSO₃ NH₄ of the sulfonic acid PEEKSO₃ H is used.

11. The process according to claim 1 wherein the zinc salt PEEKSO₃ Zn_1/2 of the sulfonic acid PEEKSO₃ H is used.

12. The process according to claim 1 wherein a dipolar, aprotic solvent is used as the solvent for the homogeneous solution L1.

13. The process according to claim 12, wherein the solvent used is at least one of dimethylformamide, N-methylpyrrolidone, dimethylacetamide and dimethylsulfoxide.

14. The process according to claim 1 wherein 0.25 to 1 g/l of a surfactant is present in homogeneous solution L1.

15. The process according to claim 14, wherein the surfactant is anionic.

16. The process according to claim 15, wherein a perfluorooctane sulfonate is used as the anionic surfactant.

17. The process according to claim 16, wherein the tetraethylammoniumperfluorooctane sulfonate of formula (II)

18. The process according to claim 1 wherein the membrane is precipitated at temperatures ranging between -20°

C. and +50°

C.

19. The process according to claim 18 wherein water is used as the precipitating agent for the membrane.

20. The process according to claim 18 wherein a water/solvent mixture is used as the precipitating agent for the membrane.

21. The process according to claim 20, wherein a dipolar, aprotic solvent is used as the solvent.

22. The process according to claim 21, wherein the solvent used is at least one of dimethylformamide, N-methylpyrrolidone, dimethylacetamide and dimethylsulfoxide.

23. The process according to claim 1 wherein a water/solvent mixture having 0 to 50% by weight of solvent is used.

24. The process according to claim 23, wherein a water/solvent mixture having 5 to 50% of solvent is used.

25. The process according to claim 1 wherein methanolic solution L2 contains 0.5 to 2% by weight of the sulfonic acid PEEKSO₃ H or salt.

26. The process according to claim 1 wherein the methanolic solution L2 is sprayed onto the polymer membrane.

27. The process according to claim 1 wherein the methanolic solution L2 is brushed onto the polymer membrane.

28. The process according to claim 1 wherein the polymer membrane is immersed in the methanolic solution L2.

29. The process according to claim 1 wherein the sulfonic acid PEEKSO₃ H or salt, present on the membrane surface, is cross-linked with Ca⁺⁺ ions.

30. Polymer membrane produced according to a process as defined in claim 1.

31. The polymer membrane according to claim 30, which is a flat membrane.

32. Polymer membrane according to claim 30, which is a tubular membranes.

33. Polymer membrane according to claim 30, which is a capillary membranes.

34. Polymer membrane according to claim 30, which is a hollow fiber.

35. In a method of ultrafiltration in which the material to be ultrafiltered is passed through an ultrafiltration membrane, the improvement which comprises employing the polymer membrane of claim 30 as the ultrafiltration membrane.