Highly porous polyvinylidene difluoride membranes

• US 5,834,107 A
• Filed: 01/22/1997
• Issued: 11/10/1998
• Est. Priority Date: 01/22/1996
• Status: Expired due to Term

• Current Assignee: USF Filtration and Separations Group, Inc. (Siemens AG)
• Original Assignee: USF Filtration and Separations Group, Inc. (Siemens AG)
• Inventors: Wang, I-Fan, Zepf, Robert, Ditter, Jerome F.
• Primary Examiner(s): Bell, James J.
• Assistant Examiner(s): Copenheaver, Blaine R.
• Application Number:
  US08/785,962
• Time in Patent Office: 657 Days
• Field of Search: 428/310.5, 428/315.5, 428/315.7, 210/490, 210/500.23, 210/500.27, 264/41, 264/216, 427/245, 427/244
• US Class Current: 428/310.5
• CPC Class Codes: B01D 2239/0421 Rendering the filter material hydrophilic
• CPC Class Codes: B01D 2239/0428 Rendering the filter material hydrophobic
• CPC Class Codes: B01D 2239/0627 Spun-bonded
• CPC Class Codes: B01D 2239/065 More than one layer present in the filtering material apparatus incorporating such gas filtering material B01D2275/10
• CPC Class Codes: B01D 2239/0654 Support layers
• CPC Class Codes: B01D 2239/0668 The layers being joined by heat or melt-bonding
• CPC Class Codes: B01D 2239/0681 The layers being joined by gluing
• CPC Class Codes: B01D 2239/1216 Pore size
• CPC Class Codes: B01D 2239/1291 Other parameters
• CPC Class Codes: B01D 2323/12 Specific ratios of components used
• CPC Class Codes: B01D 2325/022 Asymmetric membranes
• CPC Class Codes: B01D 2325/04 Characteristic thickness
• CPC Class Codes: B01D 2325/34 Molecular weight or degree of polymerisation
• CPC Class Codes: B01D 2325/36 Hydrophilic membranes
• CPC Class Codes: B01D 39/083 of organic material
• CPC Class Codes: B01D 39/1653 of synthetic origin
• CPC Class Codes: B01D 67/0011 Casting solutions therefor
• CPC Class Codes: B01D 67/0016 Coagulation
• CPC Class Codes: B01D 69/02 characterised by their properties
• CPC Class Codes: B01D 69/08 Hollow fibre membranes manufacture of hollow fibres D01D5/24, D01F1/08
• CPC Class Codes: B01D 71/34 : Polyvinylidene fluoride
• CPC Class Codes: Y10T 428/249961 : With gradual property change within a component
• CPC Class Codes: Y10T 428/249978 : Voids specified as micro
• CPC Class Codes: Y10T 428/249979 : Specified thickness of void-containing component [absolute or relative] or numerical cell dimension

Abstract

The present invention relates to the field synthetic polymeric membrane materials formed from casting polyvinylidene difluoride (PVDF) polymer solutions and/or dispersions. Membranes formed in accordance with the present invention are all highly porous. Both internally isotropic membranes and highly asymmetric PVDF membranes are disclosed. The membranes of the invention are useful in a variety of microfiltration and ultrathin applications.

Claims

1. A microporous polyvinylidene difluoride polymer membrane, the membrane having a microporous surface comprising minimum pores, an opposite surface comprising maximum pores, and a thickness therebetween, the thickness comprising a porous support formed from filamentous webs of polymer material.

2. The membrane of claim 1, further comprising from about 1% to about 30% by weight polyvinylpyrrolidone.

3. The membrane of claim 2, wherein the polyvinylpyrrolidone has an average molecular weight of about 45,000 daltons.

4. The membrane of claim 2, wherein the polyvinylpyrrolidone has an average molecular weight of about 9,000 daltons.

5. The membrane of claim 1, rendered hydrophilic by contacting the membrane with a wetting agent.

6. The membrane of claim 5, wherein the wetting agent comprises hydroxypropylcellulose.

7. The membrane of claim 5, wherein the wetting agent comprises a surfactant.

8. The membrane of claim 1, further comprising a supporting material laminated thereto.

9. The membrane of claim 8, wherein the supporting material is a nonwoven polymer fabric.

10. The membrane of claim 1, wherein the membrane is a hollow fiber.

11. The membrane of claim 1, the membrane having an integral asymmetric structure, the minimum pores of the microporous surface having a first average diameter, and the maximum pores of the opposite surface having a second average diameter, wherein a ratio of the second average diameter to the first average diameter is from about 5 to about 500.

12. The membrane of claim 11, having a flow rate of water of from about 25 to about 500 cm/min at 10 psid.

13. The membrane of claim 11, wherein the thickness is less than about 140 μ

m.

14. The membrane of claim 13, wherein the thickness is less than about 70 μ

m.

15. The membrane of claim 11, having a bubble point of water of from about 0.5 to about 50 psid.

16. The membrane of claim 11, the porous support comprising a gradient of gradually increasing pore sizes from the microporous surface to the opposite surface.

17. The membrane of claim 1, the membrane having an isotropic structure through at least about 80% of the thickness of the membrane.

18. The membrane of claim 17, wherein the thickness is less than about 75 μ

m.

19. The membrane of claim 18, wherein the thickness is less than about 30 μ

m.

20. A method of preparing a polyvinylidene difluoride membrane comprising the steps of:

providing a casting dope comprising between about 12% and 20% by weight of polyvinylidene difluoride and between about 0% and 30% by weight of a hydrophilic polymer, dissolved in a solvent;

casting the dope to form a thin film;

exposing the thin film to a humid gaseous environment;

coagulating the film in a water bath; and

recovering a formed microporous polyvinylidene difluoride polymer membrane, the membrane having a microporous surface comprising minimum pores, an opposite surface comprising maximum pores, and a thickness therebetween, the therebetween thickness comprising a porous support formed from filamentous webs of polymer material.

21. The method of claim 20, wherein the dope has a temperature of between about 21°

C. and about 35°

C. during the casting step.

22. The method of claim 20, wherein the gaseous environment has a relative humidity of water between about 50% and 100%.

23. The method of claim 20, wherein the exposing step has a duration of about 2 seconds to about 120 seconds.

24. The method of claim 20, wherein the water bath has a temperature between about 20°

C. and 80°

C.

25. The method of claim 20, wherein the hydrophilic polymer comprises polyvinylpyrrolidone.

26. The method of claim 25, wherein the polyvinylpyrrolidone has an average molecular weight of about 45,000 daltons.

27. The method of claim 20, comprising the additional step of contacting the formed membrane with a wetting agent to render the membrane hydrophilic.

28. The method of claim 27, wherein the wetting agent comprises hydroxypropylcellulose.

29. The method of claim 27, wherein the wetting agent comprises a surfactant.

30. The method of claim 20, comprising the additional step of laminating to the formed membrane a support material.

31. The method of claim 30, wherein the support material is a nonwoven polymer fabric.

32. An asymmetric integral microporous polyvinylidene difluoride polymer membrane, formed from a solution or suspension comprising at least 12% by weight of polyvinylidene difluoride, the membrane having a microporous surface comprising minimum pores, an opposite surface comprising maximum pores, and a thickness therebetween, the thickness therebetween comprising a porous support formed from filamentous webs of polymer material, wherein the porous support comprises flow channels having diameters, and wherein the diameters of the flow channels gradually increase along a gradient from the microporous surface to the opposite surface.

33. An internally isotropic microporous polyvinylidene difluoride polymer membrane, the membrane having a microporous surface comprising minimum pores, the minimum pores having a first average diameter, an opposite surface comprising maximum pores, the maximum pores having a second average diameter, and a thickness therebetween, the thickness therebetween comprising a porous support formed from filamentous webs of polymer material, wherein the porous support comprises flow channels having diameters, and wherein the diameters of the flow channels substantially correspond to the first average diameter within a first region of the porous support, the first region of the porous support being adjacent the microporous surface, and wherein the diameters of the flow channels substantially correspond to the second average diameter within a second region of the porous support, the second region of the porous support being adjacent the opposite surface, and wherein the diameters of the flow channels between the first region of the porous support and the second region of the porous support have a substantially constant diameter.

34. The membrane of claim 33, wherein the first region of the porous support occupies less than about 10% of the thickness of the porous support.

35. The membrane of claim 33, wherein the second region of the porous support occupies less than about 10% of the thickness of the porous support.

36. In an improved filtering device having a membrane for filtering aqueous solutions, the improvement comprising:

an ozone resistant microporous polyvinylidene difluoride polymer membrane, formed from a solution or suspension comprising at least 12% by weight of polyvinylidene difluoride, the membrane having a microporous surface comprising minimum pores, an opposite surface comprising maximum pores, and a thickness therebetween, the thickness therebetween comprising a porous support formed from filamentous webs of polymer material.

37. The improved filter of claim 36, wherein the ozone resistant membrane has a flow rate of water of from about 25 to about 500 cm/min at 10 psid.