Asymmetric hollow fiber membranes

• US 20040050791A1
• Filed: 07/15/2003
• Published: 03/18/2004
• Est. Priority Date: 01/23/2001
• Status: Abandoned Application

• Current Assignee: Amersham Biosciences Membrane Separations Corp.
• Original Assignee: Amersham Biosciences Membrane Separations Corp.
• Inventors: Herczeg, Attila
• Application Number:
  US10/466,578
• Publication Number:
  US 20040050791A1
• Time in Patent Office: Days
• US Class Current: 210/651
• CPC Class Codes: B01D 2325/022 Asymmetric membranes
• CPC Class Codes: B01D 61/145 Ultrafiltration
• CPC Class Codes: B01D 61/147 Microfiltration
• CPC Class Codes: B01D 63/02 Hollow fibre modules
• 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 69/082 characterised by the cross-sectional shape of the fibre
• CPC Class Codes: B01D 69/087 Details relating to the spinning process
• CPC Class Codes: B01D 71/34 Polyvinylidene fluoride
• CPC Class Codes: B01D 71/68 Polysulfones; Polyethersulfones

Abstract

A porous asymmetric hollow polymer fiber membrane having an inside surface having a coarse porous structure and an outside surface having a dense porous structure, the average pore size rating of the pores at the inside surface being greater than the average pore size rating of the pores at the outside surface, as well as filters and filter devices comprising one or more of the hollow fiber membranes, the filter and devices preferably being arranged to direct fluid flow from the inside surface of the membranes to the outside surface, and methods of using the filters and filter devices, are disclosed.

Claims

1. A membrane comprising:

a porous asymmetric hollow polymer fiber having an inside porous surface having a coarse porous structure and an outside porous surface having a dense porous structure, the average pore size rating of the pores on the inside surface being greater than the average pore size rating of the pores on the outside surface.

2. The membrane of claim 1, having a progressively asymmetric structure from the inside surface to the outside surface.

7. The membrane of claim 1, the average pore size rating of the pores on the inside surface being at least about 5 times greater than the average pore size rating of the pores on the outside surface.

8. The membrane of claim 1, the average pore size rating of the pores on the inside surface being at least about 10 times greater than the average pore size rating of the pores on the outside surface.

9. The membrane of claim 1, the average pore size rating of the pores on the inside surface being at least about 100 times greater than the average pore size rating of the pores on the outside surface.

10. The membrane of any one of claims 7-9, wherein the membrane is an ultrafiltration membrane.

11. The membrane of any one of claims 7-9, wherein the membrane is a microfiltration membrane.

3. A filter comprising two or more porous asymmetric hollow polymer fiber membranes, each membrane having an inside porous surface having a coarse porous structure and an outside porous surface having a dense porous structure, the fiber membrane having a progressively asymmetric structure from the inside surface to the outside surface.

4. A filter device comprising:

a housing having an inlet and an outlet and defining a fluid flow path between the inlet and the outlet, and a plurality of porous asymmetric hollow polymer fiber membranes disposed across the fluid flow path, each porous asymmetric hollow fiber membrane having an inside surface having a coarse structure and an outside surface having a dense structure, the average pore size rating of the pores on the inside surface being greater than the average pore size rating of the pores on the outside surface;

wherein the housing is arranged to direct fluid from the inlet, through the inside surface and the outside surface of the porous asymmetric hollow fiber membranes, and through the outlet.

5. A filter device comprising:

a housing having an inlet, a first outlet and a second outlet, the housing defining a first fluid flow path between the inlet and the first outlet, and a second fluid flow path between the inlet and the second outlet;

a plurality of porous asymmetric hollow polymer fiber membranes disposed across the first fluid flow path and substantially parallel to the second fluid flow path, each porous asymmetric hollow fiber membrane having an inside surface having a coarse structure and an outside surface having a dense structure, the average pore size rating of the pores on the inside surface being greater than the average pore size rating of the pores on the outside surface;

wherein the housing is arranged to direct a permeate from the inlet, through the inside surface and the outside surface of the porous asymmetric hollow fibers, and through the first outlet, and direct a retentate from the inlet, substantially tangentially to the inner surface, and through the second outlet.

6. The filter device of claim 5 or 6, wherein each membrane has a progressively asymmetric structure from the inside surface to the outside surface.

12. A method for processing a fluid suspension comprising:

providing at least one porous asymmetric hollow polymer fiber membrane having an inside porous surface having a coarse structure and an outside porous surface having a dense structure, the average pore size rating of the pores on the inside surface being greater than the average pore size rating of the pores on the outside surface;

contacting the inside surface of the membrane with a fluid suspension comprising undesirable cellular material and a macromolecule of interest, and passing the macromolecule of interest from the inside surface to the outside surface while retaining undesirable material between the inside and outside surfaces.

13. The method of claim 12, comprising tangential flow filtration.

14. The method of claim 12, comprising dead end filtration.

17. The method of any of claims 12-16, wherein the membrane has a progressively asymmetric structure from the inside surface to the outside surface, the average pore size rating of the pores on the inside surface being at least about 5 times greater than the average pore size rating of the pores on the outside surface.

33. A membrane prepared by the method of any of claims 17-32.

15. A method of separating a fluid into a retentate and a permeate comprising:

directing a feed suspension comprising larger macromolecules and smaller macromolecules into the central bore of a hollow fiber membrane, the membrane having an inside porous surface having a coarse structure and an outside porous surface having a dense structure, the average pore size rating of the pores at the inside surface being greater than the average pore size rating of the pores at the outside surface;

passing a permeate containing the smaller macromolecules from the inside surface to the outside surface; and

passing a retentate containing the larger macromolecules through the central bore of the membrane.

16. A method of separating a fluid into a retentate and a permeate comprising:

directing a feed suspension comprising larger species and smaller species into the central bore of a hollow fiber membrane, the membrane having an inside porous surface having a coarse structure and an outside porous surface having a dense structure, the average pore size rating of the pores at the inside surface being greater than the average pore size rating of the pores at the outside surface;

passing a permeate containing the smaller species from the inside surface to the outside surface; and

passing a retentate containing the larger species through the central bore of the membrane.

18. A method of preparing an asymmetric hollow fiber membrane comprising:

providing a spinning dope comprising a first polymer, a solvent, and a nonsolvent, in ratios sufficient to form a homogenous solution or a colloidal dispersion;

extruding the dope in the form of a hollow pre-fiber from a nozzle, the pre-fiber having an inside surface and an outside surface;

contacting the outside surface of the pre-fiber with a coagulating medium; and

coagulating the pre-fiber from the outside surface to the inside surface to provide an asymmetric hollow fiber membrane.

19. The method of claim 18, wherein the spinning dope also comprises an additional polymer.

20. The method of claim 19, wherein the additional polymer is polyvinyl pyrrolidone (PVP).

21. The method of claim 20, wherein the PVP is between about 10 and 40 percent by weight of said spinning dope.

22. The method of any of claims 18-21, wherein the first polymer is a sulfone polymer.

23. The method of claim 22, wherein the sulfone polymer is polyethersulfone.

24. The method of claim 23, wherein the sulfone polymer is polysulfone or polyarylsulfone.

25. The method of any of claims 18-21, wherein the first polymer is polyvinylidene fluoride.

26. The method of any of claims 18-25, wherein the solvent is selected from the group consisting of dimethyl formamide, N-methyl pyrrolidone (NMP), dimethyl acetamide, dimethyl sulfoxide, sulfolane, dioxane, chloroform, and tetrachloroethane.

27. The method of any of claims 18-26, wherein the nonsolvent is selected from the group consisting of ethylene glycol, glycerine;

polyethylene oxides, polypropylene oxides, alkylaryl polyether alcohols, alkylaryl sulfonates, alkyl sulfates, triethylphosphate, formamide, acetic acid, propionic acid, 2-methoxyethanol, t-amyl alcohol, methanol, ethanol, isopropanol, hexanol, heptanol, octanol, acetone, methylethylketone, methylisobutylketone, butyl ether, ethyl acetate, amyl acetate, diethyleneglycol, di(ethyleneglycol)diethylether, di(ethyleneglycol)dibutylether, and water.

28. The method of any of claims 18-27, further comprising collecting the asymmetric hollow fiber membrane on a receiving plate.

29. The method of any of claims 18-28, wherein the membrane has an asymmetry ratio of at least about 5.

30. The method of any of claims 18-29, wherein the membrane has an asymmetry ratio of at least about 10.

31. The method of any of claims 18-30, wherein the membrane is a microfiltration membrane.

32. The method of any of claims 18-30, wherein the membrane is an ultrafiltration membrane.

34. A method for cleaning a hollow fiber membrane having an outside porous surface, an inside porous surface, and a bore comprising:

passing a fluid from the outside porous surface of the hollow fiber membrane to the inside porous surface of the membrane, the inside surface of the membrane having larger average pore size rated pores than the outside surface; and

,

passing the fluid from the inside surface of the membrane along the bore of the membrane.

35. The method of claim 34, wherein the membrane has material retained in the pores, and the method includes passing the retained material into the bore of the membrane and through an end of the membrane.