Hollow fiber membrane for plasma separation

• US 4,708,799 A
• Filed: 09/17/1985
• Issued: 11/24/1987
• Est. Priority Date: 07/15/1980
• Status: Expired due to Term

• Current Assignee: Membrana GmbH (Asahi Kasei Corporation)
• Original Assignee: Erich Kessler, Klaus Gerlach, Werner Henne
• Inventors: Henne, Werner, Kessler, Erich, Gerlach, Klaus
• Primary Examiner(s): Kendell, Lorraine T.
• Application Number:
  US06/777,844
• Time in Patent Office: 798 Days
• Field of Search: 428/376, 428/398, 210/500.2, 210/321.1-321.5, 210/433.2, 210/927, 210/500.23, 210/500.22, 210/500.36, 264/41, 264/209.1, 264/561, 55/16, 55/158, 422/48
• US Class Current: 210/500.23
• CPC Class Codes: B01D 69/08 Hollow fibre membranes manufacture of hollow fibres D01D5/24, D01F1/08
• CPC Class Codes: D01D 5/24 with a hollow structure; Spinnerette packs therefor D01D5/38 takes precedence; producing tubes of plastic material B29D; addition of agents forming hollow filaments D01F1/08
• CPC Class Codes: Y10T 428/2935 Discontinuous or tubular or cellular core
• CPC Class Codes: Y10T 428/2975 Tubular or cellular

Abstract

A method for production of porous hollow polymer fiber membranes. A homogeneous mixture is prepared from at least two components where one component is a fusible polymer (10 to 30 percent) and a solvent component (70-90%) is inert relative to the polymer and where said components form a binary system having in the liquid state a region of complete miscibility as well as a miscibility gap. The mixture is extruded at a temperature above the phase segregation temperature of the mixture through a hollow fiber nozzle into a spinning tube containing a solvent inert to the polymer and having a temperature below the segregation temperature. Fiber and liquid are moved in the spinning tube in the same direction at about the same speed. After solidification the hollow fiber membrane is washed with a solvent.

A liquid mixture containing biological cells and macromolecules is passed through the membrane produced for filtration and a filtration factor for human blood proteins with molecular weights of from about 60,000 to 3 million results of at least about 0.7.

Claims

1. A hollow fiber membrane for plasma separation comprising a porous hollow polymer fiber defining a volume part of at least 70% by volume pores, said porous hollow polymer fiber displaying an inner fiber diameter from about 100 to 550 micron and a wall thickness from about 15 to 300 micron and being a polymer selected from the group consisting of a polyolefin, a copolymer polyolefin, a halogen containing polyolefin and polyethylene sulfide, said volume part displaying a filtration factor for separation of marcomolecules from biological cells in a liquid mixture containing both, said filtration factor for proteins of human blood, being in the molecular weight range of from about 60,000 to 3,000,000, of at least about 0.7, said porous hollow polymer fiber being produced by a method comprising preparing a homogeneous mixture from at least two components where one component is a fusible polymer present in the mixture in amounts from about 10 to 30 percent by weight and where a solvent component is a first liquid inert relative to the polymer and present in the mixture in amounts of from about 70 to 90 percent by weight and where said components form a binary system having in the liquid state a region of complete miscibility and a miscibility gap;

extruding the mixture at a temperature above the segregation temperature of the mixture through a hollow fiber nozzle into a spinning tube containing a second liquid inert to the polymer and having a temperature in the spinning tube below said segregation temperature;

moving the fiber and the second inert spinning liquid in the same direction and with about the same or only slightly different linear speed through the spinning tube; and

removing the fiber under low tension from the spinning tube.

2. The hollow fiber membrane according to claim 1 wherein the filtration factor is from about 0.9 to 1.0.

3. The hollow fiber membrane according to claim 1 wherein the filtration factor is from about 0.9 to 1 for human blood proteins in the range of molecular weights from about 1,000,000 to 2,500,000.

4. The hollow fiber membrane according to claim 1 wherein the polymer is polypropylene.

5. The hollow fiber membrane according to claim 1 wherein the volume of hollow pores in the fiber is at least about 80 percent of the fiber.

6. The hollow fiber membrane according to claim 1 wherein the fiber has an inner diameter of from about 250 to 450 micron.

7. The hollow fiber membrane according to claim 1 wherein the wall thickness of the hollow fiber is from about 100 to 200 microns.

8. The hollow fiber membrane according to claim 1 wherein the fiber is impermeable to blood cells.

9. The hollow fiber membrane according to claim 1 wherein the flow of filtrate is at least about 0.2 of the blood flow through the filter membrane, if the flow of the filtrate is determined at a pressure difference of 0.1 bar.

10. The hollow fiber membrane according to claim 1, further comprising said membrane being produced by also washing the formed hollow fiber structure after solidation with a solvent.

11. The hollow fiber membrane according to claim 1, wherein said membrane is being produced by having the first liquid inert to the polymer and the second liquid inert to the polymer having an identical chemical composition.

12. The hollow fiber membrane according to claim 1, wherein said membrane is produced by having the speed gradient between the fiber and the spinning liquid while passing the spinning tube is less than about 15 percent.

13. The hollow fiber membrane according to claim 1, wherein said membrane is produced by having the fiber and the second inert liquid being passed through the spinning tube with the same linear speed.

14. The hollow fiber membrane according to claim 1, wherein said membrane is produced by having the fiber withdrawn from the spinning tube with a speed of from about 5 to 15 percent higher than the speed resulting without pulling at the exit of the spinning tube.

15. The hollow fiber membrane according to claim 1, wherein said membrane is produced by also washing the fiber after its solidation with a pressure washing step for removing inert liquid.

16. The hollow fiber membrane according to claim 1, wherein said membrane is produced by also winding the fiber in parallel and washing the fiber in a parallel position.

17. The hollow fiber membrane according to claim 1, wherein said membrane is produced by also maintaining an air gap between the exit face of the hollow fiber nozzle and the surface of the liquid spinning tube.

18. The hollow fiber membrane according to claim 1, wherein said membrane is produced by having the width of the air gap being about 3-5 mm.

19. The hollow fiber membrane according to claim 1, wherein said membrane is produced by having the first and second inert liquid comprise secondary amines.

20. The hollow fiber membrane according to claim 1, wherein said membrane is produced by maintaining conditions so that the resulting pores in the membrane pass macromolecules having a molecular weight of at least about 2,000,000.

21. The hollow fiber membrane according to claim 1, wherein said membrane is produced so that the hollow fiber is formed for plasma separation.

22. The hollow fiber membrane according to claim 1, wherein the polymer is selected from the group consisting of polypropylene, a copolymer of propylene and ethylene, a polymer based on 3-methyl-pentene-(1) and polyethylene-chloro-trifluoroethylene.

23. A hollow fiber membrane for plasma separation comprising a porous hollow polymer fiber defining a volume part of at least 70% by volume pores, said porous hollow polymer fiber displaying an inner fiber diameter from about 100 to 550 micron and a wall thickness from about 15 to 300 micron and being a polymer selected from the group consisting of a polyolefin, a halogen containing polyolefin and polyethylene sulfide, said volume part displaying a filtration factor for separation of macromolecules from biological cells in a liquid mixture containing both, said filtration factor for proteins of human blood, in the molecular weight range of from about 60,000 to 3,000,000, of at least about 0.7.

24. The hollow fiber membrane according to claim 23, wherein the filtration factor is from about 0.9 to 1.0.

25. The hollow fiber membrane according to claim 23, wherein the filtration factor is from about 0.9 to 1 for human blood proteins in the range of molecular weights from about 1,000,000 to 2,500,000.

26. The hollow fiber membrane according to claim 23, wherein the polymer is polypropylene.

27. The hollow fiber membrane according to claim 23, wherein the volume of hollow pores in the fiber is at least about 80 percent of the fiber.

28. The hollow fiber membrane according to claim 23, wherein the fiber has an inner diameter of from about 250 to 450 micron.

29. The hollow fiber membrane according to claim 23, wherein the wall thickness of the hollow fiber is from about 100 to 200 microns.

30. The hollow fiber membrane according to claim 23, wherein the fiber is impermeable to blood cells.

31. The hollow fiber membrane according to claim 23, the flow filtrate is at least about 0.2 of the blood flow through the filter membrane, if the flow of the filtrate is determined at a pressure difference of 0.1 bar.

32. The hollow fiber membrane according to claim 23, wherein the polymer is selected from the group consisting of polypropylene, a copolymer of propylene and ethylene, a polymer based on 3-methyl-pentene-(1) and polyethylene-chloro-trifluoroethylene.