Charge modified polyamide membrane

• US 4,702,840 A
• Filed: 04/07/1986
• Issued: 10/27/1987
• Est. Priority Date: 02/05/1982
• Status: Expired due to Term

• Current Assignee: Pall Corporation (Danaher Corporation)
• Original Assignee: Pall Corporation (Danaher Corporation)
• Inventors: Degen, Peter J., Gsell, Thomas C., Joffee, Irving B.
• Primary Examiner(s): SPEAR JR, FRANK
• Application Number:
  US06/848,911
• Time in Patent Office: 568 Days
• Field of Search: 210/500.38, 210/638, 210/490, 264/41, 521/27, 427/244, 427/245, 55/16
• US Class Current: 210/638
• CPC Class Codes: B01D 2323/12 Specific ratios of components used
• CPC Class Codes: B01D 2325/26 Electrical properties
• CPC Class Codes: B01D 2325/36 Hydrophilic membranes
• CPC Class Codes: B01D 67/00111 Polymer pretreatment in the casting solutions
• CPC Class Codes: B01D 71/56 Polyamides, e.g. polyester-amides

Abstract

Surface modified, skinless, hydrophilic, microporous, polyamide membranes are formed by preparing a casting solution comprised of (A) a casting resin system comprised of (a) an alcohol-insoluble polyamide resin, and (b) a cationic, water-soluble, quaternary ammonium, thermosetting, membrane surface modifying polymer, and (B) a solvent system in which the casting resin system is soluble; inducing nucleation of the casting solution by controlled addition of a nonsolvent for the casting resin system under controlled conditions to obtain a visible precipitate of casting resin system particles, thereby forming a casting composition; spreading the casting composition on a substrate to form a thin film; contacting and diluting the film of the casting composition with a liquid nonsolvent system for the casting resin system, thereby precipitating the casting resin system from the casting composition in the form of a thin, skinless, hydrophilic, surface modified, microporous, polyamide membrane; and washing and drying the membrane. The membranes of this invention are characterized by having fine pore ratings, the surface properties thereof being substantially controlled by cationic, quaternary ammonium groups of a modifying polymer thereby providing a positive zeta potential in alkaline media, and for those with moderate or low levels of surface modifying polymer present, a time to reach an effluent resistivity of 14 megaohms/cm under the Resistivity Test of 10 minutes or less. They have greatly enhanced filtration efficiency over a broad pH range with a variety of contaminants, including very fine negatively charged particles, bacteria and endotoxins.

Claims

1. A process for preparing a surface modified, skinless, hydrophilic, microporous, alcohol-insoluble polyamide membrane that is readily wetted by water which comprises:

(1) preparing a casting solution comprised of (A) a casting resin system comprised of (a) an alcohol-insoluble polyamide resin having a ratio CH₂ ;

NHCO of methylene CH₂ to amide NHCO groups within the range of from about 5;

1 to about 7;

1, and (b) a cationic, water-soluble, quaternary ammonium, thermosetting, membrane surface modifying polymer and (B) a solvent system in which said casting resin system is soluble;

(2) inducing nucleation of said casting solution by controlled addition of a nonsolvent for said casting resin system under controlled conditions of concentration, temperature, addition rate and degree of agitation to obtain a visible precipitate of casting resin system particles, thereby forming a casting composition;

(3) spreading said casting composition on a substrate to form a thin film thereof on the substrate;

(4) contacting and diluting the film of said casting composition with a liquid nonsolvent system for said casting resin system comprised of a mixture of solvent and nonsolvent liquids, thereby precipitating said casting resin system from said casting composition in the form of a thin, skinless, hydrophilic, surface modified, microporous, polyamide membrane;

(5) washing said membrane to remove solvent; and

(6) drying said membrane.

2. The process of claim 1 in which precipitated casting resin system particles are redissolved before spreading said casting composition on said substrate.

3. The process of claim 1 in which precipitated casting resin system particles are filtered out before spreading said casting composition on said substrate.

4. The process of claim 1 in which said polyamide resin is polyhexamethylene adipamide.

5. The process of claim 4 in which said membrane surface modifying polymer is a polyamine epichlorohydrin, said solvent system comprises formic acid and water, said nonsolvent added to induce nucleation is water, and the polyamide resin concentration in said casting solution is from about 10 to about 18%, the concentration of said polyamine epichlorohydrin polymer in said casting solution is from about 0.1 to about 0.9%, the concentration of formic acid in said casting solution is from about 65 to about 75%, and the concentration of water in said solution is from about 10 to about 20%.

6. The process of claim 1 in which said polyamide resin is poly-e-caprolactam.

7. The process of claim 1 in which said polyamide resin is polyhexamethylene sebacamide.

8. The process of claim 1 in which said polyamide resin is polyhexamethylene adipamide, said solvent system for said casting resin system comprises formic acid, and said nonsolvent added to induce nucleation is water.

9. The process of claim 8 wherein said solvent system for said casting resin system comprises formic acid and water.

10. The process of claim 1 in which the film of casting composition is contacted with said liquid nonsolvent system by immersing said film carried on said substrate in a bath of said liquid nonsolvent system.

11. The process of claim 1 wherein said polyamide resin is present in said casting solution in an amount of from about 10 to 18%, said membrane surface modifying polymer is present in an amount of from about 0.1 to 0.9%, said solvent system comprises formic acid and water and wherein said formic acid is present in said casting solution in an amount of from about 60 to 80%, and said water is present in said casting solution in an amount of from 0 to about 30%.

12. The process of claim 1 in which said membrane surface modifying polymer is a polyamine epichlorohydrin polymer.

13. The process of claim 1 in which said membrane surface modifying polymer is a polyamido/polyamino-epichlorohydrin polymer.

14. The process of claim 1 in which said casting composition is continuously spread onto said substrate, said thin film of said casting composition is continuously immersed in a bath of said liquid nonsolvent system, and the bath is maintained at a substantially constant composition with respect to nonsolvent and solvent by the addition of nonsolvent to the bath in a quantity sufficient to compensate for solvent diffusion into the bath from said thin film of said casting composition.

15. The process of claim 14 in which the substrate is a porous web having an open structure which is wetted and impregnated by the casting composition, thereby forming a membrane film having the porous web incorporated as a part thereof.

16. The process of claim 15 in which the substrate is a porous, fibrous polyester sheet.

17. The process of claim 1 in which said membrane is stripped from said substrate after washing and before drying.

18. The surface modified, skinless, hydrophilic, microporous, alcohol-insoluble, polyamide membrane product of the process of claim 1.

19. A process for preparing a surface modified, skinless, hydrophilic, microporous, alcohol-insoluble polyhexamethylene adipamide resin membrane that is readily wetted by water and which has pores that are substantially uniform from surface to surface which comprises:

(1) preparing a casting solution comprised of (A) a casting resin system comprised of (a) an alcohol-insoluble polyhexamethylene adipamide resin in a concentration within the range from about 10% to about 18% by weight and (b) a cationic, water-soluble, quaternary ammonium, thermosetting, membrane surface modifying polyamine-epichlorohydrin resin or polymer in a concentration within the range of from about 0.1% to about 0.9% and (B) a solvent system comprised of (a) formic acid in a concentration of from about 65% to about 75% and (b) from 10 to about 20% water (all percentages based on the weight of all the components in said solution);

(2) inducing nucleation of said casting solution by adding water thereto while controlling temperature, rate of addition of water and degree of agitation to obtain a visible precipitate of casting resin system particles, thereby forming a casting composition;

(3) spreading said casting composition on a polyester substrate to form a thin film of said casting composition thereon;

(4) contacting and diluting said thin film of said casting composition with an aqueous solution containing from about 37% to about 55% formic acid, thereby precipitating said casting resin system from said casting composition as a thin, surface modified, skinless, hydrophilic, microporous, polyamide membrane;

(5) washing said membrane to remove formic acid; and

(6) drying said membrane.

20. The process of claim 19 in which said membrane is stripped from said substrate after washing and before drying.

21. The process of claim 19 in which at least a portion of said visible precipitate of casting resin system particles is redissolved before spreading said casting composition on said substrate.

22. The process of claim 19 in which said visible precipitate of casting resin system particles is filtered out before spreading said casting composition on said substrate.

23. A charge modified, skinless, hydrophilic, microporous, alcohol-insoluble polyamide membrane derived from an alcohol-insoluble hydrophobic polyamide resin having a ratio CH₂ NHCO of methylene CH₂ to amide NHCO groups within the range of from about 5:

1 to about 7;

1, said membrane having an integral microstructure whose characteristics are substantially controlled by cationic, quaternary ammonium groups of a cationic, quaternary ammonium, thermoset, charge modifying polymer homogeneously distributed in said membrane, thereby providing a positive zeta potential in alkaline media.

24. The microporous, alcohol-insoluble polyamide membrane of claim 23 having through pores extending from surface to surface that are substantially uniform in shape and size.

25. The microporous, alcohol-insoluble polyamdie membrane of claim 23 having through pores extending from surface to surface that are tapered, wider at one surface of the sheet and narrowing as they proceed toward the opposite surface of the membrane.

26. The microporous, alcohol-insoluble polyamide membrane of claim 23 having pore ratings of 0.04 micrometers to 10 micrometers.

27. The microporous, alcohol-insoluble polyamide membrane of claim 23 having pore ratings of 0.1 micrometer to 5 micrometers.

28. The microporous, alcohol-insoluble polyamide membrane of claim 23 in which said polyamide resin is polyhexamethylene adipamide.

29. The microporous, alcohol-insoluble polyamide membrane of claim 28 wherein said time to reach an effluent resistivity of 14 megaohms/cm is 10 minutes or less.

30. The microporous, alcohol-insoluble polyamdie membrane of claim 28 wherein said time to reach an effluent resistivity of 14 megaohms/cm is 5 minutes or less.

31. A method for the filtration of particulates from a fluid medium comprising passing said medium through the microporous, alcohol-insoluble polyamide membrane of claim 28.

32. The microporous, alcohol-insoluble polyamide membrane of claim 23 comprising two of said membranes secured to each other and forming a multiple layer membrane filter.

33. The microporous, alcohol-insoluble polyamide membrane of claim 32 comprising a supported membrane and an unsupported membrane.

34. The multiple layer membrane of claim 33 having pore ratings of from 0.04 to 10 micrometers.

35. The multiple layer membrane of claim 33 having pore ratings of 0.1 t 5 micrometers.

36. The multiple layer membrane of claim 33 wherein said polyamide resin comprises polyhexamethylene adipamide.

37. The multiple layer membrane of claim 33 wherein each layer has a thickness of from about 0.1 to about 1.5 millimeters.

38. The multiple layer membrane of claim 33 wherein each layer has a thickness of from about 0.025 to about 0.8 millimeter.

39. The multiple layer membrane of claim 33 formed by drying the wet unsupported layer in contact with the wet supported layer.

40. A filter element comprised of the charge-modified, skinless, hydrophilic, microporous, alcohol-insoluble polyamide membrane of claim 33.

41. The filter element of claim 40 in which said membrane is in the form of a corrugated sheet.

42. A method for the filtration of particulates from a fluid medium comprising passing said medium through the membrane of claim 33.

43. The method of claim 42 wherein said medium comprises water.

44. The microporous, alcohol-insoluble polyamide membrane of claim 23 having a thickness within the range of from about 0.01 to about 1.5 mm.

45. A filter element comprised of the surface modified, skinless, hydrophilic, microporous, alcohol-insoluble polyamide membrane of claim 23.

46. The filter element of claim 45 in which said membrane is in the form of a corrugated sheet.

47. A method for the filtration of particulates from a fluid medium comprising passing said medium through the microporous, alcohol-insoluble polyamide membrane of claim 65.

48. The method of claim 47 wherein said medium comprises water.

49. A charge modified, skinless, hydrophilic, microporous, alcohol-insoluble polyamide membrane derived from about 80 to about 99.9 percent of an alcohol-insoluble, hydrophobic polyamide resin having a ratio CH₂ :

NHCO of methylene CH₂ to amide NHCO groups within the range of from about 5;

1 to about 7;

1 and from about 20 to about 0.1 percent of a cationic, quaternary ammonium, thermoset, charge modifying polymer homogeneously distributed in said membrane, said membrane having an integral microstructure whose characteristics are substantially controlled by cationic, quaternary ammonium groups of said modifying polymer, thereby providing a positive zeta potential in alkaline media.

50. The membrane of claim 49 wherein said polyamide is polyhexamethylene adipamide and said modifying polymer is polyamine-epichlorohydrin present in said membrane in an amount of from about 1 to about 5 percent.

51. The membrane of claim 50 wherein said modifying polymer is present in said membrane in an amount of from about 1 to about 2 percent.

52. The charge-modified, skinless, hydrophilic, microporous, alcohol-insoluble polyamide membrane of claim 49 comprising two of said membranes secured to each other and forming a multiple layer membrane filter sheet.

53. The multiple layer membrane of claim 52 comprising a supported membrane and an unsupported membrane.

54. The multiple layer membrane ot claim 53 having pore ratings from 0.04 to 10 micrometers.

55. A filter element comprised of the charge-modified, skinless, hydrophilic, microporous, alcohol-insoluble, polyamide multilayer membrane of claim 54.

56. The filter element of claim 55 in which said multilayer membrane is in the form of a corrugated sheet.

57. The multiple layer membrane of claim 53 having pore ratings of from 0.1 to 5 micrometers.

58. The multiple layer membrane of claim 53 in which said polyamide resin comprises polyhexamethylene adipamide.

59. The multiple layer membrane of claim 53 wherein each layer has a thickness of from about 0.01 to about 1.5 millimeters.

60. The multiple layer membrane of claim 53 wherein each layer has a thickness of from about 0.025 to about 0.8 millimeter.

61. The multiple layer membrane of claim 53 formed by drying the wet unsupported layer in contact with the wet supported layer.

62. A method for the filtration of particulates from a fluid medium comprising passing said medium through the multilayer membrane of claim 52.

63. The method of claim 62 wherein said medium comprises water.

64. A charge modified, skinless, hydrophilic, microporous, alcohol-insoluble polyhexamethylene adipamide membrane derived from about 80 to about 99.9 percent of an alcohol-insoluble, hydrophobic polyhexamethylene adipamide resin and from about 20 to about 0.1 percent of a cationic, quaternary ammonium, thermoset, charge modifying polymer homogeneously distributed in said membrane, said membrane having an integral microstructure whose characteristics are substantially controlled by quaternary ammonium groups of said modifying polymer, thereby providing a positive zeta potential in alkaline media.