Polyvinylidene fluoride porous membrane and a method for producing the same

• US 5,022,990 A
• Filed: 01/10/1990
• Issued: 06/11/1991
• Est. Priority Date: 01/12/1989
• Status: Expired due to Term

• Current Assignee: Asahi Kasei Kogyo Kabushiki Kaisha (Asahi Kasei Corporation)
• Original Assignee: Asahi Kasei Kogyo Kabushiki Kaisha (Asahi Kasei Corporation)
• Inventors: Doi, Yoshinao, Matsumura, Haruo
• Primary Examiner(s): Spitzer, Robert
• Application Number:
  US07/463,058
• Time in Patent Office: 517 Days
• Field of Search: 55/158, 210/500.23, 210/500.35, 210/500.41, 210/500.42, 264/41
• US Class Current: 210/500.42
• CPC Class Codes: B01D 2323/02 Hydrophilization
• CPC Class Codes: B01D 2325/24 Mechanical properties, e.g. strength
• CPC Class Codes: B01D 67/003 by selective elimination of components, e.g. by leaching
• CPC Class Codes: B01D 71/34 Polyvinylidene fluoride
• CPC Class Codes: C08J 2201/0543 the non-solvent being organic
• CPC Class Codes: C08J 2201/0546 the non-solvent being organic
• CPC Class Codes: C08J 2327/16 Homopolymers or copolymers of vinylidene fluoride
• CPC Class Codes: C08J 9/26 by elimination of a solid phase from a macromolecular composition or article, e.g. leaching out

Abstract

A porous membrane comprising a polyvinylidene fluoride resin and having a uniform, three-dimensional, network pore structure. The membrane has excellent chemical resistance, excellent filtering characteristics and excellent mechanical properties. The porous membrane can be produced by blending a polyvinylidene fluoride resin, an organic liquid and a powdery hydrophobic silica, subjecting the resultant blend to melt-molding to form a membrane, and extracting the organic liquid and the hydrophobic silica from the melt-molded membrane.

Claims

1. A porous membrane comprising a polyvinylidene fluoride, resin and having pores running throughout an interior of said porous membrane and opening at both surfaces of said porous membrane,

said interior of said porous membrane containing substantially no macrovoids having a diameter of 10 μ

m or more,

the average diameter of said pores in each surface of said porous membrane being within the range of from 0.05 μ

m to less than 5 μ

m,

the ratio of the average pore diameter of said pores at each surface of said porous membrane to the average pore diameter of said pores in the interior of said porous membrane in terms of the average pore diameter of pores in a cross-section of said porous membrane taken along a line perpendicular to each surface of said porous membrane, being from 0.5 to 2.0,

the ratio of the maximum pore diameter of said pores as measured by the bubble point method to a true average pore diameter of said pores as measured by the half-dry method being from 1.2 to 2.5,

and said membrane having a uniform, three-dimensional, network pore structure, and a tensile strength at break of from 70 to 200 kg/cm², a tensile elongation at break of from 100 to 500% and a porosity of from 40 to 90%.

2. The porous membrane according to claim 1, wherein said polyvinylidene fluoride resin is a vinylidene fluoride homopolymer or a copolymer of vinylidene fluoride and at least one comonomer selected from the group consisting of ethylene tetrafluoride, propylene hexafluoride, trifluorochloroethylene and ethylene.

3. The porous membrane according to claim 1, wherein said interior contains substantially no macrovoids having a diameter of 5 μ

m or more.

4. A method for producing a porous membrane of claim 1, comprising:

(a) blending a polyvinylidene fluoride resin with an organic liquid and a powdery hydrophobic silica;

(b) subjecting the resultant blend to melt-molding to form a membrane; and

(c) extracting said organic liquid and said powdery hydrophobic silica from said membrane.

5. The method according to claim 4, wherein in step (c), said organic liquid is first extracted and, subsequently, said powdery hydrophobic silica is extracted.

6. The method according to claim 4, wherein in step (c), said organic liquid and said powdery hydrophobic silica are simultaneously extracted from said membrane.

7. The method according to any one of claims 4 to 6, wherein said powdery hydrophobic silica has an average primary particle diameter of from 0.005 to 0.5 μ

m, a specific surface area of from 30 to 500 m² /g and a methanol wettability of at least 30% by volume in terms of the methanol concentration of an aqueous methanol solution capable of completely wetting said powdery hydrophobic silica.

8. The method according to any one of claims 4 to 6, wherein said powdery hydrophobic silica has an average primary particle diameter of from 0.005 to 0.5 μ

m, a specific surface area of from 50 to 300 m² /g and a methanol wettability of at least 30% by volume in terms of the methanol concentration of an aqueous methanol solution capable of completely wetting said powdery hydrophobic silica.

9. The method according to any one of claims 4 to 6, wherein said organic liquid has a solubility parameter of from 8.4 to 10.5.

10. The method according to any one of claims 4 to 6, wherein said organic liquid is a mixture of at least two different types of organic liquids each having a solubility parameter of from 8.4 to 10.5.

11. The method according to claim 10, wherein said mixture contains at least 50% by weight of dioctyl phthalate, based on the total weight of said mixture.

12. The method according to any one of claims 4 to 6, wherein said polyvinylidene fluoride resin is a vinylidene fluoride homopolymer or a copolymer of vinylidene fluoride and at least one comonomer selected from the group consisting of ethylene tetrafluoride, propylene hexafluoride, trifluorochloroethylene and ethylene.