Porous fluorine resin membrane and process for preparing the same

• US 4,623,670 A
• Filed: 12/13/1985
• Issued: 11/18/1986
• Est. Priority Date: 12/27/1984
• Status: Expired due to Term

• Current Assignee: Asahi Kasei Kogyo Kabushiki Kaisha
• Original Assignee: Asahi Kasei Kogyo Kabushiki Kaisha
• Inventors: Miura, Morikazu, Mutoh, Yoshihiko
• Primary Examiner(s): Foelak, Morton
• Application Number:
  US06/808,491
• Time in Patent Office: 340 Days
• Field of Search: 521/61, 521/64, 521/145, 521/134, 210/500.2
• US Class Current: 521/61
• CPC Class Codes: B01D 67/0027 by stretching
• CPC Class Codes: B01D 67/003 by selective elimination of components, e.g. by leaching
• CPC Class Codes: B01D 71/32 containing fluorine atoms
• CPC Class Codes: C08J 2201/0442 the inorganic phase being a metal, its oxide or hydroxide
• CPC Class Codes: C08J 2323/08 Copolymers of ethene C08J2323/16 takes precedence
• CPC Class Codes: C08J 2327/12 containing fluorine atoms
• CPC Class Codes: C08J 9/26 by elimination of a solid phase from a macromolecular composition or article, e.g. leaching out

Abstract

The invention relates to a porous membrane made of a particular fluorine resin, having excellent chemical resistance, excellent thermal resistance, excellent filtration performance and excellent mechanical properties, and having uniform porous structure comprising minute pores, and also relates to a process for preparing the same. In particular, the invention relates to a porous membrane suited for a microfilter having excellent thermal resistance and excellent filtration performance, especially a porous membrane suited for a microfilter for use in purification of chemicals such as strong acid and strong alkali by utilizing the excellent chemical resistance, and also a process for preparing the same.

Claims

1. A process for preparing a porous fluorine resin membrane, which comprises mixing 10 to 60% by volume of a fluorine resin selected from the group consisting of an ethylene-tetrafluoroethylene copolymer, an ethylene-chlorotrifluoroethylene copolymer and polychlorotrifluoroethylene, 7 to 42% by volume of an inorganic fine powder material and 30 to 75% by volume of a chlorotrifluoroethylene oligomer, followed by melt-molding to form a molded product, removing by extraction the chlorotrifluoroethylene oligomer from said molded product, and further removing by extraction therefrom the inorganic fine powder material.

6. The process for preparing a porous fluorine resin membrane according to claim 1, wherein said chlorotrifluoroethylene oligomer is a 4 to 20 mer.

2. A process for preparing a porous fluorine resin membrane, which comprises mixing 10 to 60% by volume of a fluorine resin selected from the group consisting of an ethylene-tetrafluoroethylene copolymer, an ethylene-chlorotrifluoroethylene copolymer and polychlorotrifluoroethylene, 7 to 42% by volume of an inorganic fine powder material and 30 to 75% by volume of a mixture of a chlorotrifluoroethylene oligomer and an organic heat-resistant substance having the SP value of 5 to 11 other than the chlorotrifluoroethylene oligomer, followed by melt-molding to form a molded product, removing by extraction the chlorotrifluoroethylene oligomer and the organic heat resistant substance from said molded product, and further removing by extraction therefrom the inorganic fine powder material.

5. The process for preparing a porous fluorine resin membrane according to claim 2, wherein said heat-resistant organic substance is silicone oil.

8. The process for preparing a porous fluorine resin membrane according to claim 2, wherein said chlorotrifluoroethylene oligomer is a 4 to 20 mer.

11. The process for preparing a porous fluorine resin membrane according to claim 5, wherein said chlorotrifluoroethylene oligomer is a 4 to 20 mer.

3. A process for preparing a porous fluorine resin membrane, which comprises mixing 10 to 60% by volume of a fluorine resin selected from the group consisting of an ethylene-tetrafluoroethylene copolymer, an ethylene-chlorotrifluoroethylene copolymer and polychlorotrifluoroethylene, 7 to 42% by volume of an inorganic fine powder material and 30 to 75% by volume of a chlorotrifluoroethylene oligomer, followed by melt-molding to form a molded product, applying an annealing after removing by extraction the chlorotrifluoroethylene oligomer from said molded product, and further removing by extraction therefrom the inorganic fine powder material.

9. The process for preparing a porous fluorine resin membrane according to claim 3, wherein said chlorotrifluoroethylene oligomer is a 4 to 20 mer.

4. A process for preparing a porous fluorine resin membrane, which comprises mixing 10 to 60% by volume of a fluorine resin selected from the group consisting of an ethylene-tetrafluoroethylene copolymer, an ethylene-chlorotrifluoroethylene copolymer and polychlorotri-fluoroethylene, 7 to 42% by volume of an inorganic fine powder material and 30 to 75% by volume of a mixture of a chlorotrifluoroethylene oligomer and an organic heat-resistant substance having the SP value of 5 to 11 other than the chlorotrifluoroethylene oligomer, followed by melt-molding to form a molded product, applying an annealing after removing by extraction the chlorotrifluoroethylene oligomer and the organic heat resistant substance from said molded product, and further removing by extraction therefrom the inorganic fine powder material.

7. The process for preparing a porous fluorine resin membrane according to claim 4, wherein said heat-resistant organic substance is silicone oil.

10. The process for preparing a porous fluorine resin membrane according to claim 4, wherein said chlorotrifluoroethylene oligomer is a 4 to 20 mer.