US4623670A
Expired / Lapsed
US
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Porous fluorine resin membrane and process for preparing the same
Assignee: Asahi Kasei Corp
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Filing: 1985-12-13
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Granted: 1986-11-18
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Expires: 2005-12-13
Abstract
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.
Inventors
- 👤 Yoshihiko Mutoh
- 👤 Morikazu Miura
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 11:19
CPC Classifications
C; C08; C08J; C08J9/00; C08J9/26; B; B01; B01D; B01D67/00; B01D67/0002; B01D67/0023; B01D67/0025; B01D67/0027; B01D67/003; B01D71/00; B01D71/06; B01D71/30; B01D71/32; C08J2201/00; C08J2201/04; C08J2201/044; C08J2201/0442; C08J2323/00; C08J2323/02; C08J2323/04; C08J2323/08; C08J2327/00; C08J2327/02; C08J2327/12
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
85 words
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.
Claim 2
Dependent Claim
85 words
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.
Claim 3
Dependent Claim
112 words
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.
Claim 4
Dependent Claim
112 words
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.
Claim 5
Dependent Claim
89 words
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.
Claim 6
Dependent Claim
89 words
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.
Claim 7
Dependent Claim
116 words
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.
Claim 8
Dependent Claim
116 words
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.
Claim 9
Dependent Claim
21 words
The process for preparing a porous fluorine resin membrane according to claim 2, wherein said heat-resistant organic substance is silicone oil.
Claim 10
Dependent Claim
23 words
The process for preparing a porous fluorine resin membrane according to claim 1, wherein said chlorotrifluoroethylene oligomer is a 4 to 20 mer.
Claim 11
Dependent Claim
21 words
The process for preparing a porous fluorine resin membrane according to claim 4, wherein said heat-resistant organic substance is silicone oil.
Claim 12
Dependent Claim
23 words
The process for preparing a porous fluorine resin membrane according to claim 2, wherein said chlorotrifluoroethylene oligomer is a 4 to 20 mer.
Claim 13
Dependent Claim
23 words
The process for preparing a porous fluorine resin membrane according to claim 3, wherein said chlorotrifluoroethylene oligomer is a 4 to 20 mer.
Claim 14
Dependent Claim
23 words
The process for preparing a porous fluorine resin membrane according to claim 4, wherein said chlorotrifluoroethylene oligomer is a 4 to 20 mer.
Claim 15
Dependent Claim
23 words
The process for preparing a porous fluorine resin membrane according to claim 5, wherein said chlorotrifluoroethylene oligomer is a 4 to 20 mer.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1989-11-17 | 1990-05-19 | 1990-11-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-11-17 | 1994-05-19 | 1994-11-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-11-17 | 1998-05-19 | 1998-11-18 | $7700.00 | Window Closed / Lapsed |