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US4772440A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for production of porous membrane

Assignee: Terumo Corp
•
Filing: 1986-11-12
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Granted: 1988-09-20
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Expires: 2006-11-12
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Abstract

Abstract In a method for the manufacture of a porous membrane by the steps of causing a polymer solution to flow and spread in a uniform thickness on a substrate and solidifying the formed layer of the polymer solution in a bad solvent, the improvement which comprises using a fluorinated hydrocarbon as the bad solvent and optionally carrying out the removal of a good solvent mingling into the fluorinated hydrocarbon during the course of the solidification by the technique of extraction from water, and repeating the fluorinated hydrocarbon.

Inventors

  • 👤 Masaaki Kasi
  • 👤 Noriyuki Koyama

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 10:34
CPC Classifications
B; B01; B01D; B01D69/00; B01D69/06; B01D67/00; B01D67/0002; B01D67/0009; B01D67/0016; B01D67/00165; B01D69/10; B01D69/107; B01D71/00; B01D71/06; B01D71/30; B01D71/32; B01D71/34; C; C08; C08J; C08J5/00; C08J5/18; C08J7/00; C08J7/04; B01D2323/00; B01D2323/02; B01D2323/12; B01D2325/00; B01D2325/04; B01D2325/20; B01D2325/36; C08J2327/00; C08J2327/02; C08J2327/12

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 98 words
A method for the manufacture of a porous membrane comprising the steps of dissolving a polymer in a good solvent therefor to form a polymer solution, causing said polymer solution to flow and spread in a layer of uniform thickness on a substrate, and solidifying said layer of said polymer solution in a bad solvent therefor, wherein said bad solvent is a fluorinated hydrocarbon having substantially no compatibility with water, and removing said good solvent mingled into said fluorinated hydrocarbon during the course of solidification, by the technique of extraction from water, and using said fluorinated hydrocarbon repeatedly.
Claim 2
Independent Claim 98 words
A method for the manufacture of a porous membrane comprising the steps of dissolving a polymer in a good solvent therefor to form a polymer solution, causing said polymer solution to flow and spread in a layer of uniform thickness on a substrate, and solidifying said layer of said polymer solution in a bad solvent therefor, wherein said bad solvent is a fluorinated hydrocarbon having substantially no compatibility with water, and removing said good solvent mingled into said fluorinated hydrocarbon during the course of solidification, by the technique of extraction from water, and using said fluorinated hydrocarbon repeatedly.
Claim 3
Dependent Claim 29 words
A method according to claim 1, wherein one fluorinated hydrocarbon, selected from the group consisting of trichlorotrifluoroethane, tetrachlorodifluoroethane, dibromotetrafluoroethane, trichloromonofluoromethane, and mixtures thereof is used as said bad solvent.
Claim 4
Dependent Claim 16 words
A method according to claim 1, wherein one fluorinated type resin is used as said polymer.
Claim 5
Dependent Claim 40 words
A method according to claim 1, wherein a fluorine type resin selected from the group consisting of vinylidene fluoride homopolymer, copolymers of vinylidene fluoride with other monomers, and combinations of such polymers with other polymers is used as said polymer.
Claim 6
Dependent Claim 34 words
A method according to claim 1, wherein one member selected from the group consisting of dimethyl formamide, dimethyl acetamide, dimethyl sulfoxide, methylethyl ketone, acetone, tetrahydrofuran, and mixtures thereof is used as said good solvent.
Claim 7
Dependent Claim 22 words
A method according to claim 1, wherein paper, mixed paper, polyester type film or polyolefine type film is used as said substrate.
Claim 8
Dependent Claim 26 words
A method according to claim 1, wherein the concentration of said polymer in said polymer solution is in the range of 10 to 25% by weight.
Claim 9
Dependent Claim 25 words
A method according to claim 1, wherein the thickness of the layer of said polymer solution is in the range of 100 to 1,000 μm.
Claim 10
Dependent Claim 16 words
A method according to claim 4, wherein vinylidene fluoride homopolymer is used as said fluorinated resin.
Claim 11
Dependent Claim 24 words
A method according to claim 1, wherein said layer of polymer solution on said substrate is removed from said bad solvent and then dried.
Claim 12
Dependent Claim 21 words
A method according to claim 10, wherein said layer of polymer solution removed from said solvent is dried at room temperature.
Claim 13
Dependent Claim 28 words
A method according to claim 11, wherein said good solvent and said bad solvent are separated from each other by extraction in water in a water-bubble extraction tank.

References Cited (Backward Citations)

US3928517A Cited
FR2391837A1 Cited
US4203848A Cited
FR2506792A1 Cited
US4444716A Cited
JPS5891732A Cited
EP0160551A2 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1991-09-20 1992-03-21 1992-09-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1995-09-20 1996-03-21 1996-09-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1999-09-20 2000-03-21 2000-09-20 $7700.00 Window Closed / Lapsed

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