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US4520044A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of composite membranes

Assignee: EIDP Inc
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Filing: 1984-07-30
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Granted: 1985-05-28
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Expires: 2004-07-30
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Abstract

Abstract A process is disclosed for producing a composite reverse osmosis membrane. The process involves forming a porous polysulfone membrane from a solution of polysulfone followed by quenching the polysulfone membrane in an aqueous solution of m-phenylenediamine followed by reacting the m-phenylenediamine on the polysulfone membrane with either trimesoyl chloride or cyclohexane-1,3,5-tricarbonyl chloride in a water immiscible solution thereof.

Inventors

  • 👤 Sherman A. Sundet

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 07:35
CPC Classifications
B; B01; B01D; B01D69/00; B01D69/12; B01D71/00; B01D71/06; B01D71/56

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 104 words
A process for forming a thin film composite membrane comprising forming a membrane from a solution of a polysulfone in a polar, organic solvent containing from 10 to 20% by weight polysulfone, quenching the resulting membrane in an aqueous bath containing 0.1 to 10% weight/volume m-phenylenediamine, removing the resulting porous polysulfone film containing m-phenylenediamine from the aqueous bath, and immersing said porous polysulfone film in a water immiscible solution comprising 0.05 to 5% weight/volume trimesoyl chloride, cyclohexane-1,3,5-tricarbonyl chloride, or mixtures thereof whereby the m-phenylene diamine reacts with the trimesoyl chloride or cyclohexane-1,3,5-tricarbonyl chloride to form a continuous layer supported by the porous polysulfone membrane.
Claim 2
Dependent Claim 104 words
A process for forming a thin film composite membrane comprising forming a membrane from a solution of a polysulfone in a polar, organic solvent containing from 10 to 20% by weight polysulfone, quenching the resulting membrane in an aqueous bath containing 0.1 to 10% weight/volume m-phenylenediamine, removing the resulting porous polysulfone film containing m-phenylenediamine from the aqueous bath, and immersing said porous polysulfone film in a water immiscible solution comprising 0.05 to 5% weight/volume trimesoyl chloride, cyclohexane-1,3,5-tricarbonyl chloride, or mixtures thereof whereby the m-phenylene diamine reacts with the trimesoyl chloride or cyclohexane-1,3,5-tricarbonyl chloride to form a continuous layer supported by the porous polysulfone membrane.
Claim 3
Dependent Claim 22 words
The process of claim 1 wherein concentration of m-phenylene diamine in this aqueous quench bath is from 0.5 to 5% by weight/volume.
Claim 4
Dependent Claim 16 words
The process of claim 2 wherein the polar organic solvent for the polysulfone is dimethyl formamide.
Claim 5
Dependent Claim 18 words
The process of claim 3 wherein the solvent for the trimesoyl chloride or cyclohexane-1,3,5-tricarbonyl chloride is a chlorofluorocarbon.

References Cited (Backward Citations)

US4039440A Cited
US3926798A Cited
US4277344A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-05-27 1988-11-26 1989-05-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-05-27 1992-11-26 1993-05-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-05-27 1996-11-26 1997-05-28 $7700.00 Window Closed / Lapsed

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