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US4439322A Expired / Lapsed US ⏱️ 0.0 years remaining

Polymethyl methacrylate membrane

Assignee: Toray Industries Inc
•
Filing: 1981-06-29
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Granted: 1984-03-27
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Expires: 2001-06-29
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Abstract

Abstract A membrane for microfiltration, ultrafiltration or dialysis comprises a methyl methacrylate copolymer containing about 0.5 to 10 mol % of a monomer having sulfonate groups, and a methyl methacrylate copolymer containing about 0.5 to 10 mol % of a monomer having quaternary nitrogen-containing groups. It is manufactured by mixing those copolymers, dissolving the mixture in a solvent such as dimethylsulfoxide or dimethylformamide, and forming a membrane from a solution of the copolymers by casting or spinning. The membrane is particularly suitable for use in the purification of blood, and its most preferable form is hollow fibers. A method of preparing hollow fibers comprises extruding the copolymer solution through a spinneret having an annular orifice defined by a thin central tube while a liquid or gas is being injected into the central tube, and coagulating the extrusion product.

Inventors

  • 👤 Takeshi Sonoda
  • 👤 Yoshitaka Tanaka
  • 👤 Shigenori Takenaka
  • 👤 Tatsuo Nogi

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 21:15
CPC Classifications
B; B01; B01D; B01D69/00; B01D69/08; B01D71/00; B01D71/06; B01D71/40; B01D71/401; B01D71/4011; B01D71/76; B01D71/80

Claims Analysis

Total Claims: 20
Claim 1
Independent Claim 41 words
A ionically crosslinked polymethyl methacrylate separation membrane which is impermeable to red and white blood cells and platelets having an albumin permeability of at least about 30%, and having a water permeation rate of about 0.1 to 60 liters/hr.m 2 .mmHg.
Claim 2
Dependent Claim 41 words
A ionically crosslinked polymethyl methacrylate separation membrane which is impermeable to red and white blood cells and platelets having an albumin permeability of at least about 30%, and having a water permeation rate of about 0.1 to 60 liters/hr.m 2 .mmHg.
Claim 3
Dependent Claim 73 words
The membrane defined in claim 1, wherein said membrane comprises a mixture of a methyl methacrylate copolymer (A) containing about 0.5 to 10 mol % of a monomer having sulfonate groups, and a methyl methacrylate copolymer (B) containing about 0.5 to 10 mol % of a monomer having quaternary nitrogen-containing groups, the numbers of the sulfonate and the quaternary nitrogen containing groups in the copolymers having a ratio of about 5:1 to 1:5.
Claim 4
Dependent Claim 43 words
The membrane defined in claim 2, wherein said monomer having sulfonate groups is selected from the group consisting of p-styrenesulfonic acid, allylsulfonic acid, methacrylsulfonic acid, 3-methacryloxypropanesulfonic acid, vinylsulfonic acid, 3-acryloxypropanesulfonic acid, and 2-acryl-amino-2-methylpropanesulfonic acid and the sodium, potassium, ammonium and pyridine salts thereof.
Claim 5
Dependent Claim 15 words
The membrane defined in claim 2, wherein said monomer having sulfonate groups is sodium p-styrenesulfonate.
Claim 6
Dependent Claim 49 words
The membrane defined in claim 2, wherein said monomer having a quaternary nitrogen-containing group is selected from the group consisting of 2-methacryloyloxy ethyltrimethylammonium chloride, 2-methacryloyloxyethyl triethylammonium chloride, dimethyl (2-methacryloyloxyethyl)phenylammonium chloride, 2-acryloxyethylammonium chloride, 2-hydroxy-3-methacryloyloxypropyltrimethylammonium chloride, vinylbenzyltrimethylammonium chloride, and methy(2-methyl-5-vinyl)pyridinium chloride, and bromides, iodides, sulfates and sulfonates instead of said chlorides.
Claim 7
Dependent Claim 14 words
The membrane defined in claim 2, further including in the copolymer a vinyl monomer.
Claim 8
Dependent Claim 22 words
The membrane defined in claim 2, wherein said ratio is about 2:1 to 1:1 so that the membrane is anionic or neutral.
Claim 9
Dependent Claim 26 words
The membrane defined in claim 2, wherein said copolymers (A) and (B) have a weight-average molecular weight of at least about 100,000 when they are mixed.
Claim 10
Dependent Claim 15 words
The membrane defined in claim 8, wherein said molecular weight is about 200,000 to 800,000.
Claim 11
Dependent Claim 13 words
The membrane defined in claim 1 in the form of a hollow fiber.
Claim 12
Dependent Claim 96 words
A method of manufacturing the separation membrane of claim 1, which comprises: mixing a methyl methacrylate copolymer (A) containing about 0.5 to 10 mol % of a monomer having sulfonate groups, and a methyl methacrylate copolymer (B) containing about 0.5 to 10 mol % of a monomer having quaternary nitrogen-containing groups in a ratio of weight of about 1:9 to 9:1; dissolving the mixture of said copolymers (A) and (B) in at least one solvent to prepare a solution containing about 4 to 40% by weight of said copolymers; and forming a membrane from said solution.
Claim 13
Dependent Claim 21 words
The method defined in claim 11, wherein said solvent is selected from the group consisting of dimethylsulfoxide, dimethylformamide, dimethylacetamide and N-methyl-2-pyrrolidone.
Claim 14
Dependent Claim 36 words
The method defined in claim 11, further comprising adding to said solvent at least one substance selected from the group consisting of water, formamide, alcohols, urea, calcium chloride, polyoxyethyleneetherlauryl alcohol, isooctyl phenoxypolyethoxy ethanol and polyethylene glycol.
Claim 15
Dependent Claim 47 words
The method defined in claim 11, wherein said membrane is a hollow fiber membrane, and wherein said forming operation comprises: maintaining said solution at a temperature of at least about 50° C.; extruding said solution through a hollow fiber spinneret; and coagulating the product of said extrusion.
Claim 16
Dependent Claim 61 words
The method defined in claim 14, wherein said spinneret is substantially centrally provided with a thin tube defining an annular orifice therearound, said method further including injecting into said thin tube a substance selected from the group consisting of said solvent, a mixture of said solvent with water, a mixture of said solvent with a polyhydric alcohol, air and inert gas.
Claim 17
Dependent Claim 47 words
The method defined in claim 14, further including the step of causing said extrusion product to travel a distance of about 0.1 to 200 cm through an atmosphere selected from the group consisting of air and an inert gas before it is introduced into the coagulating bath.
Claim 18
Dependent Claim 44 words
The method defined in claim 14, wherein said coagulating step is performed with a coagulating agent selected from the group consisting of water and a mixture of said solvent and water, said coagulating agent having a temperature of about 0° C. to 98° C.
Claim 19
Dependent Claim 134 words
The method of manufacturing the separation membrane of claim 1, which comprises: mixing a methyl methacrylate copolymer (A) containing about 0.5 to 10 mol % of a monomer having sulfonate groups, and a methyl methacrylate copolymer (B) containing about 0.5 to 10 mol % of a monomer having quaternary nitrogen-containing groups so that the number of said sulfonate groups in the mixture of said copolymers has a ratio of about 5:1 to 1:5 to that of said quaternary nitrogen-containing groups; dissolving said mixture in a solvent selected from the group consisting of dimethylsulfoxide, dimethylacetamide, N-methyl-2-pyrrolidone and dimethylformamide, and containing a compound selected from the group consisting of glycerin, water, calcium chloride and formamide to prepare a solution containing about 4 to 40% by weight of said copolymers; and forming a membrane from said solution.
Claim 20
Dependent Claim 47 words
The method defined in claim 18, wherein said membrane is composed of hollow fibers, and wherein said forming operation comprises: maintaining said solution at a temperature of at least about 50° C.; extruding said solution through a hollow fiber spinneret; and coagulating the product of said extrusion.

References Cited (Backward Citations)

US3276598A Cited
US3546142A Cited
US3615024A Cited
US4127625A Cited
US4035459A Cited
US4262041A Cited
JPS54146278A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-03-27 1987-09-26 1988-03-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-03-27 1991-09-26 1992-03-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-03-27 1995-09-26 1996-03-27 $7700.00 Window Closed / Lapsed

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