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US4686044A Expired / Lapsed US ⏱️ 0.0 years remaining

Polycarbonate-polyether-copolymer membrane

Assignee: Akzo NV
•
Filing: 1985-12-09
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Granted: 1987-08-11
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Expires: 2005-12-09
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Abstract

Abstract A method is provided for producing a membrane from polycarbonate-polyether-blockcopolymers with about 5 to 35 weight percent of repeating alkyleneethercarbonate units and about 95 to 65 weight percent of repeating bisphenol A-carbonate units, wherein the polyethyleneoxide blocks have a molecular weight from about 1,000 to 20,000, wherein the intrinsic viscosity of the copolymer is from about 180 to 300 ml/g as measured in chloroform at 25 DEG C. and wherein the ultrafiltration rate is from about 4 to 200 ml/h.m2.mm Hg. In a first dissolving step a polycarbonate-polyether-copolymer is homogeneously mixed with a solvent at a temperature from about 80 DEG to 120 DEG C. and in a second dissolving step the temperature is brought to about 140 DEG to 180 DEG C. to produce a true solution. The filtered solution is cooled to from about 20 DEG to 50 DEG C. and is then extruded through a nozzle into a bath comprising a nonsolvent for the polymer for precipitating the polymer. The precipitated polymer is then washed and dried. The resulting membranes improve the processes of hemodialyzing and of homofiltration.

Inventors

  • 👤 Joachim Behnke
  • 👤 Hans-Jurgen Pitowski

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 03:30
CPC Classifications
B; B01; B01D; B01D71/00; B01D71/06; B01D71/76; B01D71/80; B01D63/00; B01D63/02; B01D69/00; B01D69/02; B01D71/52; C; C08; C08G; C08G64/00; C08G64/18; C08G64/183; B01D71/50; Y; Y10; Y10T; Y10T428/00; Y10T428/29; Y10T428/2913; Y10T428/2973; Y10T428/2975

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 107 words
An isotropic polycarbonate-polyether block copolymer membrane useful for hemodialysis, containing less than 0.5 weight percent impurities consisting essentially of (1) about 5 to 35 weight percent of repeating polyethylene-ether-carbonate units, the polyethylene oxide blocks of said copolymer having a molecular weight of from 1000 to 20,000, and (2) about 95 to 65 weight percent of repeating bisphenol A - carbonate units wherein the intrinsic viscosity of said copolymer ranges from about 180 to 300 ml/g as measured in chloroform at 25° C., and the ultrafiltration rate of said membrane amounts to about 4 to 200 ml/h.m 2 mmHg, said membrane being prepared by a wet extrusion process.
Claim 2
Dependent Claim 107 words
An isotropic polycarbonate-polyether block copolymer membrane useful for hemodialysis, containing less than 0.5 weight percent impurities consisting essentially of (1) about 5 to 35 weight percent of repeating polyethylene-ether-carbonate units, the polyethylene oxide blocks of said copolymer having a molecular weight of from 1000 to 20,000, and (2) about 95 to 65 weight percent of repeating bisphenol A - carbonate units wherein the intrinsic viscosity of said copolymer ranges from about 180 to 300 ml/g as measured in chloroform at 25° C., and the ultrafiltration rate of said membrane amounts to about 4 to 200 ml/h.m 2 mmHg, said membrane being prepared by a wet extrusion process.
Claim 3
Dependent Claim 11 words
The membrane according to claim 1 formed as a flat foil.
Claim 4
Dependent Claim 11 words
The membrane according to claim 1 formed as a tubular foil.
Claim 5
Dependent Claim 11 words
The membrane according to claim 1 formed as a hollow fiber.
Claim 6
Dependent Claim 33 words
The membrane according to claim 1 wherein numerically the dialytical permeability DL B12 for vitamine B 12 (as measured at 20° C.) depends on the ultrafiltration efficiency UFL according to the formula ##EQU6##
Claim 7
Dependent Claim 49 words
The membrane according to claim 1 wherein the polycarbonate-polyether-copolymer comprises from about 7 to 13 weight percent of repeating polyethyleneoxide-carbonate units, wherein the average molecular weight of the polyethyleneoxide-carbonate blocks is from about 6,000 to 10,000, and from about 93 to 87 weight percent of repeating bisphenol A-carbonate units.
Claim 8
Dependent Claim 193 words
An isotropic polycarbonate-polyether block copolymer membrane useful for hemodialysis, containing less than 0.5 weight percent impurities consisting essentially of (1) about 5 to 35 weight percent of repeating polyethylene-ether-carbonate units, the polyethylene oxide blocks of said copolymer having a molecular weight of from 1000 to 20,000, and (2) about 95 to 65 weight percent of repeating bisphenol A - carbonate units wherein the intrinsic viscosity of said copolymer ranges from about 180 to 300 ml/g as measured in chloroform at 25° C., and The ultrafiltration rate of said membrane amounts to about 4 to 200 ml/h.m 2 mmHg, said membrane being prepared by a wet extrusion process comprising the following steps: (a) dissolving said polycarbonate - polyether block copolymer in a solvent therefor at a temperature of from about 80°-120° C., (b) increasing the temperature of said solution to about 140°-180° C., (c) filtering said solution, (d) cooling said filtered solution to about 20°-50° C., (e) extruding said solution through a nozzle into a bath containing a non-solvent for the copolymer for precipitating the polymer, and (f) drying the extruded precipitated polymer in the presence of measures for preventing longitudinal and cross-sectional shrinkage.
Claim 9
Dependent Claim 193 words
An isotropic polycarbonate-polyether block copolymer membrane useful for hemodialysis, containing less than 0.5 weight percent impurities consisting essentially of (1) about 5 to 35 weight percent of repeating polyethylene-ether-carbonate units, the polyethylene oxide blocks of said copolymer having a molecular weight of from 1000 to 20,000, and (2) about 95 to 65 weight percent of repeating bisphenol A - carbonate units wherein the intrinsic viscosity of said copolymer ranges from about 180 to 300 ml/g as measured in chloroform at 25° C., and The ultrafiltration rate of said membrane amounts to about 4 to 200 ml/h.m 2 mmHg, said membrane being prepared by a wet extrusion process comprising the following steps: (a) dissolving said polycarbonate - polyether block copolymer in a solvent therefor at a temperature of from about 80°-120° C., (b) increasing the temperature of said solution to about 140°-180° C., (c) filtering said solution, (d) cooling said filtered solution to about 20°-50° C., (e) extruding said solution through a nozzle into a bath containing a non-solvent for the copolymer for precipitating the polymer, and (f) drying the extruded precipitated polymer in the presence of measures for preventing longitudinal and cross-sectional shrinkage.
Claim 10
Dependent Claim 13 words
The membrane according to claim 7 in the form of a flat foil.
Claim 11
Dependent Claim 12 words
The membrane according to claim 7 in the form of a tube.
Claim 12
Dependent Claim 13 words
The membrane according to claim 7 in the form of a hollow fiber.
Claim 13
Dependent Claim 32 words
The membrane according to claim 7 wherein numerically the dialytical permeability DL B12 for Vitamin B 12 (measured at 20° C.) depends on the ultrafiltration efficiency UFL according to the formula ##EQU7##
Claim 14
Dependent Claim 54 words
The membrane according to claim 7 wherein said polycarbonate-polyether copolymer consists assentially of (1) about 7 to 13 weight percent of repeating polyethylene oxide-carbonate units, wherein the average molecular weight of the polyethylene oxide-carbonate blocks is from about 6,000 to 10,000, and (2) about 93 to 87 weight percent of repeating bisphenol A-carbonate units.

References Cited (Backward Citations)

US3448185A Cited
US4032309A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-08-10 1991-02-09 1991-08-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-08-10 1995-02-09 1995-08-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-08-10 1999-02-09 1999-08-11 $7700.00 Window Closed / Lapsed

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