PROCEDIMIENTO DE FABRICACION DE UNA MEMBRANA SEMIPERMEABLE DE FIBRAS HUECAS DE POLISULFONA.

    公开(公告)号:ES2237760T3

    公开(公告)日:2005-08-01

    申请号:ES96304796

    申请日:1996-06-28

    Abstract: LAS MEMBRANAS DE FIBRA HUECA RESPECTIVAS APROPIADAS PARA USAR EN LA ELIMINACION DE CONTAMINANTES NO DESEADOS DE LA SANGRE, EN PARTICULAR EN UN RIÑON ARTIFICIAL, TIENEN: (1) AREA POR MEMBRANA DE 1.6 M{SUP,2}, UN ESPACIO IN VITRO PARA UREA Y FOSFORO RESPECTIVAMENTE DE (MAYOR O IGUAL) 195, Y (MAYOR O IGUAL) 180, ML/MIN, UN ESPACIO {BE}{SUB,2}-MICROGLOBULINA DE (MAYOR O IGUAL) 44 ML/MIN Y PERMEABILIDAD DE ALBUMINA DE (MENOR O IGUAL) 0,5%; (2) UNA PERMEABILIDAD DE ALBUMINA DE (MENOR O IGUAL) 1,5% Y UN COEFICIENTE TOTAL DE MASA TRANSFERIBLE DE K{SUB,O} (MAYOR O IGUAL) 0,0012 CM/MIN; Y (3) UN DIALIZANTE DE VITAMINA B{SUB,12} DE (MAYOR O IGUAL) 135 ML/MIN Y UNA PERMEABILIDAD DE ALBUMINA DE (MENOR O IGUAL) 3%. LAS MEMBRANAS PUEDEN SER PREPARADAS MEDIANTE GIRO DE FIBRA HUECA DE UNA SOLUCION DE GIRO QUE CONTIENE UNA POLISULFONA, UN POLIMERO HIDROFILO , UN DISOLVENTE Y AGUA, TENIENDO LA SOLUCION DE GIRO UNA VISCOSIDAD X A 30 (GRADOS) C DE 25-130 DE EQUILIBRIO Y UNA CANTIDAD Y% DE AGUA DADO POR: -0,01X+ 1,45 (MENOR O IGUAL) -0,01X + 2,25 LAS MEMBRANAS PUEDEN SER INCORPORADAS A UN MODULO HEMODIALIZADOR POR UN METODO EN EL QUE SON PREIMPREGNADAS CON UN AGENTE HUMECTANTE, Y A PARTIR DE ENTONCES GUARDADAS SEPARADAMENTE LA UNA DE LA OTRA POR ESPACIADORES Y ENTONCES INSERTADAS EN EL MODULO.

    2.
    发明专利
    未知

    公开(公告)号:AT289219T

    公开(公告)日:2005-03-15

    申请号:AT96304796

    申请日:1996-06-28

    Abstract: Respective hollow fiber membranes suitable for use in removing undesired contaminants from blood, in particular in an artificial kidney, have: (1) per membrane area of 1.6 m , in vitro clearances for urea and phosphorus respectively of ≥ 195, and ≥ 180, ml/min, a beta 2-microglobulin clearance ≥ 44 ml/min and an albumin permeability ≤ 0.5%; (2) an albumin permeability ≤ 1.5% and an overall mass transfer coefficient Ko ≥ 0.0012 cm/min; and (3) a vitamin B12 dialyzance of ≥ 135 ml/min and an albumin permeability ≤ 3%. The membranes can be prepared by spinning hollow fibers from a spinning solution comprising a polysulfone, a hydrophilic polymer, a solvent and water, the spinning solution having a viscosity x at 30 DEG C of 25-130 poise and a quantity y % of water given by: The membranes can be incorporated into a hemodialyzer module by a method in which they are preimpregnated with a wetting agent, thereafter kept separate from one another by spacers and then inserted in the module.

    POLYSULFONE HOLLOW FIBER SEMIPERMEABLE MEMBRANE

    公开(公告)号:CA2180222A1

    公开(公告)日:1996-12-31

    申请号:CA2180222

    申请日:1996-06-28

    Abstract: Respective hollow fiber membranes suitable for use in removing undesired contaminants from blood, in particular in an artificial kidney have: (1) per membrane area of 1.6 m2, in vitro clearances for urea and phosphorus respectively of ml/min, a .beta.2-microglobulin clearance albumin permeability (2) an albumin permeability mass transfer coefficient Ko (3) a vitamin B12 dialyzance of albumin permeability The membranes can be prepared by spinning hollow fibers from a spinning solution comprising a polysulfone, a hydrophilic polymer, a solvent and water, the spinning solution having a viscosity x at 30.degree.C of 25-130 poise and a quantity y % of water given by: -0.01x + 1.45 The membranes can be incorporated into a hemodialyzer module by a method in which they are preimpregnated with a wetting agent, thereafter kept separate from one another by spacers and then inserted in the module.

    POLYSULFONE HOLLOW FIBER SEMIPERMEABLE MEMBRANE

    公开(公告)号:CA2180222C

    公开(公告)日:2006-10-10

    申请号:CA2180222

    申请日:1996-06-28

    Abstract: Respective hollow fiber membranes suitable for use in removing undesired contaminants from blood, in particular in an artificial kidney, have: (1) per membrane area of 1.6 m2, in vitro clearances for urea and phosphorus respectively of .gtoreq. 195, and .gtoreq. 180, ml/min, a .beta.2-microglobulin clearance .gtoreq. 44 ml/min and an albumin permeability .ltoreq. 0.5%; (2) an albumin permeability .ltoreq. 1.5% and an overall mass transfer coefficient Ko .gtoreq. 0.0012 cm/min; and (3) a vitamin B12 dialyzance of .gtoreq. 135 ml/min and an albumin permeability .ltoreq. 3%. The membranes can be prepared by spinning hollow fibers from a spinning solution comprising a polysulfone, a hydrophilic polymer, a solvent and water, the spinning solution having a viscosity x at 30.degree.C of 25-130 poise and a quantity y % of water given by: -0.01.times. + 1.45 .ltoreq. y .ltoreq. -0.01.times. + 2.25. The membranes can be incorporated into a hemodialyzer module by a method in which they are preimpregnated with a wetting agent, thereafter kept separate from one another by spacers and then inserted in the module.

    5.
    发明专利
    未知

    公开(公告)号:DE69634352T2

    公开(公告)日:2006-01-12

    申请号:DE69634352

    申请日:1996-06-28

    Abstract: Respective hollow fiber membranes suitable for use in removing undesired contaminants from blood, in particular in an artificial kidney, have: (1) per membrane area of 1.6 m , in vitro clearances for urea and phosphorus respectively of ≥ 195, and ≥ 180, ml/min, a beta 2-microglobulin clearance ≥ 44 ml/min and an albumin permeability ≤ 0.5%; (2) an albumin permeability ≤ 1.5% and an overall mass transfer coefficient Ko ≥ 0.0012 cm/min; and (3) a vitamin B12 dialyzance of ≥ 135 ml/min and an albumin permeability ≤ 3%. The membranes can be prepared by spinning hollow fibers from a spinning solution comprising a polysulfone, a hydrophilic polymer, a solvent and water, the spinning solution having a viscosity x at 30 DEG C of 25-130 poise and a quantity y % of water given by: The membranes can be incorporated into a hemodialyzer module by a method in which they are preimpregnated with a wetting agent, thereafter kept separate from one another by spacers and then inserted in the module.

    6.
    发明专利
    未知

    公开(公告)号:DE69634352D1

    公开(公告)日:2005-03-24

    申请号:DE69634352

    申请日:1996-06-28

    Abstract: Respective hollow fiber membranes suitable for use in removing undesired contaminants from blood, in particular in an artificial kidney, have: (1) per membrane area of 1.6 m , in vitro clearances for urea and phosphorus respectively of ≥ 195, and ≥ 180, ml/min, a beta 2-microglobulin clearance ≥ 44 ml/min and an albumin permeability ≤ 0.5%; (2) an albumin permeability ≤ 1.5% and an overall mass transfer coefficient Ko ≥ 0.0012 cm/min; and (3) a vitamin B12 dialyzance of ≥ 135 ml/min and an albumin permeability ≤ 3%. The membranes can be prepared by spinning hollow fibers from a spinning solution comprising a polysulfone, a hydrophilic polymer, a solvent and water, the spinning solution having a viscosity x at 30 DEG C of 25-130 poise and a quantity y % of water given by: The membranes can be incorporated into a hemodialyzer module by a method in which they are preimpregnated with a wetting agent, thereafter kept separate from one another by spacers and then inserted in the module.

    POLYSULFONE HOLLOW FIBER TYPE ARTIFICIAL KIDNEY AND ITS PRODUCTION

    公开(公告)号:JPH11104235A

    公开(公告)日:1999-04-20

    申请号:JP26673797

    申请日:1997-09-30

    Abstract: PROBLEM TO BE SOLVED: To provide a polysulfone type hollow fiber type artificial kidney which has high water permeability, is high in performance to remove uremic substances and is excellent in terms of safety without the admission of permeation of endotoxin even if this artificial kidney has moderate albumin permeability. SOLUTION: This process for production consists in confining the solvent remaining in the hollow fibers of the artificial kidney comprising the hollow fiber membranes consisting of a polysulfone resin contg. a hydrophilic high- molecular material to a specific value or below by washing, then executing a sterilization treatment by using gamma rays and electron beams and insolubilizing the hydrophilic high-molecular material by crosslinking. As a result, the permeability of the albumin is specified to >=0.2 to

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