Hollow fibre membrane with improved separating efficiency, and production of hollow fibre membrane with improved separating efficiency
A technology of fiber membranes and fiber membrane bundles, applied in the field of hollow fiber membranes for sterilization, hollow fiber membrane filters, and the manufacture of hollow fiber membranes with polysulfone and polyvinylpyrrolidone membrane materials
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Embodiment 1
[0139] Embodiment 1: the method for purifying hollow fiber membrane filter
[0140] image 3 Schematically depicts the steps comprising rinsing and sterilization for use in the production of hollow fiber membranes according to the invention, respectively hollow fiber membrane filters according to the first, second and third aspects of the invention The first step in the decontamination procedure. image 3 A fluid port 118 of a first chamber 119 of a hollow fiber membrane filter 113 surrounding the interior of the hollow fiber membranes is shown, which is fluidly connected to the connection 101 by a line 109 with a valve 105 . Another fluid port 117 is fluidly connected to connection 102 via line 110 , valve 106 and forms the inlet to a second chamber 120 of hollow fiber membrane filter 113 enclosing the space between the hollow fiber membranes. Another fluid port 114 is in fluid connection with valve 107 and connection 103 via line 111 and forms the inlet to the second chamb...
Embodiment 2
[0149] Example 2: Example implementation of the hollow fiber membrane of the present invention
[0150] A spinning solution consisting of 16 parts by weight of polysulfone (P3500 from Solvay), 4.4 parts by weight of polyvinylpyrrolidone (K82-86 from Ashland) and 79.6 parts by weight of DMAC was stirred, heated to 60°C and degassed so that It is processed into a homogeneous spinning mass. The spinning mass was extruded into strands through an annular spinneret with a center-controlled precipitant consisting of 35% DMAC and 65% water. The precipitating agent is guided within the hollow strands. The temperature of the ring spinneret was 70°C. The extruded strands are led through a precipitation chamber whose atmosphere has a relative humidity of 100%. The height of the sedimentation gap is 200 mm; the residence time of the sedimentation gap is set to 0.4 seconds. The strands were introduced into a precipitation bath consisting of water whose temperature was controlled at 80 °...
Embodiment 3
[0152] Embodiment 3: comparative example
[0153] The same materials as in Example 2 were used. A spinning solution consisting of 16 parts by weight of polysulfone, 4 parts by weight of polyvinylpyrrolidone and 80 parts by weight of DMAC was stirred, heated to 50° C. and degassed in order to process it into a homogeneous spinning mass. The spinning mass was extruded into strands through an annular spinneret with a center controlled precipitant consisting of 54% DMAC and 46% water. The precipitating agent is guided within the hollow strands. The temperature of the ring spinneret was 40°C. The extruded strands were led through a precipitation chamber whose atmosphere had a relative humidity of 30%. The height of the sedimentation gap is 600mm, and the residence time of the sedimentation gap is set to 1.35 seconds. The strands were introduced into a precipitation bath consisting of water whose temperature was controlled at 68 °C and precipitated into hollow fiber membranes. ...
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