Abstract A hollow fiber membrane made of a cellulose ester having a membrane thickness of not more than 75 μm, and having void volume (x, % by volume) of the membrane and a rate of ultrafiltration (y, ml/m 2 .hr.mmHg) satisfying the following formula: 55x-2500≦y≦48x+600 wherein x≧60, and further has a β-lipoprotein sieving coefficient (sc) of not less than 0.95, and preferably having further not more than 2% of change ratio in the axial direction and in the radial direction when dipped freely in water at 121° C. for 20 minutes. Said hollow fiber membrane is useful for the medical use, such as the exchange of plasma in patients, collection of plasma from healthy donors, the pre-treatment of plasma for the collection and purification of valuable materials contained in plasma.
A method comprising: producing a hollow fiber membrane made of a cellulose ester for separation of plasma, by extruding a spinning solution containing 20% by weight or more of a cellulose ester in an aprotic polar solvent having a boiling point of 150° C. or higher or a non-solvent through a tube in orifice nozzle together with an inner solution which is an aqueous solution of the same solvent or non-solvent as used for the spinning solution, and coagulating the extruded membrane in a coagulation bath under the following conditions: 0° C.<T.sub.1 -T.sub.2 ≦40° C. wherein T 1 is a temperature of extrusion and T 2 is a temperature in the coagulation bath, and the concentration of the solvent or non-solvent in the coagulation bath and in the inner solution: ≧50% by weight.
Claim 2
Independent Claim
133 words
A method comprising: producing a hollow fiber membrane made of a cellulose ester for separation of plasma, by extruding a spinning solution containing 20% by weight or more of a cellulose ester in an aprotic polar solvent having a boiling point of 150° C. or higher or a non-solvent through a tube in orifice nozzle together with an inner solution which is an aqueous solution of the same solvent or non-solvent as used for the spinning solution, and coagulating the extruded membrane in a coagulation bath under the following conditions: 0° C.<T.sub.1 -T.sub.2 ≦40° C. wherein T 1 is a temperature of extrusion and T 2 is a temperature in the coagulation bath, and the concentration of the solvent or non-solvent in the coagulation bath and in the inner solution: ≧50% by weight.
Claim 3
Dependent Claim
34 words
The method for the production of a hollow fiber membrane according to claim 1, wherein the coagulation bath contains an aqueous solution of the same solvent or non-solvent as used in the spinning solution.
Claim 4
Dependent Claim
30 words
The method for the production of a hollow fiber membrane according to claim 1, wherein the hollow fiber membrane is subjected to heat-treatment at 80° C. or higher after coagulation.