Claims
- 1. A process for the preparation of a porous regenerated cellulose hollow fiber having a hollow portion extending continuously along the entire fiber length and a screen filter structure, comprising the steps of extruding a cuprammonium solution of a cellulose from an annular spinning orifice and coagulating, regenerating and water-washing the extrudate, said spinning solution being extruded from an outer annular spinning orifice and liquid that is composed of at least one organic solvent free of hydroxyl groups, having a solubility of at least 10% by weight in a 28% aqueous solution of ammonia, which does not swell a cellulose and having a composition causing micro-phase-separation in the cuprammonium solution of a cellulose, being extruded from a central spinning orifice, to cause micro-phase-separation to occur before the coagulation of said fiber.
- 2. A process for the preparation of a porous regeneration cellulose hollow fiber according to claim 1, wherein the liquid is extruded as a hollowing agent from the central spinning orifice, and the extrudate is fibrous.
- 3. A process for the preparation of a porous regenerated cellulose hollow fiber according to claim 2, wherein both the hollowing agent liquid extruded from the central spinning orifice and a coagulant having direct contact with the outer wall portion of the fibrous extrudate are mixed solutions comprising at least one organic solvent free of hydroxyl groups, having a solubility of at least 10% by weight in a 28% aqueous solution of ammonia, which does not swell a cellulose and having a composition causing micro-phase-separation in the cuprammonium solution of a cellulose.
- 4. A process for the preparation of a porous regenerated cellulose hollow fiber according to claim 1, wherein at least one organic solvent having a boiling point lower than 100.degree. C., a solubility of at least 10% by weight in water and free of hydroxyl groups is added to the spinning solution at a concentration lower than the concentration corresponding to the gel point or at a concentration not higher than 30% by weight.
- 5. A process for the preparation of a porous regenerated cellulose hollow fiber according to claim 1, wherein the cellulose concentration in the spinning solution is in the range of from 4 to 10% by weight.
- 6. A process for the preparation of a porous regenerated cellulose hollow fiber according to claim 2, wherein both the hollowing agent liquid extruded from the central spinning orifice and a coagulant having direct contact with the outer wall portion of the fibrous extrudate comprise an organic solvent, ammonia and water, the concentration of ammonia is not more than 5% by weight based on water, and the concentration of the organic solvent is in the range of from 20 to 160% by weight based on water.
- 7. A process for the preparation of a porous regenerated cellulose hollow fiber according to claim 6, wherein the organic solvent is acetone.
- 8. A process for the preparation of a porous regenerated cellulose hollow fiber according to claim 1, wherein the average molecular weight of the cellulose dissolved in the cuprammonium solution is at least 1.times.10.sup.5.
- 9. A process for the preparation of a porous regenerated cellulose hollow fiber according to claim 3, wherein at least one organic solvent having a boiling point lower than 100.degree. C., a solubility of at least 10% by weight in water and free of hydroxyl groups is added to the spinning solution at a concentration corresponding to the gel point or at a concentration not higher than 30% by weight.
- 10. A process for the preparation of a porous regenerated cellulose hollow fiber according to claim 9, wherein the cellulose concentration in the spinning solution is in the range of from 4 to 10% by weight.
- 11. A process for the preparation of a porous regenerated cellulose hollow fiber according to claim 3, wherein the cellulose concentration in the spinning solution is in the range of from 4 to 10% by weight.
- 12. A process for the preparation of a porous regenerated cellulose hollow fiber according to claim 3, wherein both the hollowing agent liquid extruded from the central spinning orifice and the coagulant having direct contact with the outer wall portion of the fibrous extrudate comprise an organic solvent, ammonia and water, the concentration of ammonia is not more than 5% by weight based on water, and the concentration of the organic solvent is in the range of from 20 to 160% by weight based on water.
- 13. A process for the preparation of a porous regenerated cellulose hollow fiber according to claim 3, wherein the average molecular weight of the cellulose dissolved in the cuprammonium solution is at least 1.times.10.sup.5.
Priority Claims (2)
Number |
Date |
Country |
Kind |
58-76305 |
May 1983 |
JPX |
|
58-76306 |
May 1983 |
JPX |
|
Parent Case Info
This is a division of application Ser. No. 604,512, filed Apr. 27, 1984, now U.S. Pat. No. 4,604,326.
US Referenced Citations (4)
Foreign Referenced Citations (2)
Number |
Date |
Country |
49-13424 |
Feb 1974 |
JPX |
55-1363 |
Jan 1980 |
JPX |
Divisions (1)
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Number |
Date |
Country |
Parent |
604512 |
Apr 1984 |
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