Polyvinyl alcohol-based hollow fiber membrane and process for producing the same

• US 5,976,433 A
• Filed: 12/23/1997
• Issued: 11/02/1999
• Est. Priority Date: 06/05/1995
• Status: Expired due to Fees

• Current Assignee: Kuraray Company Limited
• Original Assignee: Kuraray Company Limited
• Inventors: Kusudo, Osamu, Komatsu, Kensaku
• Primary Examiner(s): FORTUNA, ANA M
• Application Number:
  US08/998,041
• Time in Patent Office: 679 Days
• Field of Search: 210/500.42, 210/500.23, 264/41, 264/514, 264/638, 264/640, 428/398
• US Class Current: 264/41
• CPC Class Codes: B01D 69/08 Hollow fibre membranes manufacture of hollow fibres D01D5/24, D01F1/08
• CPC Class Codes: B01D 71/38 Polyalkenylalcohols; Polyalkenylesters; Polyalkenylethers; Polyalkenylaldehydes; Polyalkenylketones; Polyalkenylacetals; Polyalkenylketals
• CPC Class Codes: B01D 71/381 Polyvinylalcohol
• CPC Class Codes: D01D 5/24 with a hollow structure; Spinnerette packs therefor D01D5/38 takes precedence; producing tubes of plastic material B29D; addition of agents forming hollow filaments D01F1/08
• CPC Class Codes: D01F 6/14 from polymers of unsaturated alcohols, e.g. polyvinyl alcohol, or of their acetals or ketals
• CPC Class Codes: Y10T 428/2975 Tubular or cellular
• CPC Class Codes: Y10T 428/2978 Surface characteristic

Abstract

A polyvinyl alcohol-based hollow fiber membrane having a ratio between the size of particles of 90% rejection and that of particles of 10% rejection of not more than 5, thus proving to have a sharp fractionating property, is produced by a process which comprises, on producing a polyvinyl alcohol-based hollow fiber membrane by dry-jet wet spinning or wet spinning, using a spinneret having heat insulating structure.

Claims

1. A process for producing a polyvinyl alcohol-based hollow fiber membrane, which comprises forming said polyvinyl alcohol-based hollow fiber membrane by dry-jet wet spinning or wet spinning of a spinning dope with a spinneret having a heat insulated structure, thereby preventing said spinning dope from undergoing partial phase separation by cooling in the spinneret.

2. The process of claim 1, wherein said spinning dope comprises a solution of a vinyl alcohol-based polymer as a principal component, a pore-forming agent and a solvent capable of dissolving said vinyl alcohol-based polymer and said pore-forming agent and having an upper critical separation temperature of from about 30 to 95°

C.

3. The process of claim 2, which further comprises spinning the spinning dope at a temperature of an external coagulating bath with an internal coagulating liquid being set lower than said upper critical separation temperature.

4. The process of claim 2, wherein said pore-forming agent is selected from the group consisting of polyethylene glycol, polypropylene glycol, tetraethylene glycol, triethylene glycol, ethylene glycol, lower alkyl alcohols, polyhydric alcohols and lower alkyl esters.

5. The process of claim 4, wherein said polyhydric alcohol is glycerine or butanediol or a mixture thereof.

6. The process of claim 4, wherein said lower alkyl ester is ethyl lactate or butyl lactate or a mixture thereof.

7. The process of claim 2, wherein said solvent is selected from the group consisting of water, alcohol/water, dimethyl sulfoxide, dimethylformamide, dimethylacetamide and N-methylpyrrrolidone.

8. The process of claim 7, wherein said solvent is water.

9. The process of claim 2, wherein said spinning dope further comprises boric acid, acetic-acid, a surfactant or an anti-foaming agent or a mixture thereof.

10. The process of claim 9, wherein said spinning dope has a an upper critical separation temperature of from 50 to 90°

C.

11. The process of claim 1, wherein said vinyl alcohol-based polymer has a degree of polymerization of from about 500 to 16,000.

12. The process of claim 11, wherein said vinyl alcohol-based polymer has a degree of polymerization of at least about 1,700.

13. The process of claim 1, wherein a bath draft thereof is set at about 1.0 to 20.0.

14. The process of claim 1, wherein the spinning dope has a concentration of vinyl alcohol-based polymer of from about 1 to 50% by weight.

15. The process of claim 14, wherein the spinning dope has a concentration of vinyl alcohol-based polymer of from about 3 to 20% by weight.

16. The process of claim 1, which further comprises treating said formed polyvinyl alcohol-based hollow fiber membrane with treatment comprising drawing, neutralization, water washing, wet heat treatment, sodium sulfate substitution, membrane modification or drying or a combination thereof.

17. The process of claim 16, wherein said membrane modification comprises acetalization, etherification, esterification or crosslinking.