Claims
- 1. A process for the preparation of a polymer solution which comprises the steps of: (a) mixing a polymer, other than cellulose esters of lower fatty acids, with a solvent to swell the polymer in the solvent; (b) cooling the swelled mixture; and then (c) warming the cooled mixture to dissolve the polymer in the solvent.
- 2. The process as claimed in claim 1, wherein the polymer is selected from the group consisting of polyolefins, polyamides, polysulfones, polyethers, polystyrenes, polycarbonates, polyacrylic polymers, polyacrylamides, polymethacrylic polymers, polymethacrylamides, polyvinyl alcohols, polyureas, polyesters, polyurethanes, polyimides, polyvinyl acetates, polyvinyl acetals and proteins.
- 3. The process as claimed in claim 1, wherein the polymer is mixed with the solvent at a temperature of -10 to 55.degree. C.
- 4. The process as claimed in claim 1, wherein the the swelled mixture is cooled to a temperature of -100 to -10.degree. C.
- 5. The process as claimed in claim 1, wherein the the swelled mixture is cooled at a rate of faster than 1.degree. C. per minute.
- 6. The process as claimed in claim 1, wherein the the cooled mixture is warmed to a temperature of 0 to 200.degree. C.
- 7. The process as claimed in claim 1, wherein the the cooled mixture is warmed to a temperature of 0 to 120.degree. C.
- 8. The process as claimed in claim 1, wherein the the cooled mixture is warmed at a rate of faster than 1.degree. C. per minute.
- 9. The process of claim 1, wherein the solvent is an organic solvent.
- 10. The process of claim 9, wherein the organic solvent is selected from the group consisting of ketones, esters, ethers, hydrocarbons and alcohols.
- 11. The process of claim 1, wherein the solvent has a boiling point in the range of 20 to 300.degree. C.
- 12. The process of claim 1, further comprising adding in step (a) one or more additives selected from the group consisting of plasticizers, deterioration inhibitors, dyes, and ultraviolet absorbents.
- 13. The process of claim 1, wherein the cooling step (b) is carried out in a closed system.
- 14. The process of claim 1, wherein the cooled mixture is warmed to a temperature of 0 to 55.degree. C.
- 15. The process of claim 1, wherein the warming step (c) is carried out in a closed system.
- 16. The process of claim 1, further comprising adjusting the solution concentration after step (c).
- 17. The process of claim 1, further comprising adding one or more components selected from the group consisting of plasticizers, deterioration inhibitors, dyes and ultraviolet absorbents after step (c).
Priority Claims (3)
Number |
Date |
Country |
Kind |
7-344614 |
Dec 1995 |
JPX |
|
8-216769 |
Jul 1996 |
JPX |
|
8-216772 |
Jul 1996 |
JPX |
|
CROSS-REFERENCE TO RELATED APPLICATION
This is a continuation-in-part application of U.S. patent application Ser. No. 08/759,638 filed on Dec. 5, 1996.
US Referenced Citations (3)
Number |
Name |
Date |
Kind |
3948870 |
Stoy et al. |
Apr 1976 |
|
4581431 |
Yamazaki et al. |
Apr 1986 |
|
5516818 |
Chen et al. |
May 1996 |
|
Foreign Referenced Citations (1)
Number |
Date |
Country |
07 23993A1 |
Jul 1996 |
EPX |
Non-Patent Literature Citations (2)
Entry |
J.M.G. Cowie et al., report in Makromol., The Dissolution and Stability of Cellulose . . . , 143, pp. 105-114 (1971). |
K. Kamide et al., Textile Machinery Society, Dry Spinning of Cellulose Triacetate Filament Yarns . . . , vol. 34, pp. 57-61 (1981). |
Continuation in Parts (1)
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Number |
Date |
Country |
Parent |
759638 |
Dec 1996 |
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