Claims
- 1. A process for manufacturing polyethylene terephthalate fibers having improved low-pilling properties which comprise
- admixing in the feed throat of an extruder polyethylene terephthalate discrete solid polymer materials having an inherent viscosity of about 0.56 to about 0.60 with about 0.25% by weight ethylene glycol to form an admixture;
- melting in said extruder said solid polymer materials into a liquid and reacting said admixture to lower the inherent viscosity of said polyethylene terephthalate fibers to an inherent viscosity of about 0.39 to about 0.43, said inherent viscosity being determined by a concentration of 0.5% of the polymer in a solvent comprising 60% by weight phenol and 40% by weight tetrachloroethane, the polymer being dissolved at 125.degree. C. and being measured at 25.degree. C.;
- extruding the admixture into fibers;
- drafting the fibers; and
- heatsetting the fibers at a constant length.
- 2. A process as defined in claim 1, wherein said discrete solid polyethylene terephthalate polymer materials is in the form of pellets.
- 3. A process as defined in claim 1, wherein said fibers are heatset at constant length for about 90.+-.5 seconds at a temperature of about 200.degree. C. to about 215.degree. C.
- 4. A process as defined in claim 1, wherein said fibers are drawn at a ratio of about 4:1.
- 5. A process as defined in claim 2, wherein said extruder is maintained at a temperature of about 265.degree. C. to about 270.degree. C.
- 6. A process as defined in claim 2, wherein said fibers are heatset at constant length for about 90.+-.5 seconds at a temperature of about 200.degree. C. to about 215.degree. C.
- 7. A process as defined in claim 1, wherein said polyethylene terephthalate has an inherent viscosity of about 0.58.
- 8. A polyester fiber as made by the process of claim 1, said fiber being low pilling.
- 9. A polyester fiber as made by the process of claim 3, said fiber being low pilling, having a tenacity of about 3.5 to about 4.5 grams per denier, and an elongation of about 17% to about 27% and tenacity at 10% elongation of about 2.9 to about 3.5 grams per denier, and a shrinkage at 190.degree. C. for 10 minutes of about 6% to about 8%.
- 10. A process as defined in claim 1, wherein said fibers are relaxed up to about 5% while being heatset to a controlled length.
- 11. A process as defined in claim 1, wherein said fibers are relaxed up to about 2.5% while being heatset to a controlled length.
- 12. A process as defined in claim 11 wherein said fibers are heatset to a controlled length for about 90.+-.5 seconds at a temperature of about 200.degree. C. to about 215.degree. C.
- 13. A process as defined in claim 10, wherein said fibers are drawn at a ratio of about 3.9:1 to about 4.3:1.
- 14. A process as defined in claim 10, wherein said polyethylene terephthalate has an inherent viscosity of about 0.58 to about 0.60.
- 15. A polyester fiber as made by the process of claim 10, said fiber being low-pilling, having a tenacity of about 3.5 to about 4.65 grams per denier, an elongation of about 17% to about 27%, tenacity at 10% elongation of about 3.0 to about 3.95 grams per denier, and a shrinkage at 190.degree. C. for 10 minutes of about 6% to about 8%.
- 16. A polyester fiber as made by the process of claim 10, said fiber being low pilling, having a tenacity of about 4.0 to about 4.5 grams per denier, an elongation of about 17% to about 27%, tenacity at 10% elongation of about 3.2 to about 3.7 grams per denier, and a shrinkage at 190.degree. C. for 10 minutes of about 6% to about 8%.
Parent Case Info
This is a continuation-in-part application of U.S. Ser. No. 186,103 filed Sept. 11, 1980 abandoned.
US Referenced Citations (10)
Foreign Referenced Citations (4)
Number |
Date |
Country |
43-4546 |
Feb 1968 |
JPX |
47-2061 |
Jan 1972 |
JPX |
49-35618 |
Apr 1974 |
JPX |
50-13622 |
Feb 1975 |
JPX |
Continuation in Parts (1)
|
Number |
Date |
Country |
Parent |
186103 |
Sep 1980 |
|