Claims
- 1. Polyoxymethylene fiber comprising a polyoxymethylene copolymer that has a half-crystallization time of at least 30 sec when the polyoxymethylene copolymer is cooled from a molten state at 200° C. to 150° C. at a cooling rate of 80° C./min and maintained constantly at the temperature of 150° C.
- 2. The polyoxymethylene fiber as described in claim 1 wherein the half-crystallization time of the polyoxymethylene copolymer is at least 100 sec.
- 3. The polyoxymethylene fiber as described in claim 1 wherein the polyoxymethylene copolymer contains repeating units of oxyalkylene represented by the following formula (1) in repeating units of oxymethylene:-[-(CH2)n-O-]m (1) (In the formula, n represents an integer of two or more; and m is an integer of one or more).
- 4. The polyoxymethylene fiber as described in claim 3 wherein a content of the repeating units of oxyalkylene represented by formula (1) is from 0.5 to 10 mole percent to the total repeating units of oxymethylene and oxyalkylene.
- 5. The polyoxymethylene fiber as described in claim 3 wherein the content of the repeating units of oxyalkylene represented by formula (1) is from 2.0 to 10 mole percent to the total repeating units of oxymethylene units and oxyalkylene.
- 6. The polyoxymethylene fiber as described in claim 1 wherein the polyoxymethylene copolymer contains therein from 0 to 4 mmol/kg of a hemiformal terminal group detected through 1H-NMR.
- 7. The polyoxymethylene fiber as described in claim 1 that is prepared by melt spinning at a take-off speed of from 300 to 5000 m/min.
- 8. The polyoxymethylene fiber as described in claim 1 that is prepared by melt spinning at a take-off speed of from 1000 to 5000 m/min.
- 9. The polyoxymethylene fiber as described in claim 1 that is prepared by further heating and stretching after the melt spinning.
- 10. A process for producing polyoxymethylene fiber, comprising taking off fibrous matter spun from a spinning nozzle of a melt spinning apparatus while heating at an ambient temperature of from 140 to 250° C., when the polyoxymethylene copolymer is subjected to melt spinning to produce the polyoxymethylene fiber.
- 11. The process for producing polyoxymethylene fiber as described in claim 10 wherein when a point selected in the range of 0 to 10 cm from the surface of the spinning nozzle is taken as a heat-starting point (L1) and a point selected from the range exceeding 5 cm from the surface of the spinning nozzle is taken as a heat-finishing point (L2), heating is carried out between L1 and L2 [herein, L2≧L1+5 (unit: cm)].
- 12. The process for producing polyoxymethylene fiber as described in claim 11 wherein the heat-starting point (L1) is selected in the range of from 0 to 3 cm from the surface of the spinning nozzle.
- 13. The process for producing polyoxymethylene fiber as described in claim 11 wherein the heat-starting point (L1) is 0 cm from the surface of the spinning nozzle.
- 14. The process for producing polyoxymethylene fiber as described in claim 11 wherein the heat-finishing point (L2) is selected in the range of from 5 to 200 cm from the surface of the spinning nozzle.
- 15. The process for producing pblyoxymethylene fiber as described in claim 11 wherein the heat-finishing point (L2) is selected in the range of from 10 to 100 cm from the surface of the spinning nozzle.
- 16. The process for producing polyoxymethylene fiber as described in claim 11 wherein the heat-finishing point (L2) is selected in the range of from 10 to 80 cm from the surface of the spinning nozzle.
- 17. The process for producing polyoxymethylene fiber as described in claim 11 wherein the taking-off speed of the fibrous matter is from 300 to 5000 m/min.
- 18. The process for producing polyoxymethylene fiber as described in claim 11 wherein the taking-off speed of the fibrous matter is from 1000 to 5000 m/min.
- 19. The process for producing polyoxymethylene fiber wherein the polyoxymethylene fiber prepared according to a process as described in 10 is further heated and stretched.
- 20. The process for producing polyoxymethylene fiber as described in claim 10 wherein the half-crystallization time of the polyoxymethylene copolymer is at least 30 sec, when the polyoxymethylene copolymer is cooled from a molten state at 200° C. to 150° C. at a cooling rate of 80° C./min and maintained constantly at the temperature of 150° C.
- 21. The process for producing polyoxymethylene fiber as described in claim 20 wherein the half-crystallization time of the polyoxymethylene copolymer is at least 100 sec.
- 22. The process for producing polyoxymethylene fiber as described in claim 10 wherein the polyoxymethylene copolymer contains repeating units of oxyalkylene represented by the following formula (1) in the repeating units of oxymethylene, and a content of the repeating units of oxyalkylene is from 2.0 to 10 mol percent to the total repeating units of oxymethylene and oxyalkylene-[-(CH2)n-O-]m- (1) (In the formula, n represents an integer of two or more; and m represents an integer of one or more).
- 23. A fiber which comprises the polyoxymethylene copolymer of claim 1.
- 24. A process for making a fiber comprise melt-spinning the polyoxymethylene copolymer of claim 1.
Priority Claims (1)
Number |
Date |
Country |
Kind |
2001-283391 |
Sep 2001 |
JP |
|
Parent Case Info
This application is the U.S. national phase of international application PCT/JP02/09517 filed 17 Sep. 2002 which designated the U.S. and claims benefit of JP 2001-283391 dated 18 Sep. 2001, the contents of each of which are hereby incorporated by reference.
PCT Information
Filing Document |
Filing Date |
Country |
Kind |
PCT/JP02/09517 |
|
WO |
00 |
Publishing Document |
Publishing Date |
Country |
Kind |
WO03/02526 |
3/27/2003 |
WO |
A |
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A |
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A |
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JP |
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JP |
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JP |
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