Monofilament based on a polyamide composition
US-2015065648-A1 · Mar 5, 2015 · US
US10494740B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10494740-B2 |
| Application number | US-201615388999-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 22, 2016 |
| Priority date | Dec 23, 2015 |
| Publication date | Dec 3, 2019 |
| Grant date | Dec 3, 2019 |
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Methods of producing a polyamide filaments and fibers are provided. The methods include providing a dual-terminated polyamide and spinning the dual-terminated polyamide at a speed of 3500 m/min to 8000 m/min to form a fiber. In one embodiment, the polyamide has an amine endgroup concentration of 25 mmol/kg to 40 mmol/kg and a carboxyl endgroup concentration of 18 mmol/kg to 50 mmol/kg. Fibers and yarns comprising polyamide filaments and fibers formed from the method are also disclosed.
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What is claimed is: 1. A method of producing a plurality of fibers, the method comprising: providing a dual-terminated polyamide-6 (PA-6) having an amine endgroup concentration of 25 mmol/kg to 40 mmol/kg, a carboxyl endgroup concentration of 18 mmol/kg to 50 mmol/kg, and a relative viscosity of 2.6 RV to 3.0 RV; and spinning the dual-terminated polyamide-6 (PA-6) at a speed of 3500 m/min to 8000 m/min to form the fibers. 2. The method of claim 1 , wherein spinning includes heating the dual-terminated polyamide-6 (PA-6) to a temperature of 230° C. to 300° C. 3. The method of claim 1 , wherein spinning includes extruding the dual-terminated polyamide-6 (PA-6) through a spinneret including tri-lobal shape holes, wherein the tri-lobal shape holes define an R value of 0 to 0.1 mm. 4. The method of claim 1 , wherein the polyamide fibers each comprises a plurality of filaments, and the polyamide fibers have a denier per filament of 1.5 to 5. 5. The method of claim 1 , wherein the dual-terminated polyamide-6 (PA-6) includes amine endgroups and carboxyl endgroups with different, chemically distinct terminators. 6. The method of claim 1 , wherein the dual-terminated polyamide-6 (PA-6) has an amine endgroup concentration of 27 mmol/kg to 37 mmol/kg. 7. The method of claim 1 , wherein the dual-terminated polyamide-6 (PA-6) has an amine endgroup concentration of 30 mmol/kg to 35 mmol/kg. 8. The method of claim 1 , wherein the dual-terminated polyamide-6 (PA-6) has a carboxyl endgroup concentration of 20 mmol/kg to 40 mmol/kg. 9. The method of claim 1 , wherein the dual-terminated polyamide-6 (PA-6) has a carboxyl endgroup concentration of 22 mmol/kg to 30 mmol/kg. 10. The method of claim 1 , wherein the dual-terminated polyamide-6 (PA-6) has a relative viscosity of 2.7 RV to 3.0 RV. 11. The method of claim 1 , wherein the dual-terminated polyamide-6 (PA-6) has a relative viscosity of 2.8 RV to 3.0 RV. 12. The method of claim 1 , wherein the dual-terminated polyamide-6 (PA-6) has a polydispersity index less than 1.8. 13. The method of claim 1 , wherein the dual-terminated polyamide-6 (PA-6) has an extractables content of less than 0.8 wt. %. 14. The method of claim 1 , wherein prior to the spinning step, the dual-terminated polyamide-6 (PA-6) is heated to a temperature of 240° C. to 300° C. 15. The method of claim 1 , wherein prior to the spinning step, the dual-terminated polyamide-6 (PA-6) is heated to a temperature of 250° C. to 290° C. 16. The method of claim 1 , wherein the spinning step is carried out at a speed of 4000 m/min to 6000 m/min. 17. The method of claim 4 , wherein the polyamide fibers each comprises a plurality of filaments, and the polyamide fibers have a denier per filament of 1.7 to 5. 18. The method of claim 4 , wherein the polyamide fibers each comprises a plurality of filaments, and the polyamide fibers have a denier per filament of 1.7 to 3.
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