Process for removing residual spin solvent from a gel spun filament, the filament, multi-filament yarn and products comprising the filament

Patent metadata

Field	Value
Publication number	US-9260801-B2
Application number	US-59346908-A
Country	US
Kind code	B2
Filing date	Mar 21, 2008
Priority date	Mar 27, 2007
Publication date	Feb 16, 2016
Grant date	Feb 16, 2016

Abstract

Process for removing residual spin solvent from a gel spun, UHMwPE filament having an effective diameter of above 16 μm, comprising the steps of: removing residual spin solvent from the filament to a level of below 100 ppm at elevated temperature, while keeping the filament taut. The invention also relates to gel spun UHMwPE filament having an effective diameter of above 16 μm and a residual spin solvent residue of less than 100 ppm. Preferably the filament has a creep rate, measured at 50° C., under a load, so that the initial stress is 600 MPa, of less than 510 −6 sec −1 .

First claim

The invention claimed is:

1. A process for removal of residual spin solvent from a gel spun ultrahigh molecular weight polyethylene (UHMwPE) filament comprising the steps of:
(a) providing a gel spun UHMwPE filament having an effective diameter of above 16 μm and a residual spin solvent content of between 100 and 2000 ppm,
(b) winding the gel spun UHMwPE filament provided by step (a) around a frame so that the filament is taut around the frame at a tension of more than 0.15 g/dtex, and subsequently
(c) placing the frame with the filament wound taut therearound according to step (b) in an autoclave and removing residual spin solvent from the filament by subjecting the filament taut to super critical CO 2 extraction in the autoclave at a temperature between 80° C. and 147.5° C. and at a pressure between 50 bar and 400 bar for a time period between half an hour and 24 hours to thereby obtain a UHMwPE filament with residual spin solvent content of below 100 ppm.

2. The process according to claim 1 , which comprises providing a gel spun, UHMwPE filament having an effective diameter of above 18 μm.

3. The process according to claim 1 , wherein the elevated temperature is above 90° C.

4. The process according to claim 1 , wherein the elevated temperature is below 130° C.

5. The process according to claim 1 , wherein step (c) is carried out under a reduced air pressure so that the filament is in an environment having an oxygen content of less than 3 mol/m 3 .

6. The process according to claim 5 , wherein the oxygen content of the environment is less than 1 mol/m 3 .

7. The process according to claim 1 , wherein step (c) is practiced such that the spin solvent is removed to a level below 80 ppm.

8. The process according to claim 1 , wherein step (c) is practiced such that the spin solvent is removed to a level below 60 ppm.

9. The process according to claim 1 , wherein the filament does not contain spin finish when the residual spin solvent is removed according to step (c).

10. The process according to claim 1 , wherein step (a) comprises providing a gel spun, UHMwPE filament having an effective diameter of above 25 μm.

11. The process according to claim 1 , wherein step (a) comprises providing a gel spun, UHMwPE filament having an effective diameter of above 75 μm.

12. The process according to claim 1 , wherein step (a) comprises providing a gel spun, UHMwPE filament having an effective diameter of above 18 μm.

13. The process according to claim 1 , wherein step (a) comprises providing a gel spun, UHMwPE filament having a residual spin solvent content of between 200 and 1500 ppm.

14. The process according to claim 1 , wherein the filament is a monofilament or a multi-filament yarn.

15. The process according to claim 1 , wherein step (b) comprises keeping the filament taut around the frame with a tension of above 0.30 g/dtex.

16. The process according to claim 1 , wherein step (c) comprises subjecting the filament to super critical CO 2 extraction in an autoclave at a temperature between 110° C. and 130° C. and pressure between 100 bar and 400 bar.

17. The process according to claim 5 , wherein the oxygen content of the environment is less than 0.2 mol/m 3 .

18. The process according to claim 1 , wherein the UHMwPE filament with residual spin solvent content of below 100 ppm obtained after step (c) has a tenacity of at least 3.4 N/tex.

Assignees

• Marissen Roelof R
• Vaz Claudia Maria C M
• Snijder Carina Sacha C S
• Simmelink Joseph Arnold Paul Maria J A P M
• Nielaba Leonard Josef Arnold L J A
• Dsm Ip Assets Bv

Inventors

• Marissen Roelof R
• Vaz Claudia Maria C M
• Snijder Carina Sacha C S
• Simmelink Joseph Arnold Paul Maria J A P M
• Nielaba Leonard Josef Arnold L J A

Classifications

• D01F6/04 Primary

  from polyolefins · CPC title

• D01F13/04

  of synthetic polymers · CPC title

• A61L17/14

  Post-treatment to improve physical properties · CPC title

• D10B2321/0211

  high-strength or high-molecular-weight polyethylene, e.g. ultra-high molecular weight polyethylene [UHMWPE] · CPC title

• Y10T428/298

  Physical dimension · CPC title