US2016201225A1PendingUtilityA1
Process for removing residual spin solvent from a gel spun filament, the filament, multi-filament yarn and products comprising the filament
Est. expiryMar 27, 2027(~0.7 yrs left)· nominal 20-yr term from priority
Inventors:Roelof MarissenClaudia Maria VazCarina S. SnijderJoseph Arnold Paul Maria SimmelinkLeonard Josef Arnold Nielaba
A61L 17/14D01F 13/04D10B 2321/0211Y10T428/298D01F 6/04Y02P70/62
51
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Claims
Abstract
Processes for removing residual spin solvent from a gel spun, UHMwPE filament having an effective diameter of above 16 μm, comprise 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. Gel spun UHMwPE filaments having an effective diameter of above 16 μm and a residual spin solvent residue of less than 100 ppm are also provided. 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 5·10 −6 sec −1 .
Claims
exact text as granted — not AI-modified1 . A process for removing residual spin solvent from a gel spun, UHMwPE filament, comprising the steps of:
(a) providing a gel spun UHMwPE filament having a titer of 2-100 dtex, and a residual spin solvent content of between 100 and 2000 ppm, (b) winding the filament provided in step a) around a frame such that the filament is kept taut with a tension of above 0.15 g/dtex, and (c) removing residual spin solvent from the filament by subjecting the filament around a frame of step b) to an elevated temperature above 80° C. and below 140° C., to obtain a treated UHMwPE filament having a residual solvent level of below 60 ppm.
2 . The process according to claim 1 , wherein the filament provided in step a) has residual spin solvent content of more than 200 ppm.
3 . The process according to claim 1 , wherein the filament provided in step a) has a titer of 2-30 dtex.
4 . The process according to claim 1 , wherein the filament is provided in step a) as a multi-filament yarn.
5 . The process according to claim 1 , wherein the elevated temperature is above 90° C.
6 . The process according to claim 1 , wherein the elevated temperature is above 100° C.
7 . The process according to claim 1 , wherein the elevated temperature is below 130° C.
8 . The process according to claim 1 , wherein the elevated temperature is below 125° C.
9 . The process according to claim 1 , wherein step (c) is carried out in an environment having an oxygen content of less than 3 mol/m 3 .
10 . The process according to claim 9 , wherein step (c) is carried out under a reduced air pressure.
11 . The process according to claim 1 , wherein step (c) is carried out for at least half an hour.
12 . The process according to claim 1 , wherein the treated filament obtained in step (c) has a residual spin solvent level of below 40 ppm.
13 . The process according to claim 1 , wherein the treated filament obtained in step (c) has a tenacity of at least 3.4 N/tex.
14 . The process according to claim 1 , wherein the treated filament obtained in step (c) has a creep rate, measured at 50° C. under a load so that the initial stress is 600 MPa, of less than 5·10 −6 sec−1.
15 . The process according to claim 14 , wherein the treated filament has a creep rate of less than 10 −7 sec −1 .
16 . A treated gel spun UHMwPE filament as obtained by the process according to claim 1 .
17 . A gel spun UHMwPE filament having a diameter of above 16 μm and a residual spin solvent residue of less than 60 ppm.
18 . The gel spun UHMwPE filament according to claim 17 , wherein the filament has a creep rate, measured at 50° C. under a load so that the initial stress is 600 MPa, of less than 5·10 −6 sec −1 .
19 . The gel spun UHMwPE filament according to claim 17 , wherein the filament has a creep rate, measured at 50° C. under a load so that the initial stress is 600 MPa, of less than 8·10 −6 sec −1 .
20 . The gel spun UHMwPE filament according to claim 17 , wherein the filament has a creep rate, measured at 50° C. under a load so that the initial stress is 600 MPa, of less than 10 −7 sec −1 .
21 . A multi-filament yarn comprising a filament according to claim 16 .
22 . A mono-filament consisting of one filament according to claim 16 .
23 . A product for medical application comprising the yarn according to claim 21 .
24 . A product for medical application comprising the monofilament according to claim 22 .Cited by (0)
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