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

US2016201225A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2016201225-A1
Application numberUS-201614994121-A
CountryUS
Kind codeA1
Filing dateJan 12, 2016
Priority dateMar 27, 2007
Publication dateJul 14, 2016
Grant date

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  1. Title

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  2. Abstract

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  5. First independent claim

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Abstract

Official abstract text for this publication.

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 .

First claim

Opening claim text (preview).

1 . 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 .

Assignees

Inventors

Classifications

  • Post-treatment to improve physical properties · CPC title

  • of synthetic polymers · CPC title

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

  • Physical dimension · CPC title

  • D01F6/04Primary

    from polyolefins · CPC title

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What does patent US2016201225A1 cover?
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 tha…
Who is the assignee on this patent?
Dsm Ip Assets Bv
What technology area does this patent fall under?
Primary CPC classification D01F6/04. Mapped technology areas include Textiles & Paper.
When was this patent published?
Publication date Thu Jul 14 2016 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).