Technique for Forming Porous Fibers
US-2019374672-A1 · Dec 12, 2019 · US
US11724002B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11724002-B2 |
| Application number | US-201816470858-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 19, 2018 |
| Priority date | Feb 28, 2017 |
| Publication date | Aug 15, 2023 |
| Grant date | Aug 15, 2023 |
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A method for forming a fiber is provided. The method comprises extruding a matrix polymer and a nanoinclusion additive to form a thermoplastic composition in which the nanoinclusion additive is dispersed within a continuous phase of the matrix polymer. The extruded thermoplastic composition is thereafter passed through a spinneret to form a fiber having a porous network containing a plurality of nanopores, wherein the average percent volume occupied by the nanopores within a given unit volume of the fiber is from about 3% to about 15% per cm3.
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What is claimed is: 1. A method for forming a fiber, the method comprising: extruding a matrix polymer and a nanoinclusion additive to form a thermoplastic composition in which the nanoinclusion additive is dispersed within a continuous phase of the matrix polymer, wherein the nanoinclusion additive contains a copolyetherester elastomer; and thereafter, passing the extruded thermoplastic composition through a spinneret to form a fiber having a porous network containing a plurality of nanopores, wherein the average percent volume occupied by the nanopores within a given unit volume of the fiber is from about 3% to about 15% per cm 3 . 2. The method of claim 1 , wherein the spinneret has a length-to-diameter ratio of about 6:1 or less. 3. The method of claim 1 , wherein the ratio of the melt flow rate of the matrix polymer to the melt flow rate of the nanoinclusion additive is about 2:1 or more. 4. The method of claim 1 , wherein the nanoinclusion additive has a melt flow rate of from about 0.1 to about 50 grams per 10 minutes, determined at a load of 2160 grams and at a temperature at least about 40° C. above the melting temperature of the nanoinclusion additive in accordance with ASTM D1238-13. 5. The method of claim 1 , wherein the matrix polymer has a melt flow rate of from about 0.5 to about 80 grams per 10 minutes, determined at a load of 2160 grams and at a temperature at least about 40° C. above the melting temperature of the matrix polymer in accordance with ASTM D1238-13. 6. The method of claim 1 , wherein extrusion occurs at a temperature of from about 180° C. to about 340° C. 7. The method of claim 1 , further comprising quenching the fiber after it is passed through the spinneret. 8. The method of claim 1 , wherein the fiber is a substantially continuous filament. 9. The method of claim 1 , wherein the fiber has a diameter of from about 1 to about 100 micrometers. 10. The method of claim 1 , wherein the nanoinclusion additive constitutes from about 0.01 wt. % to about 15 wt. % of the thermoplastic composition. 11. The method of claim 1 , wherein the nanoinclusion additive contains a siloxane polymer. 12. The method of claim 1 , wherein the nanoinclusion additive contains a polyepoxide. 13. The method of claim 1 , wherein the nanopores have an average cross-sectional dimension of about 800 nanometers or less. 14. The method of claim 1 , wherein the nanopores have an average axial dimension of from about 100 to about 5000 nanometers. 15. The method of claim 1 , wherein the matrix polymer includes a polyester. 16. The method of claim 15 , wherein the polyester is polyethylene terephthalate. 17. The method of claim 1 , wherein the matrix polymer includes a polyolefin. 18. The method of claim 17 , wherein the polyolefin is a propylene homopolymer. 19. The method of claim 1 , wherein the continuous phase constitutes from about 60 wt. % to about 99 wt. % of the thermoplastic composition. 20. The method of claim 1 , wherein the matrix polymer includes a polyester and wherein the continuous phase constitutes from about 60 wt. % to about 99 wt. % of the thermoplastic composition.
Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives thereof {(A61L15/225 takes precedence)} · CPC title
Polyesters derived from dicarboxylic acids and dihydroxy compounds (C08L67/06 takes precedence) · CPC title
Discontinuous hollow structure or microporous structure · CPC title
for forming hollow filaments · CPC title
from polyolefins · CPC title
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