Plexifilamentary Sheets
US-2015368416-A1 · Dec 24, 2015 · US
US9765447B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9765447-B2 |
| Application number | US-201514922339-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 26, 2015 |
| Priority date | Feb 24, 2012 |
| Publication date | Sep 19, 2017 |
| Grant date | Sep 19, 2017 |
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Processes for preparing ultra-high molecular weight polyethylene (“UHMW PE”) filaments and multi-filament yarns, and the yarns and articles produced therefrom. Each process produces UHMW PE yarns having tenacities of 45 g/denier to 60 g/denier or more at commercially viable throughput rates.
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What is claimed is: 1. A process for producing an ultra-high molecular weight polyethylene (UHMW PE) multi-filament yarn having a tenacity of at least 45 g/denier, wherein said yarn is fabricated from an UHMW PE polymer having an intrinsic viscosity of at least about 21 dl/g and a yarn intrinsic viscosity that exceeds 90% relative to the intrinsic viscosity of the UHMW PE polymer; wherein said intrinsic viscosities are measured in decalin at 135° C. according to ASTM D1601-99, the process comprising: a) providing a mixture comprising an UHMW PE polymer and a spinning solvent, said UHMW PE polymer having an intrinsic viscosity of at least about 21 dl/g as measured in decalin at 135° C. according to ASTM D1601-99; b) forming a solution from said mixture; c) passing the solution through a spinneret to form a plurality of solution filaments; d) cooling the solution filaments to a temperature below the gel point of the UHMW PE polymer to thereby form a gel yarn; e) removing the spinning solvent from the gel yarn to form a dry yarn; and f) stretching at least one of the solution filaments, the gel filaments and the solid filaments in one or more stages to form a yarn product having a tenacity of greater than 45 g/d, and wherein said yarn product has an intrinsic viscosity that exceeds 90% relative to the intrinsic viscosity of the UHMW PE polymer; wherein said intrinsic viscosities are measured in decalin at 135° C. according to ASTM D1601-99. 2. The process of claim 1 wherein the yarn is fabricated from an UHMW PE polymer having an intrinsic viscosity of 21 dl/g or more. 3. The process of claim 1 wherein the yarn intrinsic viscosity is at least about 28 dl/g. 4. The process of claim 1 wherein said process further comprises adding an antioxidant to said mixture and/or to said solution. 5. The process of claim 1 wherein said process further comprises sparging said mixture or said solution with nitrogen prior to step c). 6. The process of claim 1 wherein the post-drawn, highly oriented yarn product is produced at a throughput rate of at least about 3.0 g/min/yarn end for a yarn product having a tenacity of 45 g/d. 7. The process of claim 1 wherein the yarn is fabricated from a composition comprising a blend of an UHMW PE polymer and a solvent, wherein the UHMW PE polymer is present in said blend in an amount of less than 5% by weight based on the weight of the solvent plus the UHMW PE polymer. 8. The process of claim 1 wherein said process further comprises adding an antioxidant to said mixture and/or to said solution and sparging said mixture or said solution with nitrogen prior to step c). 9. A process for producing an ultra-high molecular weight polyethylene (UHMW PE) multi-filament yarn, comprising: a) providing a mixture comprising a UHMW PE polymer and a spinning solvent, wherein the UHMW PE polymer is present in said mixture in an amount of less than 5.0% by weight based on the weight of the solvent plus the weight of the UHMW PE polymer; b) forming a solution from said mixture; c) passing the solution through a spinneret to form a plurality of solution filaments; d) cooling the solution filaments to a temperature below the gel point of the UHMW PE polymer to thereby form a gel yarn; e) removing the spinning solvent from the gel yarn to form a dry yarn; and f) stretching at least one of the solution filaments, the gel filaments and the solid filaments in one or more stages to form a yarn product. 10. The process of claim 9 wherein said process further comprises adding an antioxidant to said mixture and/or to said solution. 11. The process of claim 10 wherein said process further comprises sparging said mixture or said solution with nitrogen prior to step c). 12. The process of claim 9 wherein said solution consists of said UHMW PE polymer and said spinning solvent. 13. The process of claim 9 wherein the solution includes UHMW PE in an amount of 4.0% or less by weight of the solution. 14. The process of claim 13 wherein said solution consists of said UHMW PE polymer and said spinning solvent. 15. The process of claim 9 wherein said UHMW PE polymer provided in a) has an intrinsic viscosity of at least about 35 dl/g as measured in decalin at 135° C. according to ASTM D1601-99. 16. The process of claim 13 wherein at least one of the solution filaments, the gel filaments and the solid filaments are stretched in one or more stages to form a yarn product having a tenacity of greater than 45 g/d, and wherein said UHMW PE polymer provided in a) has a ratio of weight average molecular weight to number average molecular weight (M w /M n ) of 3 or less. 17. The process of claim 16 wherein said yarn product has an intrinsic viscosity of at least about 21 dl/g as measured in decalin at 135° C. according to ASTM D1601-99. 18. The process of claim 1 wherein the yarn intrinsic viscosity exceeds 95% relative to the intrinsic viscosity of the UHMW PE polymer.
high-strength or high-molecular-weight polyethylene, e.g. ultra-high molecular weight polyethylene [UHMWPE] · CPC title
from polyolefins · CPC title
Fabric composed of a fiber or strand which is of specific structural definition · CPC title
characterised by the method of forming fleeces or layers, e.g. reorientation of fibres · CPC title
Other non-woven fabrics · CPC title
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