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US 2018/0023218 A9Published application
Process and product of high strength uhmw pe fibers
AssigneeHoneywell International Inc.
InventorsTHOMAS Y. TAM, JOHN A. YOUNG, QIANG ZHOU, CONOR J. TWOMEY, CHARLES R. ARNETT
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Abstract
An improved process for solution spinning of ultra-high molecular weight polyethylene (UHMW PE) filaments, wherein the 10 wt % solution of the UHMW PE in mineral oil at 250° C. has a Cogswell extensional viscosity and a shear viscosity within select ranges.
Claims20
1-20. (canceled)
A solid ultra-high molecular weight polyethylene (UHMW PE) filament produced by a process comprising the steps of:
- a) selecting an UHMW PE having an intrinsic viscosity (IV) from about 5 dl/g to about 45 dl/g when measured in decalin at 135° C., wherein a 10 wt. % solution of the UHMW PE in mineral oil at 250° C. has a Cogswell extensional viscosity (λ) in accordance with the following formula:
- λ≧5,917(IV)0.8;
- b) dissolving the UHMW PE in a solvent at elevated temperature to form a solution having a concentration of from about 5 wt. % to about 50 wt. % of UHMW PE;
- c) discharging the solution through a spinneret to form solution filaments;
- d) cooling the solution filaments to form gel filaments;
- e) removing solvent from the gel filaments to form solid filaments containing less than about 5 wt. % of solvent;
- f) stretching at least one of the solution filaments, the gel filaments and the solid filaments to a combined stretch ratio of at least 10:1, wherein the solid filaments are stretched to a ratio of at least 2:1. stretch ratio of at least 10:1, wherein at least 2:1 is of the solid filaments.
4 more elements
A solid ultra-high molecular weight polyethylene (UHMW PE) filament produced by a process comprising the steps of:
- a) selecting an UHMW PE having an intrinsic viscosity from 5 to 45 dl/g when measured in decalin at 135° C., wherein a 10 wt. % solution of the UHMW PE in mineral oil at 250° C. has a Cogswell extensional viscosity and a shear viscosity such that the Cogswell extensional viscosity is at least eight times the shear viscosity;
- b) dissolving the UHMW PE in a solvent to form a solution having a concentration of from about 5 wt. % to about 50 wt. % of UHMW PE;
- c) discharging the solution through a spinneret to form solution filaments;
- d) cooling the solution filaments to form gel filaments;
- e) removing solvent from the gel filaments to form solid filaments containing less than about 5 wt. % of solvent;
- f) stretching at least one of the solution filaments, the gel filaments and the solid filaments to a combined stretch ratio of at least 10:1, wherein the solid filaments are stretched to a ratio of at least 2:1.
3 more elements
Dependencies are inferred from the claim text.