Plexifilamentary Sheets
US-2015368416-A1 · Dec 24, 2015 · US
US11021811B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11021811-B2 |
| Application number | US-201515531653-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 2, 2015 |
| Priority date | Dec 2, 2014 |
| Publication date | Jun 1, 2021 |
| Grant date | Jun 1, 2021 |
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The present invention provides a continuous method for the production of at least one polymeric yarn comprising the steps of: mixing a polymer with a first solvent generating a mixture; homogenizing the mixture; rendering the mixture inert; dosing the mixture to an extruder; immersing the mixture in a quenching bath (30), wherein an air gap is maintained before the mixture achieves the surface of the liquid of the quenching bath (30) forming at least one polymeric yarn; drawing at least once the at least one polymeric yarn; washing the polymeric yarn with a second solvent that is more volatile than the first solvent; heating the at least one polymeric yarn; drawing at room temperature, at least once, the at least one polymeric yarn; and heat drawing, at least once, the at least one polymeric yarn, wherein the mixture comprises: a polymer comprising ultra-high molecular weight polyethylene, comprising an intrinsic viscosity of from 5 dL/g to 40 dL/g, and a polydispersity index of from 2 to 10; and a first solvent capable of dissolving the polymer under the process conditions, and comprising a dynamic viscosity, measured at a temperature of 37.8° C., according to ASTM D-445, greater than 10 cP. The present invention further provides a continuous system for the production of at least one polymeric yarn, comprising: means for mixing the polymer with a first solvent generating a mixture; means for homogenizing the mixture; means for rendering the mixture inert; means for dosing the mixture to an extruder; means for immersing the mixture in a quenching bath (30), wherein an air gap is maintained before the mixture achieves the surface of the liquid of the quenching bath (30) forming at least one polymeric yarn; means for drawing at least once the at least one polymeric yarn; means for washing for washing the at least one polymeric yarn with a second solvent that is more volatile than the first solvent; means for heating the at least one polymeric yarn; means for drawing at room temperature at least once the at least one polymeric yarn; and means for heat drawing at least once the at least one polymeric yarn, wherein the mixture comprises: a polymer comprising ultra-high molecular weight polyethylene, comprising an intrinsic viscosity of from 5 dL/g to 40 dL/g, and a polydispersity index of from 2 to 10; and a first solvent capable of dissolving the polymer under the process conditions and comprising a dynamic viscosity, as measured at a temperature of 37.8° C. according to the ASTM standard D-445, greater than 10 cP. Further, the present invention provides a polymeric yarn made according to the above stated method.
Opening claim text (preview).
What is claimed is: 1. A continuous method for the production of at least one polymeric yarn comprising the steps of: mixing a polymer with a first solvent, providing a mixture; homogenizing the mixture; rendering the mixture inert; dosing the mixture in an extruder, forming a homogeneous solution; dosing the solution in an orifice die, providing the solution with the shape of filament yarn; immersing the solution with the shape of filament yarn in a quenching bath, wherein an air gap is maintained before the mixture achieves a surface of the liquid of a quenching bath forming at least one gel yarn; drawing at least once the at least one gel yarn; washing the gel yarn with a second solvent that is more volatile than the first solvent; drying the at least one gel yarn; and heat drawing at least once the at least one gel yarn; the method being characterized in that in the step of dosing the solution in the orifice die: the minimum speed of the solution at an orifice die inlet is defined by V e > L T η S ( T ) ( 26000 M n ) 3 ϕ - 7 / 3 PDI 3 / 2 e log PDI 1 ( λ 0 - 1 ) ; and the maximum speed of the solution at the orifice die inlet is defined by V e < D e T η S ( T ) ( 26000 M w ) 3 ϕ - 7 / 3 log λ 0 λ 0 - 1 . 2. The method of claim 1 , characterized in that the mixture comprises: a polymer comprising ultra-high molecular weight polyethylene, comprising an intrinsic viscosity of between 5 dL/g and 40 dL/g, and a polydispersity index of between 2 and 10; a first solvent capable of dissolving the polymer under process conditions, and comprising a dynamic viscosity, as measured at a temperature of 37.8° C., according to ASTM D-445, of greater than 10 cP. 3. The method of claim 1 , characterized in that the mixture comprises: a polymer comprising ultra-high molecular weight polyethylene, comprising an intrinsic viscosity of between 10 dL/g and 20 dL/g, and a polydispersity index of between 3 and 6; and a first solvent capable of dissolving the polymer under process conditions, and comprising a dynamic viscosity, as measured at a temperature of 37.8° C., according to the standard ASTM D-445, of greater than 30 cP. 4. The method according to claim 1 , comprising a post drawing step in which the draw ratio is greater than 1.5 and lower than 3. 5. The method according to claim 1 , characterized in that the Survival Index is greater than 70%. 6. The method according to claim 1 , characterized in that: the polymer is selected from the group consisting of high molecular weight polyolefin, ultra high molecular weight polyolefin, ultra-high molecular weight polyethylene, high molecular weight polypropylene and ultra high molecular weight polypropylene, ethene-propene copolymer, polyvinyl alcohol, polyesters, polyoxide ethylene, and ultra-high molecular weight polyethylene, and the first solvent is selected from the group consisting of a mineral oil, aliphatic hydrocarbons, cyclo-aliphatic hydrocarbons, aromatic hydrocarbons, and halogenated hydrocarbons. 7. A polymeric yarn, made according to a method for the production of at least one polymeric yarn, said method comprising the steps of: mixing a polymer with a first solvent, providing a mixture; homogenizing the mixture; rendering the mixture inert; dosing the mixture in an extruder, forming a homogeneous solution; dosing the solution in an orifice die, providing the solution with the shape of filament yarn; immersing the solution with the shape of filament yarn in a quenching bath, wherein an air gap is maintained before the mixture achieves a surface of the liquid of a quenching bath forming at least one gel yarn; drawing at least once the at lea
polyethylene · CPC title
from polyolefins · CPC title
high strength · CPC title
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