Method of manufacturing high-strength sheath-core type synthetic fiber, and high-strength sheath-core type synthetic fiber manufactured thereby
Abstract
The present disclosure relates to a method of manufacturing a high-strength sheath-core type synthetic fiber and high-strength sheath-core type synthetic fiber manufactured thereby, the method including forming a fiber by melt-spinning a thermoplastic polymer of a sheath component and a core component through a spinning pack including a sheath-core type bicomponent spinning nozzle; performing a heat treatment by allowing a molten fiber to pass through a heating zone disposed directly below the spinning nozzle during the melt-spinning; cooling the heat-treated fiber; and drawing the cooled fiber, wherein the sheath component includes a resin including the sheath component having elongation viscosity and thermal conductivity lower and specific heat higher than those of a resin included in the core component, and an ultra-fine high-strength synthetic fiber satisfying predetermined strength or higher as compared to a fine diameter and intrinsic viscosity may be provided.
Claims
exact text as granted — not AI-modified1 . A method of manufacturing a high-strength sheath-core type synthetic fiber, the method comprising:
forming a fiber by melt-spinning a thermoplastic polymer of a sheath component and a core component, through a spinning pack including a sheath-core type bicomponent spinning nozzle; performing a high-temperature heat treatment by allowing a molten fiber to pass through a heating zone disposed directly below the spinning nozzle during the melt-spinning; cooling the heat-treated as-spun fiber; and drawing the cooled as-spun fiber, wherein the sheath component includes a resin including the sheath component having elongation viscosity and thermal conductivity lower and specific heat higher than those of a resin included in the core component.
2 . The method of claim 1 , wherein the sheath-core type synthetic fiber includes an islands-in-the-sea type fiber.
3 . The method of claim 1 , wherein, when the sheath-core type synthetic fiber is an islands-in-the-sea type fiber, a volume ratio between a sea component and an island component is 10:90 to 90:10.
4 . The method of claim 1 , wherein a thermoplastic polymer of the sheath component and the core component is independently selected from a group consisting of at least one polyester-based polymer selected from a group consisting of polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polytrimethylene terephthalate (PTT), polycyclohexanedimethanol terephthalate (PCT), polylactic acid (PLA), polyethylene naphthalate (PEN), polyethylene furanoate (PEF), and polyarylate (PAR); at least one polyamide-based polymer selected from among nylon 6, nylon 6,6, nylon 4 and nylon 4,6; and at least one polyolefin-based polymer selected from a group consisting of polyethylene and polypropylene.
5 . The method of claim 1 , wherein a difference in thermal conductivities of thermoplastic polymers between the sheath component and the core component is 0.01 J/m·s·K to 10 J/m·s·K, and a difference in specific heats therebetween is 0.05 KJ/Kg·K to 50 KJ/Kg·K.
6 . The method of claim 1 , wherein thermoplastic polymers of the sheath component and the core component satisfy at least one of conditions as below: melt viscosity of 10 poise to 10,000 poise, glass transition temperature (Tg) of 5° C. to 300° C., and crystallinity temperature of 5° C. to 300° C.
7 . The method of claim 2 , wherein the number of island fibers in the islands-in-the-sea type fiber is in a range of 1 to 1,000,000.
8 . The method of claim 1 , wherein the heating zone locally heats the fiber by a heating element formed as a circular-type element or a strip-type element in a periphery of the spinning nozzle hole.
9 . The method of claim 1 , wherein a residence time of the molten thermoplastic polymer passing through each hole in the spinning nozzle is 3 seconds or less, and a flow rate is 0.01 cc/min to 10 cc/min.
10 . A sheath-core type synthetic fiber formed of a sheath component and a core component, wherein the sheath component includes a resin having elongation viscosity and thermal conductivity lower and specific heat higher than those of a resin included in the core component.
11 . The sheath-core type synthetic fiber of claim 10 , wherein a difference in thermal conductivities of thermoplastic polymers between the sheath component and the core component is 0.01 J/m·s·K to 10 J/m·s·K, and a difference in specific heats therebetween is 0.05 KJ/Kg·K to 50 KJ/Kg·K.
12 . The sheath-core type synthetic fiber of claim 10 , wherein thermoplastic polymers of the sheath component and the core component satisfy at least one of conditions as below: melt viscosity of 10 poise to 10,000 poise, glass transition temperature (Tg) of 5° C. to 300° C., and crystallinity temperature of 5° C. to 300° C.
13 . The sheath-core type synthetic fiber of claim 10 , wherein the sheath-core type fiber is an islands-in-the-sea type fiber containing polyethylene terephthalate (PET) island yarn including an island component having a diameter of 10 nm to 500 μm and satisfying physical properties equal to or higher than strength calculated by Equation 1 below:
Strength (tensile strength, g/d)=15.873×intrinsic viscosity (I.V.) of PET fiber−3.841 Equation 1.
14 . The sheath-core type synthetic fiber of claim 13 , wherein the island yarn has an intrinsic viscosity (I.V.) of 0.5 to 3.0.
15 . The sheath-core type synthetic fiber of claim 10 , wherein the sheath-core type fiber is an islands-in-the-sea type fiber including an island component having a diameter of 10 nm to 500 μm and containing nylon island yarn satisfying physical properties equal to or higher than strength calculated by Equation 2 below:
Strength
(
tensile
strength
,
g
/
d
)
=
8.6
×
relative
viscosity
(
R
v
)
of
nylon
fiber
-
14.44
Equation
2
16 . The sheath-core type synthetic fiber of claim 15 , wherein the island yarn has a relative viscosity (Rv) of 2.0 to 5.0.
17 . The sheath-core type synthetic fiber of claim 10 , wherein, when two or more melting point peaks are present on a DSC of the core component, a difference in temperatures therebetween peaks is 10° C. or less.Join the waitlist — get patent alerts
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