Sea-island fiber with PA6 as island components, preparation method thereof, and ultrafine fiber formed by sea-island fibers
A sea-island fiber and ultra-fine fiber technology, applied in fiber processing, single-component polyamide rayon, melt spinning, etc., can solve the problems of low recycling value of polyvinyl alcohol aqueous solution, environmental pollution, waste of resources, etc.
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[0070] More specifically, the preparation method of the modified polyester comprises:
[0071] 1) Ethylene glycol and terephthalic acid undergo esterification reaction; the temperature of the esterification reaction is 240-270°C; the time of the esterification reaction is 2-4h;
[0072] 2) Add isophthalic acid dibasic acid ester-5-sodium sulfonate or isophthalic acid dibasic acid ester-5-potassium sulfonate, and add 2-methyl-1,3-propanediol and 1,3- Propylene glycol is transesterified; the temperature of the transesterification reaction is 240-270°C; the time of the transesterification reaction is 1-3h;
[0073] 3) adding catalyst and heat stabilizer to carry out polycondensation reaction; the temperature of polycondensation reaction is 270-300°C; the time of polycondensation reaction is 2-4h; the catalyst is antimony trioxide; the heat stabilizer is trimethyl phosphate or phosphoric acid Triphenyl ester; the added amount of the heat stabilizer is 0.02% to 0.06% of the mass o...
Embodiment 1
[0077] In this example, the molar ratio of terephthalic acid, ethylene glycol, isophthalic acid dibasic acid ester-5-sulfonate sodium or potassium, 2-methyl-1,3-propanediol and 1,3-propanediol The ratio is 1:2.0:0.05:0.10:0.08, and the modified copolyester is formed by the above-mentioned method.
[0078] In this embodiment, the sea component of the sea-island fiber uses the modified copolyester as described above, and the island component uses PA6. In this embodiment, the mass ratio of the sea component to the island component is 1:7.
[0079] Using melt composite spinning technology, the island component PA6 is fed into the first screw extruder for melt extrusion, and at the same time, the sea component modified copolyester is fed into the second screw extruder for extrusion; the first The temperature in the five zones in the screw extruder is 265°C-270°C, 270°C-275°C, 275°C-280°C, 275°C-280°C, 270°C-275°C; the temperature in the five zones in the second screw extruder is 2...
Embodiment 2
[0083] In this example, the molar ratio of terephthalic acid, ethylene glycol, isophthalic acid dibasic acid ester-5-sulfonate sodium or potassium, 2-methyl-1,3-propanediol and 1,3-propanediol The ratio is 1:1.5:0.03:0.05:0.10, and the modified copolyester is formed by the above-mentioned method.
[0084] In this embodiment, the sea component in the sea-island fiber adopts the modified copolyester as described above, and the island component adopts semi-dull PA6 and black PA6 masterbatches. The mass ratio of the sea component to the island component in this embodiment is 1:5.
[0085] Using melt composite spinning technology, the island component semi-dull PA6 and black PA6 masterbatches are blended with a dispersant, and the blending ratio is 7:3. After mixing evenly, they are fed into the first screw extruder for melt extrusion. At the same time, Feed the sea component modified copolyester into the second screw extruder for extrusion; the temperature in the five zones of th...
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