Modified polyester chip for manufacturing high-elasticity polyester fiber and preparation method thereof
A polyester fiber and modified polyester technology, applied in the direction of single-component polyester rayon, etc., can solve the problems of decreased thermal stability of fiber products, increased filament breakage rate, high equipment requirements, etc., and achieve stable spinning performance , reduce crystallinity, increase the effect of ductility
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Embodiment 1
[0019] (1) Adjust terephthalic acid, ethylene glycol and ethylene glycol antimony into a slurry according to the conventional ratio; then add 2-methyl-1,3-propanediol to the slurry to obtain a modified slurry, so that 2 - The molar ratio of methyl-1,3-propanediol to ethylene glycol is 5:95;
[0020] (2) Put the modified slurry prepared above into the esterification reaction kettle to directly esterify into esterified products. The esterification temperature is 250-280°C, the esterification pressure is 0.3Mpa, and the reaction time is 2.5 hours. The liquid phase polycondensation is carried out in the prepolymerization tank and the final polymerization tank, and after the liquid phase polycondensation, the modified polyester chip finished product with an intrinsic viscosity of 0.5-0.7dl / g for the manufacture of high elastic polyester fiber is obtained by cooling and slicing; the prepolymerization temperature The temperature is 260-275°C, the vacuum degree is 800pa, and the pre-c...
Embodiment 2
[0022] (1) Adjust terephthalic acid, propylene glycol and ethylene glycol antimony into a slurry according to the conventional ratio; then add 2-methyl-1,3-propanediol to the slurry to obtain a modified slurry, so that 2- The molar ratio of methyl-1,3-propanediol to propylene glycol is 5:95;
[0023] (2) Put the modified slurry prepared above into the esterification reaction kettle to directly esterify into esterified products. The esterification temperature is 250-280°C, the esterification pressure is 0.3Mpa, and the reaction time is 2.5 hours. The liquid phase polycondensation is carried out in the prepolymerization kettle and the final polymerization kettle, and after the liquid phase polycondensation, the modified polyester chip finished product with an intrinsic viscosity of 0.8-1.0dl / g for the manufacture of high elastic polyester fiber is obtained by cooling and slicing; the prepolymerization temperature The temperature is 260-275°C, the vacuum degree is 800pa, and the ...
Embodiment 3
[0025] (1) Adjust terephthalic acid, butanediol and ethylene glycol antimony into a slurry according to the conventional ratio; then add 2-methyl-1,3-propanediol to the slurry to obtain a modified slurry, so that 2 - The molar ratio of methyl-1,3-propanediol to butanediol is 3:97;
[0026] (2) Put the modified slurry prepared above into the esterification reaction kettle to directly esterify into esterified products. The esterification temperature is 250-280°C, the esterification pressure is 0.3Mpa, and the reaction time is 2.5 hours. The liquid phase polycondensation is carried out in the prepolymerization tank and the final polymerization tank, and after the liquid phase polycondensation, the modified polyester chips with an intrinsic viscosity of 0.9-1.1dl / g are obtained by cooling and slicing for the manufacture of high elastic polyester fibers; the prepolymerization temperature The temperature is 260-275°C, the vacuum degree is 800pa, and the pre-condensation time is 1 ho...
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