Fully-molten low-melting-point polyester fibers and preparation method thereof
A low-melting polyester and fiber technology, applied in the field of polyester fibers, can solve the problems of difficult crystallization, high dimensional shrinkage of interwoven fabrics, and high comonomer content, and achieve improved stability, good dimensional stability, and low dimensional shrinkage. rate effect
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Embodiment 1
[0042] In this embodiment, the following method is used to prepare the finished fiber of full-melt low-melting point polyester:
[0043] (1) Configure terephthalic acid, ethylene glycol, isophthalic acid and antimony-based catalysts into a mixed slurry, wherein the molar ratio of isophthalic acid and terephthalic acid is 1:1, and the amount of antimony-based catalysts The antimony element is 450ppm of the total mass of terephthalic acid, and the molar ratio of the alcohol component ethylene glycol to the acid component terephthalic acid and isophthalic acid in the mixed slurry is 1.13:1, and then the mixed slurry It is transported to the esterification system for esterification reaction. The esterification system is composed of the first esterification reactor and the second esterification reactor. The reaction temperature of the first esterification reactor is 260°C and the reaction time is 2h. The reaction temperature of the reaction kettle is 265°C and the reaction time is ...
Embodiment 2
[0048] In this embodiment, the following method is used to prepare the finished fiber of full-melt low-melting point polyester:
[0049] (1) Terephthalic acid, ethylene glycol, isophthalic acid and antimony-based catalysts are formulated into a mixed slurry, wherein the molar ratio of isophthalic acid to terephthalic acid is 0.667:1, and the amount of antimony-based catalysts The antimony element is 430ppm of the total mass of terephthalic acid, the molar ratio of the alcohol component ethylene glycol to the acid component terephthalic acid and isophthalic acid in the mixed slurry is 2:1, and then the mixed slurry It is transported to the esterification system for esterification reaction. The esterification system is composed of an independent esterification reactor, wherein the reaction temperature of the esterification reactor is 285°C and the reaction time is 1.5h to obtain a low-melting point polyester oligomer melt body;
[0050] (2) The low-melting point polyester oligo...
Embodiment 3
[0054] In this embodiment, the following method is used to prepare the finished fiber of full-melt low-melting point polyester:
[0055] (1) Configure terephthalic acid, ethylene glycol, 2,2-dimethyl-1,3-propanediol and antimony-based catalysts into a mixed slurry, in which 2,2-dimethyl-1,3-propanediol The molar ratio to terephthalic acid is 0.4:1, the amount of antimony-based catalyst is 200ppm of the total mass of terephthalic acid in terms of antimony, and the alcohol component ethylene glycol and 2,2-dimethyl- The molar ratio of 1,3-propanediol to the acid component terephthalic acid is 1.05:1, and then the mixed slurry is sent to the esterification system for esterification reaction. The first esterification reaction tank and the second esterification reaction tank of the esterification system Reactor composition, wherein the reaction temperature of the first esterification reactor is 265°C, the reaction time is 4h, the reaction temperature of the second esterification re...
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Abstract
Description
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Application Information
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