Method for preparing 2,3-butanediol modified polyester chips
A technology of polyester slices and butanediol, applied in the direction of single-component polyester rayon, etc., can solve the problems of high crystallinity and low thermal shrinkage, and achieve stable performance, uniform dyeing, and excellent spinning performance
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Embodiment 1
[0038] First, on the continuous polyester equipment, the monomers of terephthalic acid (PTA), 2,3-butanediol and ethylene glycol (EG) are mixed according to the The molar ratio of ethylene glycol (EG) monomer is 1: 0.07: 1.23, respectively continuously and stably metered and added to the slurry tank for beating, and silicotungstic acid and stannous chloride are added in the beating tank, wherein silicon tungsten The add-on of acid and the mol ratio of terephthalic acid are 0.010%, and the add-on of stannous chloride and the mol ratio of phthalic acid are 0.08%;
[0039] Then the above-mentioned slurry is continuously and stably transported to the reaction kettles of esterification-I, esterification-II and esterification-III, and stabilizers are continuously added to the reaction kettles of esterification-III; Polycondensation and final polycondensation to obtain a modified polyester melt; the polyester melt is cast, pelletized, and dried to obtain modified polyester chips. Wh...
Embodiment 2
[0043] First, on the continuous polyester equipment, the monomers of terephthalic acid (PTA), 2,3-butanediol and ethylene glycol (EG) are mixed according to the , The molar ratio of ethylene glycol (EG) monomer is 1:0.15:1.15, respectively continuously and stably metered and added to the slurry tank for beating, and silicotungstic acid and stannous chloride are added to the beating tank, wherein silicon tungsten The add-on of acid and the mol ratio of terephthalic acid are 0.015%, and the add-on of stannous chloride and the mol ratio of phthalic acid are 0.03%;
[0044] Then the above-mentioned slurry is continuously and stably transported to the reaction kettles of esterification-I, esterification-II and esterification-III, and stabilizers are added to the reaction kettles of esterification-III; and final polycondensation to obtain a modified polyester melt; the polyester melt is cast, pelletized, and dried to obtain modified polyester chips. Wherein, the specific esterifica...
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