Modified polyester and preparing method thereof
A technology for modifying polyester and polybasic acid, applied in the field of polyester preparation, can solve the problems of poor polyester product performance, reduced polyester thermal stability, and gray polyester color, etc., and achieves high dye uptake, reduced dosage, bright color effect
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[0026] Preparation of Control 1:
[0027] Add 500g PTA, 280g EG (the molar ratio of PTA and EG is 1:1.5), 150ug / g ethylene glycol antimony in turn in the PU2.5 reaction polymerization kettle, and carry out the esterification reaction at 240°C, 0.2-0.3MPa, and 40rpm rotating speed. , when the esterification rate reaches more than 95%, vent to normal pressure, end the esterification, put in 300ug / g triphenyl phosphite, raise the temperature to 280°C, drop the absolute pressure below 100pa, react for 2 hours, and use Nitrogen to eliminate vacuum, discharge, cut into pellets, and dry to obtain polyester chips.
[0028] Preparation of Control 2:
[0029] 500g PTA, 280g EG, 150ug / g ethylene glycol antimony, 3ug / g cobalt phosphate were sequentially added to the PU2.5 reaction polymerization kettle, and the esterification reaction was carried out at 240°C, 0.2-0.3MPa, and 40rpm. More than 95%, vent to normal pressure, end esterification, put in 300ug / g triphenyl phosphite, raise the...
Embodiment 1
[0035] Add 500g PTA, 280gEG, 150ug / g ethylene glycol antimony, 14ug / g cobalt phosphate, 20ug / g calcium carbonate in sequence to the PU2.5 reaction polymerization kettle, and carry out the esterification reaction at 240°C, 0.2-0.3MPa, and 40rpm. , when the esterification rate reaches more than 95%, vent to normal pressure, end the esterification, put in 300ug / g triphenyl phosphite, raise the temperature to 280°C, drop the absolute pressure below 100pa, react for 2 hours, and use Nitrogen to eliminate vacuum, discharge, cut into pellets, and dry to obtain polyester chips.
Embodiment 2
[0037] 500g PTA, 280g EG, 150ug / g ethylene glycol antimony, 10ug / g cobalt phosphate, 10ug / g barium sulfate were added in sequence to the PU2.5 reaction polymerization kettle, and the esterification reaction was carried out at 240°C, 0.2-0.3MPa, and 40rpm. , when the esterification rate reaches more than 95%, vent to normal pressure, end the esterification, add 300ug / g triphenyl phosphite, raise the temperature to 280°C, drop the absolute pressure below 100pa, react for 2 hours, and use Nitrogen to eliminate vacuum, discharge, cut into pellets, and dry to obtain polyester chips.
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