Preparation method of thermal degradation-resistant degradation PBT polyester with high viscosity
A high-viscosity, heat-resistant technology, applied in the field of PBT polyester preparation, can solve the problems of thermal degradation of PBT melt and the addition of multiple chain extenders, etc., to achieve stable properties, reduce the content of terminal carboxyl groups, and increase the esterification rate Effect
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Embodiment 1
[0021] Weigh the raw material with terephthalic acid and 1,4-butanediol molar ratio of 1:1.05 and put it into the slurry tank for beating for 1 hour, weigh the catalyst tetrabutyl titanate and dissolve it in 1,4-butanediol to prepare the catalyst Disperse in tank for 1 hour, mix the two kinds of slurries and continue beating for 0.5 hours, prepare the reaction slurry and transport it to the esterification reactor; the esterification temperature is 231°C, the esterification pressure is 22kPa, the esterification residence time is 3.5h, After completion, the esterification product is transported to the pre-condensation reactor, and the esterification rate reaches 99.5% at this time; the pre-condensation temperature is 240°C, the pre-condensation pressure is 3kPa, and the residence time is 0.75h. The prepared prepolymers are sequentially prepolymerized filter and prepolymer cooler for filtration and cooling, and then transported to the final polymerization reactor; the final polyco...
Embodiment 2
[0024]Weigh terephthalic acid and 1,4-butanediol molar ratio of 1:1.2 raw materials into the slurry tank for 1.5h, weigh the catalyst tetrabutyl titanate dissolved in 1,4-butanediol in the catalyst Disperse in the preparation tank for 1.5 hours, mix the two kinds of slurry and continue beating for 1 hour, prepare the reaction slurry and transport it to the esterification reactor; the esterification temperature is 240°C, the esterification pressure is 18kPa, the esterification residence time is 4h, and the esterification After completion, the esterification product is transported to the precondensation reactor, and the esterification rate reaches 99.7% at this time; the precondensation temperature is 245°C, the precondensation pressure is 2kPa, and the residence time is 1h. The filter and the prepolymer cooler are filtered and cooled, and then sent to the final polymerization reactor; the final polycondensation temperature is 260°C, the final polycondensation pressure is 0.05kPa...
Embodiment 3
[0027] Weigh the raw material with a molar ratio of terephthalic acid and 1,4-butanediol of 1:1.15 and put it into the slurry tank for beating for 1.2 hours, weigh the catalyst tetrabutyl titanate and dissolve it in 1,4-butanediol in the catalyst Disperse in the preparation tank for 1 hour, mix the two kinds of slurry and continue beating for 0.5 hours, prepare the reaction slurry and transport it to the esterification reactor; the esterification temperature is 210°C, the esterification pressure is 20kPa, and the esterification residence time is 3.8h. After the esterification is completed, the esterification product is transported to the precondensation reactor, and the esterification rate reaches 99.5% at this time; the precondensation temperature is 250 ° C, the precondensation pressure is 5kPa, and the residence time is 0.85h. The polymer filter and the prepolymer cooler are filtered and cooled before being transported to the final polymerization reactor; the final polyconde...
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