A kind of polyester composition and its production method and application
A manufacturing method and composition technology, applied in the field of polyester composition and its manufacturing, can solve the problem that the regeneration inhibition effect of specific oligomer cyclic trimer is not obvious, the content of polyester cyclic trimer is reduced, and it is difficult to implement and other problems, to achieve the effect of good regeneration inhibition effect, industrial simplicity and excellent heat resistance.
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Embodiment 1
[0047] At a temperature of 250°C, 166 parts by weight of PTA and 71.3 parts by weight of EG were added to the esterification reactor, and the esterification reaction was carried out under normal pressure. When the esterification reaction was completed, the temperature in the esterification reactor was 250°C. Fractional distillation of water yields small molecule polymers.
[0048] Add the polycondensation reaction catalyst AO that is equivalent to polyester weight 70ppm in terms of antimony element in gained small molecule polymer, the stabilizer PA that is equivalent to copolyester weight 100ppm in phosphorus element, start decompression, heat up after 5min, pressure passes through The pressure is reduced to about 300Pa in 1 hour, and the temperature rises to 290°C after 1.5 hours; when the polycondensation reaction ends, the pressure in the reactor is about 200Pa. The obtained polymer was subjected to solid state polymerization at 230° C. for 20 hours to obtain polyester chi...
Embodiment 2
[0051] At a temperature of 250°C, 166 parts by weight of PTA and 71.3 parts by weight of EG were added to the esterification reactor, and the esterification reaction was carried out under normal pressure. When the esterification reaction was completed, the temperature in the esterification reactor was 250°C. Fractional distillation of water yields small molecule polymers.
[0052] Add the polycondensation reaction catalyst AO that is equivalent to polyester weight 110ppm in terms of antimony element in gained small molecule polymer, be equivalent to the stabilizer PA of copolyester weight 100ppm in phosphorus element, start decompression, heat up after 5min, pressure passes through The pressure is reduced to about 300Pa in 1 hour, and the temperature rises to 290°C after 1.5 hours; when the polycondensation reaction ends, the pressure in the reactor is about 200Pa. The obtained polymer was solid-state polymerized at 230° C. for 20 hours to obtain polyester chips with an intrin...
Embodiment 3
[0055] At a temperature of 250°C, 166 parts by weight of PTA and 71.3 parts by weight of EG were added to the esterification reactor, and the esterification reaction was carried out under normal pressure. When the esterification reaction was completed, the temperature in the esterification reactor was 250°C. Fractional distillation of water yields small molecule polymers.
[0056] Add the polycondensation reaction catalyst AO that is equivalent to polyester weight 195ppm in terms of antimony element in gained small molecule polymer, be equivalent to the stabilizer PA of copolyester weight 70ppm in phosphorus element, start to decompress after 5min, heat up, pressure passes through The pressure is reduced to about 300Pa in 1 hour, and the temperature rises to 290°C after 1.5 hours; when the polycondensation reaction ends, the pressure in the reactor is about 200Pa. The obtained polymer was solid-state polymerized at 230° C. for 20 hours to obtain polyester chips with an intrins...
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