Modified PET (polyethylene terephthalate) copolymer for high-toughness heat-shrinkable film and preparation method of modified PET copolymer
A heat-shrinkable film and copolymer technology, applied in the field of polyester, can solve the problems of brittleness, high heat shrinkage, and restrictions on wide application, and achieve the effects of low production cost, improved toughness, and reduced cost
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Embodiment 1
[0066] (1) On the daily production of 5 tons of small flexible modified polyester continuous polyester polycondensation production equipment, with terephthalic acid (PTA, containing 5wt% adipic acid), and ethylene glycol (containing 25wt% neopentyl glycol , 5wt% isosorbide), 250ppm catalyst—ethylene glycol antimony, a mixture of phthalic acid and adipic acid and a mixture of ethylene glycol, neopentyl glycol and isosorbide added in a molar ratio of 1:1.15; The time is 40 minutes; put it into the slurry supply tank for standby;
[0067] (2) The slurry obtained in step (1) is pumped into the first esterification reaction production still to carry out the esterification reaction. The esterification temperature is 255°C, the pressure is 2.5Kpa, and the flow rate is 200Kg / h; After the kettle, the esterification rate reaches 91-93%; it is pumped into the pipeline and passes through the syringe 1;
[0068] (3) Use syringe 1 to add antioxidant 1010 and trimethyl phosphate online; the...
Embodiment 2
[0073] (1) On the daily production of 5 tons of small flexible modified polyester continuous polyester polycondensation production equipment, with terephthalic acid (PTA, containing 10wt% adipic acid), and ethylene glycol (containing 30wt% neopentyl glycol , 10wt% isosorbide), 250ppm catalyst—ethylene glycol antimony, a mixture of phthalic acid and adipic acid and a mixture of ethylene glycol, neopentyl glycol and isosorbide are added in a molar ratio of 1:1.15; Time 30 minutes, put into the slurry supply tank for standby;
[0074] (2) Pump the slurry obtained in step (1) into the first esterification reaction production tank to carry out the esterification reaction. The esterification temperature is 255°C, the pressure is 3Kpa, and the flow rate is 180Kg / h. Make the esterification rate reach 91-93% after passing through the first esterification reaction kettle; pump it into the pipeline and pass through the syringe 1;
[0075] (3) Use syringe 1 to add antioxidant 1010 and tr...
Embodiment 3
[0080] (1) On the daily production of 5 tons of small flexible modified polyester continuous polyester polycondensation production equipment, with terephthalic acid (PTA, containing 2wt% adipic acid), and ethylene glycol (containing 15wt% neopentyl glycol , 2wt% isosorbide), 250ppm catalyst—antimony ethylene glycol, a mixture of phthalic acid and adipic acid and a mixture of ethylene glycol, neopentyl glycol and isosorbide are added in a molar ratio of 1:1.15; The time is 35 minutes; put it into the slurry supply tank for standby;
[0081] (2) pump the slurry obtained in step (1) into the first esterification reaction production still, carry out esterification reaction, the esterification temperature is 260 ℃, pressure 3Kpa, flow velocity is 190Kg / h; After the kettle, the esterification rate reaches 91-93%; it is pumped into the pipeline and passes through the syringe 1;
[0082] (3) Using syringe 1 to add antioxidant 1098 and triphenyl phosphate online; the addition of antio...
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