Biodegradable branched aromatic polyester-aliphatic polyester multi-block polymer
A multi-block copolymer and aromatic polyester technology, which is applied in the field of biodegradable branched aromatic polyester-aliphatic polyester multi-block copolymer, can solve the problem of poor melt strength, poor stability, and easy tearing Crack and other issues
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Embodiment 1
[0039] The preparation of biodegradable branched polybutylene terephthalate-block-polybutylene succinate-block-polypropylene succinate multi-block copolymer comprises the following steps:
[0040] ①Synthesis of hydroxyl-terminated polybutylene terephthalate prepolymer
[0041] Take terephthalic acid and 1,4-butanediol with a molar ratio of 1:1.8 by weighing a total of 1,500 g into the reactor, and then add 1 g of antimony trioxide (as a catalyst), wherein the reactor is equipped with a high Pure nitrogen interface, mechanical stirrer, water separator, condenser tube, etc. Start stirring (rotating speed 200r / min), heat the reaction system to 180°C, and then raise the temperature to 220°C in a temperature-programmed manner; at this temperature, the above-mentioned monomers are subjected to esterification reaction until the water output reaches 95wt% of the theoretical water output , raise the temperature to 230°C, close the nitrogen passage valve and start vacuuming to below 10...
Embodiment 2
[0049] Preparation of biodegradable branched polyethylene terephthalate-block-polyethylene adipate-block-poly(ethylene glycol succinate-co-pentanediol succinate) ester A multi-block copolymer comprising the steps of:
[0050] ①Synthesis of hydroxyl-terminated polyethylene terephthalate prepolymer
[0051] Weigh 1,800 g of terephthalic acid and ethylene glycol in a molar ratio of 1:1.9 and add them to the reactor, then add 2 g of ethylene glycol antimony (as a catalyst), wherein the reactor is equipped with a high-purity nitrogen port, Mechanical stirrer, water separator, condenser tube, etc. Start stirring (200r / min), heat the reaction system to 190°C, and then raise the temperature to 240°C in a temperature-programmed manner; at this temperature, the above-mentioned monomers are subjected to esterification reaction until the water output reaches 95wt% of the theoretical water output, Raise the temperature to 260°C, close the nitrogen passage valve and start vacuuming to bel...
Embodiment 3
[0059] Preparation of biodegradable branched polyethylene terephthalate-block-poly(1,4-cyclohexanedimethyl adipate-block-poly(ethylene adipate-co-adipate 1, 2-octanediol) ester multi-block copolymer, comprises the following steps:
[0060] ①Synthesis of hydroxyl-terminated polyethylene terephthalate prepolymer
[0061] Weigh 1,400 g of terephthalic acid and ethylene glycol in a molar ratio of 1:1.6 and add them to the reactor, then add 1.3 g of antimony ethylene glycol (as a catalyst), and the reactor is equipped with a high-purity nitrogen port , mechanical agitator, water separator, condenser tube, etc. Start stirring (200r / min), heat the reaction system to 190°C, and then raise the temperature to 240°C in a temperature-programmed manner; at this temperature, the above-mentioned monomers are subjected to esterification reaction until the water output reaches 95wt% of the theoretical water output, Raise the temperature to 270°C, close the nitrogen channel valve and start va...
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