Preparation method of all-biological-base poly butylenes succinate (PBS)
A technology for polybutylene succinate and dimethyl succinate is applied in the field of preparing biodegradable aliphatic polyester, which can solve the problems of poor thermal stability, poor product color and low molecular weight, etc., so as to improve the molecular weight , High product yield, the effect of reducing pollution
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Embodiment 1
[0029] Embodiment 1 transesterification method
[0030] Weigh 58.4g of biomass dimethyl succinate, 43.2g of 1,4-butanediol, 0.01g of calcium acetate, 0.01g of magnesium acetate and 0.01g of zinc acetate into a 250ml three-necked flask, and stir one of them. One port is connected to nitrogen protection, and the other port is connected to water separator and distillation column; start stirring, and heat the reaction system to 150°C; after 10 minutes of reaction, the temperature is raised to 220°C by program heating (heating rate is 5°C / min); keep the temperature for reaction 150min until the output of methanol reaches 95wt% of the theoretical value, the transesterification reaction is considered to be over. The by-products are mainly methanol and tetrahydrofuran, and the content of tetrahydrofuran is 0.005%. In addition, there are small amounts of unreacted dimethyl succinate and 1,4-butanediol. After the transesterification reaction, lower the temperature of the system (cooli...
Embodiment 2
[0032] Embodiment 2 transesterification method
[0033] Weigh 58.4g of biomass dimethyl succinate, 50.4g of 1,4-butanediol, and 0.05g of lithium acetate into a 250ml three-necked flask, one of which is connected to stirring, one is connected to nitrogen protection, and the other is connected to water separation Start stirring and heat the reaction system to 160°C; after 30 minutes of reaction, the temperature is raised to 200°C by program heating (heating rate is 5°C / min); keep the temperature for 180 minutes until the amount of methanol output reaches the theoretical value 95wt% can be considered as the end of the transesterification reaction. The by-products are mainly methanol and tetrahydrofuran, and the content of tetrahydrofuran is 0.02%. In addition, there are small amounts of unreacted dimethyl succinate and 1,4-butanediol. After the transesterification reaction, lower the temperature of the system (cooling rate is 10°C / min) to 155°C, remove the water trap and conden...
Embodiment 3
[0035] Embodiment 3 transesterification method
[0036] Weigh 58.4g of biomass dimethyl succinate, 43.2g of 1,4-butanediol, 0.02g of calcium acetate and 0.02g of tetraisopropyl titanate into a 250ml three-necked flask, one of which is stirred and the other is stirred. Connect the nitrogen protection, the other port is connected to the water separator and the distillation column; start stirring, and heat the reaction system to 150°C; after reacting for 30 minutes, raise the temperature to 220°C by program heating (heating rate is 5°C / min); keep the temperature for 180 minutes The transesterification reaction can be considered as finished until the amount of methanol output reaches 95wt% of the theoretical value. The by-products are mainly methanol and tetrahydrofuran, wherein the content of tetrahydrofuran is 0.01%. In addition, there are small amounts of unreacted dimethyl succinate and 1,4-butanediol. After the transesterification reaction, lower the temperature of the syst...
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