Preparation method of biodegradable polybutylene succinate
The technology of polybutylene succinate and succinate is applied in the field of preparation of biodegradable polybutylene succinate, and can solve the problems of poor product color and thermal stability, low product molecular weight and side reactions. Many problems, to achieve the effect of improving the appearance and color of the product, high product yield, and increasing molecular weight
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Embodiment 1
[0029] Weigh 58.4g of dimethyl succinate, 43.2g of 1,4-butanediol, 0.01g of manganese acetate, and 0.01g of zinc acetate into a 250ml three-necked flask. Connect the water separator and the distillation column; start stirring, and heat the reaction system to 150°C; after 10 minutes of reaction, raise the temperature to 175°C in a programmed temperature rise mode (heating rate is 5°C / min); keep the temperature for 120 minutes until the output of methanol reaches 95wt% of theoretical value promptly considers that transesterification reaction finishes. The by-products are mainly methanol and tetrahydrofuran, wherein the content of tetrahydrofuran is 0.1%. 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 10°C / min) to 155°C, remove the water separator and condenser while continuing to pass nitrogen, connect the vacuum pump port, close the nitrogen chann...
Embodiment 2
[0032] Weigh 58.4g of monomethyl succinate, 50.4g of 1,4-butanediol, 0.02g of isopropyl titanate and 0.02g of magnesium acetate into a 250ml three-necked flask, one of which is stirred and the other is protected by nitrogen gas. The other port is connected to the water separator and the distillation column; start stirring, and heat the reaction system to 160°C; after 20 minutes of reaction, the temperature is raised to 185°C by means of a temperature program (heating rate of 5°C / min); keep the temperature for 120 minutes until the by-product methanol When the liquid output with water reaches 95wt% of the theoretical value, the reaction is considered to be over. The by-products are mainly methanol, water and tetrahydrofuran, wherein the content of tetrahydrofuran is 0.2%. In addition, there are small amounts of unreacted monomethyl succinate and 1,4-butanediol. Cool down the system (cooling rate 10°C / min) to 155°C, remove the water separator and condenser while continuing to p...
Embodiment 3
[0035] Weigh 58.4g of dimethyl succinate, 43.2g of 1,4-butanediol, 0.01g of isopropyl titanate and 0.02g of calcium acetate into a 250ml three-necked flask, one of which is stirred and the other is protected by nitrogen , the other port is connected to the 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 200°C by program heating (heating rate is 5°C / min); keep the temperature for 80 minutes until the methanol comes out When the liquid amount reaches 95wt% of the theoretical value, the transesterification reaction is considered to be over. The by-products are mainly methanol and tetrahydrofuran, wherein the content of tetrahydrofuran is 0.15%. 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 10°C / min) to 155°C, remove the water separator and con...
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