Method for preparing polylactic acid from lactic acid under catalysis of titanium composite catalyst
A technology of catalyst catalyzing lactic acid and composite catalyst, applied in the field of polymer materials, can solve problems such as limitations and less research, and achieve the effects of short reaction time, simple production equipment, and broad market application prospects
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Embodiment 1
[0032] Add about 20g of lactic acid prepolymer into a 250ml three-necked flask equipped with a stirrer and a condenser tube, vacuumize and replace nitrogen for 3 to 4 times, and add tetraisopropoxytitanium and p-toluenesulfonate under the protection of nitrogen A mixture catalyst of acid (the input amount of tetraisopropoxytitanium is 0.4% of the mass of lactic acid prepolymer, and the molar ratio of tetraisopropoxytitanium to p-toluenesulfonic acid is 1:4), put the system into In an oil bath at 100°C, the system is stirred with a German IKA EUROSTAR power control visc stirrer. After the catalyst in the system is fully dissolved, the temperature is rapidly raised to 180°C and the decompression reaction is started at the same time. The vacuum degree is controlled at 30-80Pa, and the stirring speed is controlled at 400~450r / min, the polymerization reaction stops after about 25h, the product is dissolved in chloroform, precipitated in anhydrous methanol, centrifuged, the supernata...
Embodiment 2
[0034] Add about 20g of lactic acid prepolymer into a 250ml three-necked flask equipped with a stirrer and a condenser tube, vacuumize and replace nitrogen for 3 to 4 times, and add titanium tetrachloride and p-toluenesulfonic acid under the protection of nitrogen. Mixture catalyst (the input amount of titanium tetrachloride is 0.4% of the mass of lactic acid prepolymer, the molar ratio of titanium tetrachloride and p-toluenesulfonic acid is 1:4), put the system into an oil bath at 100°C , the system is stirred with a German IKA EUROSTAR power control visc stirrer. After the catalyst in the system is fully dissolved, the temperature is rapidly raised to 180°C and the decompression reaction is started at the same time. The vacuum degree is controlled at 30-80Pa, and the stirring speed is controlled at 400-450r / min. The polymerization reaction stopped after about 25 hours. The product was dissolved in chloroform, precipitated in anhydrous methanol, centrifuged, the supernatant wa...
Embodiment 3
[0036] Add about 20g of lactic acid prepolymer into a 250ml three-necked flask equipped with a stirrer and a condenser tube, vacuumize and replace nitrogen for 3 to 4 times, and add tetraisopropoxytitanium and p-toluenesulfonate under the protection of nitrogen A mixture catalyst of acid (the input amount of titanium tetraisopropoxide is 0.4% of the mass of lactic acid prepolymer, and the molar ratio of titanium tetraisopropoxide and p-toluenesulfonic acid is 1:1), put the system into In an oil bath at 100°C, the system is stirred with a German IKA EUROSTAR power control visc stirrer. After the catalyst in the system is fully dissolved, the temperature is rapidly raised to 180°C and the decompression reaction is started at the same time. The vacuum degree is controlled at 30-80Pa, and the stirring speed is controlled at 400~450r / min, the polymerization reaction stops after about 25h, the product is dissolved in chloroform, precipitated in anhydrous methanol, centrifuged, the su...
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