Synthesis of polylactate in supercrilical fluid of CO2
A polylactic acid and supercritical technology, applied in the production of bulk chemicals, can solve the problems of heavy secondary pollution, high polymerization temperature and large side reactions, and achieve the effect of saving resources
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Embodiment 1
[0035] A. Clean and dry the reactor, and pass through CO dried through 3 Å molecular sieves. 2 gas;
[0036] B. adding concentration is 0.25mol / L L-lactide, catalyst stannous isooctanoate and co-solvent, wherein the molar ratio of L-lactide and stannous isooctanoate is 1000:1, the molar ratio of co-solvent and L-lactide The ratio is 0:1;
[0037] C. Seal the reactor and heat it until the temperature reaches 85°C, and control the pressure in the reactor to 25Mpa;
[0038] D. Start the stirrer and react for 24 hours;
[0039] E. Pass cooling water, and control the temperature at 40°C, continue to stir, pass dry CO 2 Gas, flow control at 1000ml / hour, pressure at 20Mpa, supercritical extraction for 6 hours;
[0040] F. Through cooling water, the reaction kettle is lowered to room temperature, and the pressure is reduced to normal pressure, and the product is taken out, which is polylactic acid.
[0041] The weight average molecular weight of the product M w It is 43000, and ...
Embodiment 2
[0043] The concentration of L-lactide is 0.5mol / L, all the other conditions are with embodiment 1, obtain white powder product after the polymerization reaction, M wis 75000 and the PDI is 2.04.
Embodiment 3
[0045] The consumption of catalyzer is 1 / 500 of lactide, all the other conditions are with embodiment 1, obtain polylactic acid after polymerization reaction, M w is 74000 and the PDI is 2.16.
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