Method for refining glycolide and glycolide obtained by method
A technology of glycolide and monohydric alcohol, which is applied to a method of refining glycolide and the field of glycolide obtained therefrom, and can solve the problem of high solvent residue in refining glycolide
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Embodiment 1
[0056] Polycondensation-depolymerization preparation of crude glycolide: After adding 600g of glycolic acid crystals and 6g of stannous octoate catalyst into the reactor, the temperature was raised from room temperature to 90°C, and after the solid was completely dissolved, the temperature was raised to 120°C to start normal pressure Pre-polymerization, after 2 hours of pre-polymerization, the temperature was raised to 210°C. After the anhydrous evaporated, the system maintained the temperature and started vacuuming. The vacuum degree during this process was controlled at 3kPa. After the anhydrous evaporated, 482g of glycolic acid oligomer was obtained.
[0057] The oligomer is provided to the depolymerization reactor, and the depolymerization system is reacted at a reaction temperature of 290°C, a vacuum degree of 3kPa, and a stirring speed of 100 rpm to prepare crude glycolide, and the reaction is stopped after 2 hours to obtain batches of 1 crude glycolide 397g, acid content...
Embodiment 2
[0059] After mixing 50 g of the crude glycolide obtained in Example 1 with 40 g of n-butanol (water content not higher than 30 ppm) and 10 g of pentylene glycol dimethyl ether, the solid-liquid mixture was stirred at room temperature for 1 h, and then stopped Stir and carry out suction filtration, obtain filter cake 46g after suction filtration. The filter cake was mixed with 92g of n-butanol and heated to 80°C to form a homogeneous solution. Under the condition of rotating speed of 100rpm, cooling to room temperature at a rate of 10°C / h, glycolide is precipitated from the system, and suction filtration is performed, and the above-mentioned cooling recrystallization-filtration operation is repeated for the filter cake once, and the solid obtained by filtration is in Vacuum drying at 30°C for 8 hours gave 37.4 g of white crystals with a total yield of 74.8%. The purity of the refined glycolide measured by DSC is 99.73%, the carboxyl group content in the refined glycolide measu...
Embodiment 3
[0061] After mixing 50 g of the crude glycolide obtained in Example 1 with 40 g of n-butanol (water content not higher than 30 ppm) and 10 g of nonaethylene glycol dimethyl ether, the solid-liquid mixture was stirred at room temperature for 1 h, and then stopped Stir and carry out suction filtration, obtain filter cake 45g after suction filtration. The filter cake was mixed with 94g of n-butanol and heated to 80°C to form a homogeneous solution. Under the condition of rotating speed of 100rpm, cooling to room temperature at a rate of 10°C / h, glycolide is precipitated from the system, and suction filtration is performed, and the above-mentioned cooling recrystallization-filtration operation is repeated for the filter cake once, and the solid obtained by filtration is in Vacuum drying at 30°C for 8 hours gave 36.9 g of white crystals with a total yield of 73.8%. The purity of the refined glycolide measured by DSC is 99.82%. The carboxyl group content in the refined glycolide me...
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