Method for refining lactide
A technology of lactide and fractionation, applied in the direction of organic chemistry, can solve the problems of low lactide, high yield, difficult operation, etc.
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Embodiment 1
[0074] Embodiment 1. The influence of lactic acid impurity on polylactic acid molecular weight
[0075] The molecular weight of polylactic acid is controlled by the amount of hydroxyl impurities in lactide. Lactide with different concentrations of lactic acid and lactic acid oligomers (meq / kg) was polymerized into polylactic acid to illustrate the effect of these impurities on molecular weight. Polymerization was carried out at 180° C. using 0.1 wt. % stannous octoate as catalyst under an inert atmosphere.
[0076] Lactic acid impurity (meq / kg)
Embodiment 2
[0077] Embodiment 2. crude lactide
[0078] Low molecular weight poly(L-lactic acid) (250-300 g) was charged at room temperature into a specially designed laboratory distillation apparatus for the production of crude lactide. The apparatus consists of a 3-neck flask (500ml) with a large magnetic stirring bar and a heated oil bath (210-230°C), a vigreux column wrapped around a controlled heating tape (140-170°C), an insulating tape and a 3-flask sample Composition of the collection system. A vacuum of 30 mbar was maintained for crude lactide production and evaporation. Distilled fractions of crude lactide were collected for 1-2 hours. The solidified crude lactide fraction was retained for analysis of free acid, water and composition. The composition of the analyzed crude lactide is given in the table below together with the molecular weight of the low molecular weight polylactic acid. As can be seen from the free acid content and water content, high molecular weight polyl...
Embodiment 3
[0080] Embodiment 3. crude lactide
[0081] Crude lactide was continuously produced in a stirred tank reactor by continuous addition of low molecular weight poly(D,L-lactic acid). The vaporous crude lactide produced enters a column with a partial condenser. The column is mounted directly on the reactor. At the top of the column, after the condenser, water, lactic acid and some lactide are removed. The liquefied crude lactide fraction is removed in the lower part of the column. Analyze this fraction. The reaction mass was 26 kg and the temperature and pressure were kept constant during the process. The results of continuous crude lactide production are given in the table below.
[0082] Example
[0083] a Determined by NMR.
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