Lactide separation and purification method
A purification method and technology of lactide, applied in the direction of organic chemistry, etc., can solve the problems of complex equipment, cumbersome operation, and high cost
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Embodiment 1
[0063] Use as attached figure 1 The shown separation and purification process takes L-lactide as the main product.
[0064] Step 1: Crystallization process. Use as attached Figure 6 The suspended crystallizer shown has a diameter of 270mm and a height of 3m, and is equipped with 7-stage push-up propellers. The crude lactide prepared in the reaction process is used for melt crystallization. Calculated based on the total flow rate of the crude lactide stream, the total residence time is 4 hours, where the temperature of the hot oil in the heating zone is 98°C, and the temperature of the cooling medium in the cooling zone is 70°C.
[0065] The relevant results are shown in the table below, where L-LD stands for L-lactide, m-LD stands for m-lactide, D-LD stands for D-lactide, and LA stands for lactic acid.
[0066]
Embodiment 2
[0068] Use as attached figure 1 The shown separation and purification process takes L-lactide as the main product.
[0069] Step 1: The crystallization process adopts the attached Figure 6 In the suspension crystallizer shown, the crude lactide prepared in the reaction process is used for melt crystallization. Calculated based on the total flow rate of the crude lactide stream, the total residence time is 2.5h, and the temperature of the hot oil in the heating area is 120°C. The temperature of the regional cooling medium is 50°C.
[0070] The relevant results are shown in the table below.
[0071]
[0072] Analysis of the results of Examples 1 and 2: After crystallization and purification, m-lactide, lactic acid, and oligomers in the crude lactide all decreased significantly.
Embodiment 3
[0074] Use as attached figure 1 The shown process is a separation process with L-lactide as the main product.
[0075] Steps 2 and 3: Rectification process. The rectification column is filled with 3 sections of Pro-Pak Bulletin-fillers from American POPE Company, each with a height of 50cm, and the feeding position is between the first and second packings from top to bottom, and the target product is extracted from the side line, and the extraction position is From top to bottom between the second and third sections of packing.
[0076] L-LD / % m-LD / % D-LD / % LA / % Oligomer / % Optical purity / % starting material 89.4 5.6 0.4 2.8 1.85 93.7
[0077] The operating conditions of the rectifying tower are as follows:
[0078] Oil bath / ℃ Kettle temperature / ℃ Top temperature / ℃ Reflux ratio Pressure PaA stream a rectification column 135 120 104 4:1 500 Stream b rectification column 165 150 120 4:1 500
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