Method for purifying vitamin A isomer in vitamin A mother liquor
A purification method and vitamin technology, applied in liquid solution solvent extraction, organic chemistry, etc., can solve the problems of difficult separation, high price of organic solvents, high toxicity, etc., and achieve the effect of high purity, cheap and easy-to-obtain solvents, and low toxicity
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Embodiment 1
[0040] The highly polar solvent in this embodiment is all methanol, and the low polar solvent is all ether, according to figure 1 As shown in the flow process, 1000g of VA crude mother liquor (the sum of the total trans VA and 13 cis VA content is 45.12%) is dissolved in 500mL of low polarity solvent solution, and the formed material 1 enters from the middle of the normal extraction tower evenly within 4h In the normal extraction tower, the extraction agent 3 is a highly polar solvent, which enters the normal extraction tower from the top inlet of the normal extraction tower, and the low polarity solvent enters the normal extraction tower from the bottom inlet of the normal extraction tower. The polar solvent is full, and the high polar solvent is controlled: the volume ratio of material 1: low polar solvent is 20:1:4, and the temperature of the normal extraction tower is -10°C. After the extraction is completed, the heavy component phase 5 is decompressed under reduced pressur...
Embodiment 2
[0043] The highly polar solvent is acetonitrile, the low polar solvent petroleum ether, the temperature of the normal extraction tower is 20°C, and the other conditions are the same as in Example 1. After the extraction is completed, the light component phase 10 is removed under reduced pressure from the low polar solvent , to obtain 507.45g of stripping essence, content 81.35%, molar yield 91.49%.
Embodiment 3
[0045] The highly polar solvent is 10% (v / v) aqueous methanol, the low polar solvent toluene, and the temperature of the positive extraction tower is 50° C., and the others are the same as in Example 1. After the extraction is completed, the phase containing light components 10 is under reduced pressure. The low-polarity solvent was removed to obtain 520.05 g of the back-extracted fine product, with a content of 82.35% and a molar yield of 97.16%.
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