Method for extracting and separating 24-dehydrocholesterol and cholesterol by ionic liquid
A dehydrocholesterol and ionic liquid technology, applied in the production of steroids, bulk chemicals, organic chemistry, etc., can solve problems such as low separation selectivity and extraction capacity, environmental pollution caused by volatile organic solvents, and environmental pollution , to achieve the effect of reducing the theoretical plate number of fractionation and solvent consumption, reducing equipment investment and production cycle, and reducing pollution
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Embodiment 1
[0035] The mixture of raw material 24-dehydrocholesterol and cholesterol (24-dehydrocholesterol / cholesterol = 13.64%, mass ratio) is dissolved in petroleum ether with a boiling range of 60-90°C to prepare the total concentration of 24-dehydrocholesterol and cholesterol It is 0.9 g / L raw material solution. Using 1-butylcyano-3-methylimidazole-tetrafluoroborate ionic liquid as extractant, petroleum ether with a boiling range of 60-90°C as detergent, extraction agent, detergent and raw material solution The flow ratio is 6:4.5:1.5 (that is, 4:3:1), and the fractional extraction is carried out at 50°C. There are 3 stages in the extraction section and 6 stages in the washing section, and the extract and raffinate are collected.
[0036] The raffinate was concentrated in vacuo, washed with water and dried to obtain cholesterol; the extract was back-extracted with n-hexane, and the extracted phase of n-hexane was concentrated in vacuo, washed with water and dried to obtain 24-dehydro...
Embodiment 2
[0038] The mixture of raw materials 24-dehydrocholesterol and cholesterol (24-dehydrocholesterol / cholesterol=13.64%, mass ratio) is dissolved in n-hexane to prepare a raw material solution with a total concentration of 24-dehydrocholesterol and cholesterol of 1.8 g / L . 1-sulfonepropyl-quinoline-bistrifluoromethanesulfonimide salt ionic liquid is used as the extractant, n-hexane is used as the detergent, and the flow ratio of the extractant, detergent, and raw material solution is 4:3: 1. Fractional extraction is carried out at 60°C. There are 2 stages in the extraction section and 6 stages in the washing section, and the extract and raffinate are collected.
[0039] The raffinate was concentrated in vacuo, washed with water and dried to obtain cholesterol; the extract was back-extracted with n-hexane, and the extracted phase of n-hexane was concentrated in vacuo, washed with water and dried to obtain 24-dehydrocholesterol. Among them, the purity of 24-dehydrocholesterol was 9...
Embodiment 3
[0041] The mixture of raw material 24-dehydrocholesterol and cholesterol (24-dehydrocholesterol / cholesterol = 11.26%, mass ratio) is dissolved in octane to prepare a raw material solution with a total concentration of 24-dehydrocholesterol and cholesterol of 0.5 g / L . The benzimidazole-tetracyanoboric acid ionic liquid-methanol binary mixed solvent is used as the extractant (the molar fraction of benzimidazole-tetracyanoboric acid in the mixed solvent is 90%), and octane is used as the detergent. The extractant, detergent, The flow ratio of the three raw materials is 2:1:1, and the fractional extraction is carried out at 40°C. There are 3 stages in the extraction section and 7 stages in the washing section, and the extract and raffinate are collected.
[0042] The raffinate was concentrated in vacuo, washed with water and dried to obtain cholesterol; the extract was back-extracted with n-hexane, and the extracted phase of n-hexane was concentrated in vacuo, washed with water a...
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