Efficient separation method for preparing 23-acetyl alisol B
A high-efficiency technology of acetyl alisol, applied in the production of steroids, bulk chemicals, organic chemistry, etc., can solve the problems of complicated operation, cumbersome steps, consumption of organic solvents, etc., and achieves high efficiency, simple steps, and easy repeatability. Effect
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Embodiment 1
[0012] Embodiment 1 Alisma supercritical CO The preparation of fluid extraction solution
[0013] Weigh 3194.8g of Alisma coarse powder, particle size: 20 mesh, and put it into a 10L extraction tank. The extraction route is: CO2 steel cylinder→cooling system→high pressure pump→extraction kettle→analysis kettle I→analysis kettle II→CO 2 Storage Tank → Loop. The extraction temperature is 40°C and the extraction pressure is 35MPa for 2 hours. When the instrument reaches the set conditions, start timing and cycle the extraction for 2 hours. After the extraction was finished, the extract was released from the analysis kettle I and the analysis kettle II, a total of 127.5g, and the yield of the Alisma alisma extract prepared by the supercritical CO2 fluid extraction method was: 3.99%.
Embodiment 2
[0014] 23-Acetyl alisol B countercurrent chromatographic separation in Alisma in embodiment 2
[0015] The solvent system used is n-hexane-ethyl acetate-methanol-water=3:2:3:2, and the four solvents are arranged in a separatory funnel in proportion, fully shaken for 15 minutes (vigorously), and then stand still for 30 minutes to separate phases. After equilibration, the upper and lower phases were obtained respectively, the upper phase was used as the stationary phase, and the lower phase was used as the mobile phase, degassed by ultrasonic for 30 min, and set aside. Weigh an appropriate amount of sample and fully dissolve it in the lower phase (mobile phase), so that the sample concentration is 20mg / mL, the injection volume is 1ml, the stationary phase and the mobile phase are in a volume ratio of 70:30, and pumped into the high-speed countercurrent at a flow rate of 20mL / min. The chromatographic host spiral tube, the protection pressure is set to 1MPa. When the host spiral ...
Embodiment 3
[0016] Embodiment 3 contains the crystallization and recrystallization of 23-acetyl alisitol B component
[0017] After concentrating the collected 23-acetyl alisitol B component solution, it was analyzed by liquid chromatography that the main component of the solution was 23-acetyl alisitol B. When the solution was left at room temperature for a period of time, colorless needles were precipitated Crystallization, separation of crystallization after centrifugation, recrystallization with acetone-water or methanol-water, and vacuum drying to obtain 2 mg of high-purity 23-acetyl alisitol B monomer, which is more than 99% pure through liquid chromatography analysis The yield of 23-acetyl alisitol B after purification and drying by countercurrent chromatography is: 10%, then supercritical fluid extraction, countercurrent chromatography separation and purification, concentrated crystallization and vacuum drying process, the yield of 23-acetyl alisitol B is 0.40%.
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