Separation purification method for natural abscisic acid
A technology for the separation and purification of natural abscisic acid, applied in the field of biofermentation-biochemical pesticide production, can solve the problems of low purification efficiency and high cost of natural abscisic acid, and achieve the effect of less product residue, simple method and high purity
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Embodiment 1
[0023] The abscisic acid fermentation liquid is filtered through the plate and frame to obtain the plate and frame filtrate, the pH is adjusted to 4.9, and the ultrafiltration membrane with a molecular weight cut off of 3000 is used to treat it to obtain an ultrafiltration dialysate, which is concentrated through a nanofiltration membrane with a molecular weight cut off of 100 , to obtain a concentrated solution, the concentrated solution is acidified and then extracted with ethyl ester, the extract is concentrated to 60 mg / ml, then dichloromethane is added, impurities are adsorbed by silica gel column chromatography, the obtained chromatographic solution is concentrated under reduced pressure, and the vacuum degree is -0.084Mpa, jacket circulating water temperature is 60°C, material temperature is 40°C, cooled and crystallized, filtered and dried to obtain abscisic acid product with a content of 96%.
Embodiment 2
[0025] The abscisic acid fermentation broth is filtered through the plate and frame to obtain the plate and frame filtrate, the pH is adjusted to 5.5, and the ultrafiltration membrane with a molecular weight cut off of 5000 is used to obtain the ultrafiltration dialysate, which is concentrated through a nanofiltration membrane with a molecular weight cut off of 150 , to obtain a concentrated solution, the concentrated solution is acidified and extracted with butyl ester, the extract is concentrated to 70mg / ml, then petroleum ether is added, impurities are adsorbed through alumina column chromatography, the obtained chromatographic solution is concentrated under reduced pressure, and the vacuum degree is -0.09Mpa, jacket circulating water temperature is 58°C, material temperature is 38°C, after concentration, add 0.8 times of hexane, cool and crystallize, filter and dry to obtain abscisic acid product with a content of 95.2%.
Embodiment 3
[0027] The abscisic acid fermentation liquid is filtered through the plate and frame to obtain the plate and frame filtrate, the pH is adjusted to 6.0, and the ultrafiltration membrane with a molecular weight cut off of 10000 is used to obtain the ultrafiltration dialysate, which is concentrated through a reverse osmosis membrane with a molecular weight cut off of 50 , to obtain a concentrated solution, the concentrated solution was acidified and extracted with isoamyl acetate, the extract was concentrated to 80 mg / ml, then chloroform was added, and impurities were adsorbed by magnesium silicate column chromatography, the obtained chromatographic solution was concentrated under reduced pressure, vacuum The temperature is -0.092Mpa, the temperature of the jacket circulating water is 45°C, and the material temperature is 30°C. During the concentration process, 0.7 times of chloroform is added, cooled and crystallized, filtered, and dried to obtain an abscisic acid product with a c...
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