A method for extracting α-arbutin from fermentation broth based on membrane separation technology
A fermented liquid and arbutin technology, applied in chemical instruments and methods, organic chemistry, sugar derivatives, etc., can solve the problems of high production cost, long process route, unstable quality, etc., and achieve easy operation, simple and reasonable process , the effect of reducing production costs
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Embodiment 1
[0018] Pass 100L of α-arbutin fermentation broth through a microfiltration membrane with a membrane pore size of 1000nm, the membrane entry pressure is 0.2MPa, the membrane exit pressure is 0.1MPa, and the operating temperature is 25°C. After the fermentation broth is concentrated 8 times, 25L of dialysis water is added. The filtrate passes through the DA201 macroporous adsorption resin column at a flow rate of 2BV / H, and the analysis solution is also passed through the DA201 macroporous adsorption resin column at a flow rate of 2BV / H with 25% ethanol. The analysis solution was concentrated under reduced pressure, and decolorized by D315 macroporous adsorption resin at a flow rate of 2BV / H. The decolorization solution was concentrated twice and crystallized to obtain a total of 408.3g of α-arbutin product. The purity of the α-arbutin product detected by high pressure liquid chromatography is 99.57%.
[0019]
Embodiment 2
[0021] Pass 100L of α-arbutin fermentation broth through a microfiltration membrane with a membrane pore size of 500nm, the membrane entry pressure is 0.2MPa, the membrane exit pressure is 0.1MPa, and the operating temperature is 25°C. After the fermentation broth is concentrated 10 times, 30L of dialysis water is added. The filtrate passes through the DA201 macroporous adsorption resin column at a flow rate of 2BV / H, and the analysis solution is also passed through the DA201 macroporous adsorption resin column at a flow rate of 2BV / H with 25% ethanol. The decolorization solution was concentrated under reduced pressure, and decolorized by D315 macroporous adsorption resin at a flow rate of 2BV / H. The decolorization solution was concentrated twice and crystallized, and a total of 438.7g of α-arbutin product was obtained. The purity of the α-arbutin product detected by high-pressure liquid chromatography is 99.76%.
[0022]
Embodiment 3
[0024] Pass 100L of α-arbutin fermentation broth through a microfiltration membrane with a membrane pore size of 200nm, the membrane entry pressure is 0.2MPa, the membrane exit pressure is 0.1MPa, and the operating temperature is 25°C. After the fermentation broth is concentrated 10 times, 25L of dialysis water is added. The filtrate passes through the DA201 macroporous adsorption resin column at a flow rate of 2BV / H, and the analysis solution is also passed through the DA201 macroporous adsorption resin column at a flow rate of 2BV / H with 25% ethanol. The decolorization solution was concentrated under reduced pressure, and decolorized by D315 macroporous adsorption resin at a flow rate of 2BV / H. The decolorization solution was concentrated twice and crystallized to obtain a total of 416.4g of α-arbutin product. The purity of the α-arbutin product detected by high pressure liquid chromatography is 99.62%.
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