Method for purifying stilbene glucoside in Lysimachia clethroide duby
A stilbene glycoside and loosestrife technology, applied in chemical instruments and methods, preparation of sugar derivatives, sugar derivatives, etc., can solve the problems of poor stability, difficult synthesis, complex structure of stilbene glycosides, etc.
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Embodiment 1
[0012] Take 1 kg of pearl vegetable medicinal material, crush it into coarse powder, moisten it with 2000ml 60% ethanol; put it into a percolator; use 10000ml 60% ethanol for percolation, collect the percolation liquid; recover ethanol under reduced pressure, concentrate to 1200ml, and use 2400ml Ether extraction, a total of 3 extractions, to remove fat-soluble impurities; take the water layer, add 4000ml deionized water to dilute, centrifuge (3000 rpm) for 10 minutes, and the supernatant is passed through D-101 at a flow rate of 1L / (kg h). Pore adsorption resin (column diameter-column height=1:10, the weight of the resin is 2 times the weight of the medicinal material), use deionized water 3 times the volume of the resin to remove impurities at a flow rate of 1L / (kg h), discard, and then Use 30% ethanol that is 5 times the volume of the resin to remove impurities at a flow rate of 0.8L / (kg h), and finally use 40% ethanol that is 6 times the volume of the resin to desorb at a...
Embodiment 2
[0014] Take 5kg of loosestrife medicinal material, crush it into coarse powder, wet it with 10L 70% ethanol; put it into a percolator; use 70L 70% ethanol for percolation, collect the percolation liquid; recover ethanol under reduced pressure, concentrate to 5L, and use 10L Ether extraction, a total of 3 extractions, to remove fat-soluble impurities; take the water layer, add 10L deionized water to dilute, centrifuge (3000 rpm) for 10 minutes, and supernatant flow through D-101 at a flow rate of 1L / (kg h). Pore adsorption resin (column diameter-column height=1:10, the weight of the resin is 2 times the weight of the medicinal material), use deionized water 3 times the volume of the resin to remove impurities at a flow rate of 1L / (kg h), discard, and then Use 30% ethanol that is 4 times the volume of the resin to remove impurities at a flow rate of 0.8 L / (kg h), and finally use 40% ethanol that is 5 times the volume of the resin to desorb at a flow rate of 0.8 L / (kg h), and co...
Embodiment 3
[0016] Take 10kg of pearl vegetable medicinal material, crush it into coarse powder, moisten it with 15L 60% ethanol; put it into a percolator; use 100L 60% ethanol for percolation, collect the percolation liquid; recover ethanol under reduced pressure, concentrate to 8L, and use 2000ml Ether extraction, a total of 3 extractions, to remove fat-soluble impurities; take the water layer, add 30L deionized water to dilute, centrifuge (3000 rpm) for 10 minutes, and the supernatant is passed through D-101 at a flow rate of 1.2L / (kg h) Macroporous adsorption resin (column diameter-column height=1:8, the weight of the resin is 2 times the weight of the medicinal material), deionized water twice the volume of the resin is used to remove impurities at a flow rate of 1L / (kg h), discarded, Then use 30% ethanol that is 4 times the volume of the resin to remove impurities at a flow rate of 1 L / (kg h), and finally use 40% ethanol that is 6 times the volume of the resin to desorb with a flow r...
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