Method for separating and purifying aucubin from leaves of eucommia ulmoides oliv with NKA-2 macroporous adsorption resin
A technology of aucubin and NKA-2, which is applied in the field of green chemical technology, can solve the problems of high equipment cost, low purity and yield, and difficult separation, and achieve operation and product safety, advanced technology, and environmental friendliness Effect
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Embodiment 1
[0021] The cleaned NKA-2 macroporous adsorption resin was selected as the separation and purification resin of Eucommia aucubin, and the above-mentioned crude extract of aucubin was prepared with 60% volume concentration and neutral pH value of edible ethanol to a concentration of 0.3 mg / mL solution. 3.0 BV of the solution is passed through a separation column equipped with NKA-2 macroporous adsorption resin at a flow rate of 3.0 BV / h for adsorption and separation. After the adsorption is saturated, it is washed with 2 BV of distilled water at a flow rate of 1.5 BV / h until it is colorless. Then use 2.0BV of edible ethanol with a volume concentration of 50% to elute aucubin at a flow rate of 3.0BV / h, collect the eluate, concentrate the eluate at -0.07MPa, 50°C, and recover edible ethanol , vacuum freeze-drying to obtain purified aucubin extract, the measured yield of aucubin was 82.02%, and the purity was 50.37%.
Embodiment 2
[0023] The cleaned NKA-2 macroporous adsorption resin was selected as the separation and purification resin of Eucommia aucubin, and the above-mentioned crude extract of aucubin was prepared with 50% volume concentration and neutral pH value of edible ethanol to a concentration 0.2 mg / mL solution. Pass 2.5 BV of the solution through a separation column equipped with NKA-2 macroporous adsorption resin at a flow rate of 2.0 BV / h for adsorption and separation. After the adsorption is saturated, first wash it with 1 BV of distilled water until colorless at a flow rate of 1 BV / h. Then use 1.5 BV of edible ethanol with a volume concentration of 40% to elute aucubin at a flow rate of 2.0BV / h, collect the eluate, concentrate the eluate at -0.05MPa, 45°C, and recover edible ethanol , freeze-dried in vacuum to obtain purified aucubin extract, the measured yield of aucubin was 77.11%, and the purity was 49.3%.
Embodiment 3
[0025] The cleaned NKA-2 macroporous adsorption resin was selected as the separation and purification resin of Eucommia aucubin, and the above-mentioned crude extract of aucubin was prepared with 70% volume concentration and neutral pH value of edible ethanol to a concentration of 0.4 mg / mL solution. Pass 3.5 BV of the solution through a separation column equipped with NKA-2 macroporous adsorption resin at a flow rate of 4.0 BV / h for adsorption and separation. After the adsorption is saturated, first wash it with 3 BV of distilled water at a flow rate of 2 BV / h until it is colorless. Then use 2.5 BV of edible ethanol with a volume concentration of 60% to elute aucubin at a flow rate of 4.0 BV / h, collect the eluate, concentrate the eluate at -0.09MPa, 55°C, and recover edible ethanol , vacuum freeze-drying to obtain purified aucubin extract, the measured yield of aucubin was 78.06%, and the purity was 48.73%.
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