Method for extracting alpha- glucosidase inhibitor from traditional Chinese cinnamomum cassia
A technology of glucosidase and inhibitor, which is applied in the fields of Chinese herbal medicine preparation and chemical and chemical industry, and achieves the effects of simple process, convenient operation and no environmental pollution
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Embodiment 1
[0013] The process and steps of α-glucosidase inhibitor extraction in the present embodiment are as follows:
[0014] (1) First, 300g of raw material Chinese medicine cinnamon is pulverized, and sieved to pass through an 80-mesh sieve; then the powder is put into supercritical CO 2 Extraction in the extraction kettle of the fluid extraction device, supercritical CO 2 The fluid flows into the extraction kettle at a flow rate of 25kg per hour, the pressure in the extraction kettle is maintained at 25MPa, and the temperature is maintained at 40°C;
[0015] (2) CO 2 The fluid enters the separation tank I and the separation tank II; the pressure of the separation tank I is 6MPa, and the temperature is 55°C; the pressure of the separation tank II is 6MPa, and the temperature is 35°C; under the above conditions, supercritical CO 2 Fluid extraction for 2 hours, finally the material left in the separation tank I and the separation tank II is a component without inhibitory activity, a...
Embodiment 2
[0018] The extraction process and steps of this embodiment are exactly the same as those of Embodiment 1 above. The steps are as follows:
[0019] (1) First, 300g of raw material Chinese medicine cinnamon is pulverized, and sieved to pass through a 60-mesh sieve; then the powder is put into supercritical CO 2 Extraction in the extraction kettle of the fluid extraction device, supercritical CO 2 The fluid flows into the extraction kettle at a flow rate of 30kg per hour, the pressure in the extraction kettle is maintained at 30MPa, and the temperature is maintained at 45°C;
[0020] (2) CO 2 The fluid enters the separation tank I and the separation tank II; the pressure of the separation tank I is 8MPa, and the temperature is 65°C; the pressure of the separation tank II is 7MPa, and the temperature is 45°C; under the above conditions, supercritical CO 2 After 3 hours of fluid extraction, the final remaining substances in the separation tank I and the separation tank II are co...
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