Method for preparing extract of korea thistle leaf
A technology of extracts and extracts, which is applied in the field of preparation of artichoke extracts, can solve problems such as decomposition of heat-sensitive active ingredients, complex production process routes, and influence on product purity, and achieve bright color, avoid oxidation and decomposition, and short production time Effect
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Embodiment 1
[0018] Put 250g of powdered artichoke dry leaves into a 1L extraction kettle, and use CO 2 Replace and fill. Set extraction unit parameters, CO 2 Flow rate 20L / h, ethanol flow rate 0.3L / h; extractor pressure 35MPa, temperature 50°C; separator 1 pressure 8MPa, temperature 55°C, separator 2 pressure 5MPa, temperature 50°C. Continuous dynamic extraction for 2h, during which the extraction product was often collected from the outlet at the bottom of the separator. The obtained supercritical extract was evaporated at low temperature in vacuum, ethanol was removed therein, and dried to obtain 9.94 g of extract product, with an extraction rate of 3.97%.
Embodiment 2
[0020] 250g of powdery dried artichoke leaves are put into a 1L extraction kettle, and the supercritical extraction process is similar to that of Example 1. Set the parameters of the extraction device CO 2 The flow rate is 16L / h, and the ethanol flow rate is 0.3L / h; the pressure of the extractor is 30MPa, and the temperature is 50°C; the pressure of separator 1 is 7.6MPa, and the temperature is 55°C; the pressure of separator 2 is 4.6MPa, and the temperature is 50°C. Continuous dynamic extraction was performed for 3 hours, the product was collected, ethanol in the product was removed, and dried to obtain 9.60 g of extract product with an extraction rate of 3.84%.
Embodiment 3
[0022] 250g of powdery dried artichoke leaves are put into a 1L extraction kettle, and the supercritical extraction process is similar to that of Example 1. Set the parameters of the extraction device CO 2 Flow rate is 20L / h, ethanol flow rate is 0.3L / h; extractor pressure is 30MPa, temperature is 50°C; separator 1 pressure is 8.2MPa, temperature is 55°C, separator 2 pressure is 4.3MPa, temperature is 50°C. Continuous dynamic extraction was performed for 2 hours, the product was collected, ethanol in the product was removed, and dried to obtain 9.70 g of extract product with an extraction rate of 3.88%.
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