Extraction method for high purity rubusoside
An extraction method and technology of rubusoside, which is applied in the field of high-purity rubusoside extraction, can solve the problems of incomplete alcohol precipitation, prolong the filtration cycle, and high production cost, and achieve the effects of shortening the production cycle, simplifying the process and low production cost
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Embodiment 1
[0037] (1) Pre-treatment: remove impurities from 500kg of dried sweet tea raw materials (rubusaside content: 6.42%), pulverize them, and pass through a 40-mesh sieve to obtain sweet tea raw material powder;
[0038] (2) Microwave countercurrent extraction: 500kg of sweet tea raw material powder obtained in step (1) was subjected to microwave countercurrent extraction with 3295L deionized water at 90°C, microwave power 900w, and frequency 5000MHz for 60min, and the flow of material and water was reversed. Continuous dynamic flow, to get 3125kg extract;
[0039](3) Centrifugation: The 3125kg extract obtained in step (2) was rapidly cooled to 20°C through a plate-and-frame heat exchanger, and then spirally centrifuged with a horizontal spiral centrifuge at a centrifugal rate of 5000r / min, and then used a tubular type The centrifuge performs tubular centrifugation at a centrifugal rate of 14000r / min to obtain 3120kg of centrifugate;
[0040] (4) Macroporous resin adsorption separ...
Embodiment 2
[0046] (1) Pre-treatment: remove impurities from 500kg of dry sweet tea raw materials (rubusaside content is 6.45%), pulverize them, and pass through a 20-mesh sieve to obtain sweet tea raw material powder;
[0047] (2) Microwave countercurrent extraction: 500kg of sweet tea raw material powder obtained in step (1) was subjected to microwave countercurrent extraction with 3298L deionized water for 40min at 70°C, with a microwave power of 900w and a frequency of 7000MHz, and the flow of material and water was reversed. Continuous dynamic flow, to get 3133kg extract;
[0048] (3) Centrifugation: The 3133kg extract obtained in step (2) was rapidly cooled to 25°C through a plate-and-frame heat exchanger, and then spirally centrifuged with a horizontal spiral centrifuge at a centrifugal rate of 3000r / min, and then used a tubular type The centrifuge performs tubular centrifugation at a centrifugal rate of 12000r / min to obtain 3125kg of centrifugate;
[0049] (4) Macroporous resin a...
Embodiment 3
[0055] (1) Pre-treatment: remove impurities from 500kg of dried sweet tea raw materials (rubusaside content is 6.51%), pulverize them, and pass through a 30-mesh sieve to obtain sweet tea raw material powder;
[0056] (2) Microwave countercurrent extraction: 500kg of sweet tea raw material powder obtained in step (1) was subjected to microwave countercurrent extraction with 3290L deionized water for 50min at 80°C, with a microwave power of 800w and a frequency of 6000MHz, and the flow of material and water was reversed. Continuous dynamic flow, to obtain 3127kg extract;
[0057] (3) Centrifugation: The 3127kg extract obtained in step (2) was rapidly cooled to 23°C through a plate-and-frame heat exchanger, and then spirally centrifuged with a horizontal screw centrifuge at a centrifugal rate of 3000r / min, and then used a tubular type The centrifuge carries out tubular centrifugation at a centrifugal rate of 12000r / min to obtain 3122kg of centrifugate;
[0058] (4) Macroporous ...
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