A kind of extraction method of high-purity rubusoside
An extraction method and rubaside technology are applied in the extraction field of high-purity rubaside, which can solve the problems of prolonging the filtration cycle, incomplete alcohol precipitation, prolonging the production cycle, etc. Effect
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Embodiment 1
[0037] (1) Pre-treatment: remove impurities from 500 kg of dried sweet tea raw materials (the content of rubusoside is 6.42%), crush them, and pass through a 40-mesh sieve to obtain sweet tea raw material powder;
[0038] (2) Microwave countercurrent extraction: 500 kg of sweet tea raw material powder obtained in step (1) was subjected to microwave countercurrent extraction with 3295L deionized water for 60 minutes at 90°C, microwave power of 900w, and frequency of 5000MHz. The flow of material and water was Reverse continuous dynamic flow to obtain 3125 kg extract;
[0039](3) Centrifugation: The 3125 kg 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 tube Type centrifuge carries out tubular centrifugation with centrifugal speed 14000r / min, obtains 3120kg centrifugate;
[0040] (4) Macroporous resin adsorption...
Embodiment 2
[0046] (1) Pre-treatment: remove impurities from 500 kg of dried sweet tea raw materials (the content of rubusoside is 6.45%), pulverize them, and pass through a 20-mesh sieve to obtain sweet tea raw material powder;
[0047] (2) Microwave countercurrent extraction: 500 kg of sweet tea raw material powder obtained in step (1) was subjected to microwave countercurrent extraction with 3298L deionized water for 40 minutes at 70°C, microwave power of 900w, and frequency of 7000MHz. The flow of material and water was Reverse continuous dynamic flow to obtain 3133 kg extract;
[0048] (3) Centrifugation: The 3133 kg 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 tube Type centrifuge carries out tubular centrifugation with centrifugal rate 12000r / min, obtains 3125kg centrifugate;
[0049] (4) Macroporous resin adsorp...
Embodiment 3
[0055] (1) Pre-treatment: remove impurities from 500 kg of dried sweet tea raw materials (rubusiaside content is 6.51%), crush them, and pass through a 30-mesh sieve to obtain sweet tea raw material powder;
[0056] (2) Microwave countercurrent extraction: 500 kg of sweet tea raw material powder obtained in step (1) was subjected to microwave countercurrent extraction with 3290L deionized water for 50 minutes at 80°C, with a microwave power of 800w and a frequency of 6000MHz. The flow of the material and water was Reverse continuous dynamic flow to obtain 3127 kg extract;
[0057] (3) Centrifugation: The 3127 kg 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 spiral centrifuge at a centrifugal rate of 3000r / min, and then used a tube Type centrifuge carries out tubular centrifugation with centrifugal rate 12000r / min, obtains 3122kg centrifugate;
[0058] (4) Macroporous resin adso...
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