A processing method for continuous purification of tea saponin
A processing method and technology for tea saponin, which are applied in the processing field of continuous purification of tea saponin, can solve the problems such as adverse effects on the health of solvent producers and the environment, long adsorption time and elution time of packed columns, and inability to achieve airtightness during the purification process. , to achieve the effect of expanding the scope of use, improving market competitiveness and low cost
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Embodiment 1
[0017] Example 1: finely filter the extracted tea saponin solution, and adjust the temperature of the solution to 50°C, the impurity content of the filtrate after filtration is not more than 0.05%; the finely filtered tea saponin solution has a permeable molecular weight of 10000 The membrane is used for fine filtration and coarse separation, and the feed pressure is 1.2MPa; the permeate of the coarse separation enters the membrane with a permeable molecular weight of 5000 for the first step of separation and purification, and the feed pressure is 1.2MPa; the permeate of the first step is purified and enters the permeable The second step of purification is performed through a membrane with a molecular weight of 3000, and the feed pressure is 1.5Mpa; the permeate that passes through the membrane with a molecular weight of 3000 enters a membrane with a permeable molecular weight of 400 for nanofiltration, and the feed pressure is 1.5Mpa; After the nanofiltration retentate is drie...
Embodiment 2
[0018] Example 2: finely filter the extracted tea saponin solution, and adjust the temperature of the solution to 56°C, the impurity content of the filtrate after filtration is not more than 0.05%; the finely filtered tea saponin solution has a permeable molecular weight of 10000 The membrane is used for fine filtration and coarse separation, and the feed pressure is 1.5MPa; the permeate of the coarse separation enters the membrane with a permeable molecular weight of 5000 for the first step of separation and purification, and the feed pressure is 1.5MPa; the permeate of the first step is purified and enters the permeable The second step of purification is performed through a membrane with a molecular weight of 3000, and the feed pressure is 1.8Mpa; the permeate that passes through the membrane with a molecular weight of 3000 enters a membrane with a permeable molecular weight of 400 for nanofiltration, and the feed pressure is 2.0Mpa; After the nanofiltration retentate is drie...
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