Process of separating and purifying natural theanine
A technology for separation and purification of theanine, which is applied in the field of separation and purification of natural theanine, can solve problems such as not being comprehensively utilized, and achieve good regeneration performance
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Embodiment 1
[0020] (1) Ultrafiltration process: After the tea polyphenol industrial waste liquid is microfiltered by 0.2μm microfiltration membrane, polysulfone ultrafiltration membrane with a molecular weight cut-off of 6KD is selected, and the operating pressure is 0.08-0.10Mpa and the temperature is 30-40℃. Perform ultrafiltration to obtain ultrafiltration permeate.
[0021] (2) Macroporous adsorption resin decolorization: Ultrafiltration permeate passes through a chromatography column equipped with D301-G macroporous adsorption resin at room temperature at 4 column bed volume / hour flow rate, and the equivalent processing capacity is 16 times the column bed. Stop loading when the volume is reached, top wash with 2 times the column bed volume of deionized water, and combine the effluent before the saturation point and the top wash to obtain a clear liquid.
[0022] (3) Cation exchange resin adsorption: replace the 001×7 resin with hydrogen form and load the column, concentrate the decoloriz...
Embodiment 2
[0028] (1) The ultrafiltration process is the same as in Example 1.
[0029] (2) Decolorization of macroporous adsorption resin: Stop loading when the processing capacity is 18 times the column bed volume, top wash with 3 times the column bed volume of deionized water, and combine the effluent before the saturation point and the top wash to obtain a clear solution. The remaining conditions are the same as in Example 1.
[0030] (3) Cation exchange resin adsorption: Concentrate the decolorized clear liquid to a theanine concentration of 2.5mg / ml, adjust the pH to 3.2 with hydrochloric acid, use a flow rate of 2.0 bed volume / hour on the column, and load 10 times the sample volume The column bed volume. The remaining conditions are the same as in Example 1.
[0031] (4) Ammonia water elution: After adsorption equilibrium, the column is washed with 3 times the bed volume of deionized water, and the flow rate is 3.0 bed volume / hour. Then eluted with a pH 11.3 aqueous ammonia solution, ...
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