Method of extracting stevioside from stevia rebaudiana bertoni by simulated moving bed chromatography (SMBC) method
A technology of simulating moving bed and steviol glycosides, which is applied in the field of purification of natural plant effective components, can solve the problems of large amount of resin and mobile phase, long resin regeneration cycle, and reduced product yield, so as to reduce energy consumption and purification cost, water consumption reduction effect
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Embodiment 1
[0044] A method for extracting steviol glycosides from stevia by simulated moving bed chromatography. The specific separation process is as follows:
[0045] 1) Percolation extraction: pulverize stevia leaves, with a particle size of less than 2mm accounting for 60-90%, and put 500g of powder into a percolation container, with a leachate outlet under the percolator, and a small filter screen at the leachate outlet Or filter cloth or cotton prevents the powder from flowing out, the height of the powder is 20cm, at room temperature, with 3.5L water diafiltration leaching, the turbid liquid can be returned to the diafiltration container for re-diafiltration, this process does not require coarse filtration to directly obtain a clarified leachate ;
[0046] 2) Removal of impurities by column chromatography: The stationary phase of column chromatography is AB-8, and the specifications of the chromatography column are: diameter 50mm, length 300mm, and the sample volume of the extract is 0...
Embodiment 2
[0060] Except for the following SMB separation conditions, other conditions and steps are the same as in Example 1.
[0061] SMB separation conditions:
[0062] Flow rate of mobile phase: in the refining zone and adsorption zone, the flow rate of eluent D is Q D 6.3BV per hour, flow rate Q of injection fluid F F 0.76BV per hour, flow rate Q of raffinate R R =Q D +Q F ; In the elution zone, the eluent P flow rate Q p 6.3BV per hour, flow rate Q of extract E E =Q p ; Switching time T S : 17min;
[0063] The crude steviol glycoside product obtained by distilling and thickening the steviol glycoside extract has a yield of 12.2%, and the purity of RA is 68%.
Embodiment 3
[0065] Except for the following SMB separation conditions, other conditions and steps are the same as in Example 1.
[0066] SMB separation conditions:
[0067] Flow rate of mobile phase D: In the refining zone and adsorption zone, the flow rate of eluent D is Q D 4.6BV per hour, flow rate Q of injection fluid F F 3.8BV per hour, flow rate Q of raffinate R R =Q D +Q F ; In the elution zone, the eluent P flow rate Q p 4.6BV per hour, flow rate Q of extract E E =Q p ; Switching time T S : 15.5min;
[0068] The crude steviol glycoside product obtained by distilling and thickening the steviol glycoside extract has a yield of 9.7%, and the purity of RA is 67%.
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