A kind of extraction, separation and purification method of γ-aminobutyric acid
A technology for the separation and purification of aminobutyric acid, applied in the field of separation and purification, can solve the problems of impractical production and use, high cost, low yield of γ-aminobutyric acid, etc., and achieve easy promotion and use, easy preparation process, and purification method Effects in simple steps
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Embodiment 1
[0017] (1) Crush the rice, add 40wt% ethanol aqueous solution for extraction after smashing, the extraction temperature is 50°C, the ratio of solid to liquid is 1:7, the extraction time is 3h, and the extract is centrifuged after extraction , the centrifugal speed is 4000rpm, and the supernatant is taken;
[0018] (2) Concentrate the supernatant to twice the weight of the original rice, adjust the pH of the supernatant to 4.5 after concentration, pass through the activated 732 cation exchange resin, the sample loading flow rate is 1BV / h, and the resin column diameter to height ratio is 8:1;
[0019] (3) After the sample loading, the 732 cation exchange resin was eluted with ammonia water with a concentration of 0.03mol / L at a flow rate of 0.5BV / h. After elution, the eluate was collected and concentrated. After concentration, no solvent remains, and then purify the concentrate with ethanol. The purification temperature is at room temperature. The weight ratio of ethanol to the...
Embodiment 2
[0022] (1) Crush the rice, add 30wt% ethanol aqueous solution for extraction after smashing, the extraction temperature is 45°C, the ratio of solid to liquid is 1:6, the extraction time is 3h, and the extract is centrifuged after extraction , the centrifugal speed is 4000rpm, and the supernatant is taken;
[0023] (2) Concentrate the supernatant to twice the weight of the original rice, adjust the pH of the supernatant to 5 after concentration, pass through the activated 732 cation exchange resin, the sample loading flow rate is 2BV / h, and the diameter-to-height ratio of the resin column is 8:1;
[0024] (3) After loading the sample, use ammonia water with a concentration of 0.02mol / L to elute the 732 cation exchange resin at a flow rate of 1BV / h, collect the eluate after elution, concentrate the eluate, and concentrate Finally, no solvent remains, and then purify the concentrate with ethanol, the purification temperature is room temperature, and the weight ratio of ethanol t...
Embodiment 3
[0027] (1) Crush the rice, add 50wt% ethanol aqueous solution for extraction after smashing, the extraction temperature is 55°C, the ratio of solid to liquid is 1:8, the extraction time is 3h, and the extract is centrifuged after extraction , the centrifugal speed is 4000rpm, and the supernatant is taken;
[0028] (2) Concentrate the supernatant to twice the weight of the original rice, adjust the pH of the supernatant to 4 after concentration, pass through the activated 732 cation exchange resin, the sample loading flow rate is 1.5BV / h, and the diameter of the resin column is high The ratio is 8:1;
[0029] (3) After loading the sample, the 732 cation exchange resin was eluted with ammonia water with a concentration of 0.04mol / L at a flow rate of 1.5BV / h. After elution, the eluate was collected and concentrated. After concentration, no solvent remains, and then purify the concentrate with ethanol. The purification temperature is at room temperature. The weight ratio of ethan...
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