Method for separating and purifying gamma-polyglutamic acid produced by corn soaking water fermentation
A technology for soaking corn in water and polyglutamic acid is applied in the field of separation engineering to achieve the effects of reducing environmental pollution, shortening extraction time and improving production efficiency
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Embodiment 1
[0032] Separation and purification: use trichloroacetic acid to acidify the fermentation broth of corn soaking water; then use centrifugation to remove bacteria and macromolecular substances; then select an ultrafiltration membrane with a pore size of 0.20 μm, and use it at a pressure of 0.1 MPa and a membrane surface flow rate of Separation was carried out at 4.0 m / s, and the pH value was controlled within the range of 6.0; finally, D318 type weakly basic anion exchange resin was selected as the separation medium, and the pH of the solution was adjusted to 4.0. =3 acetic acid to elute glutamic acid; finally, γ-polyglutamic acid was vacuum-dried to obtain 77.3g γ-polyglutamic acid.
Embodiment 2
[0034] Separation and purification: use trichloroacetic acid to acidify the fermentation broth of corn soaking water; then use centrifugation to remove bacteria and macromolecular substances; then select an ultrafiltration membrane with a pore size of 0.20 μm, and use it at a pressure of 0.15 MPa and a membrane surface flow rate of Separation is carried out at 4.5 m / s, and the pH value is controlled within the range of 6.5; finally, D318 type weakly basic anion exchange resin is selected as the separation medium, and the pH of the solution is adjusted to 4.5. =2 acetic acid to elute glutamic acid; finally, γ-polyglutamic acid was vacuum-dried to obtain 112.8.g γ-polyglutamic acid.
Embodiment 3
[0036] Separation and purification: use trichloroacetic acid to acidify the fermentation broth of corn soaking water; then use centrifugation to remove bacteria and macromolecular substances; then select an ultrafiltration membrane with a pore size of 0.20 μm, and use it at a pressure of 0.2 MPa and a membrane surface flow rate of Separation was carried out at 5.0 m / s, and the pH value was controlled within the range of 7.0; finally, D318 type weakly basic anion exchange resin was selected as the separation medium, and the pH of the solution was adjusted to 5.0, then passed through the moving bed chromatography separation column, and the adsorbed resin was separated by pH =2 acetic acid to elute glutamic acid; finally, γ-polyglutamic acid was vacuum-dried to obtain 155.1 g γ-polyglutamic acid.
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