Method for extracting and separating L-valine by membrane separation and plant chromatography separation
A technology of industrial chromatography and valine, applied in the field of biochemical industry, can solve problems such as affecting product quality and yield, breaking the resin structure, increasing operating costs, etc., and achieves reduction of ionic impurities and pigment content, yield and quality The effect of improving and reducing production costs
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Embodiment 1
[0025] 4L of L-valine fermentation broth was filtered through a microfiltration membrane with a molecular weight cut-off of 200,000 to remove bacteria, the operating pressure was 0.3MPa, the temperature was 30°C, and the volume of dialysis water was 1L. The filtrate completely removes the bacterial cells; then it is separated by a 1L industrial chromatographic column, with a water consumption of 5 liters and a temperature of 30°C to obtain the separated valine supernatant. The separated supernatant was filtered through a sodium filter membrane with a molecular weight cut-off of 500 to remove small molecular impurities and pigments. The operating pressure was 1.2MPa, the temperature was 30°C, the dialyzed water volume was 1.5L, and then it was pre-concentrated through RO reverse osmosis membrane. The results are shown in the table below.
[0026] T(640nm) Volume (L) L-valine (g / L) Yield (%) fermentation broth 8.3 4.0 41.1 100 Ultrafiltration membr...
Embodiment 2
[0028] 300L of L-valine fermentation broth was filtered through a microfiltration membrane with a molecular weight cut-off of 800,000 to remove bacteria. The operating pressure was 0.35MPa, the temperature was 30°C, and the dialyzed water volume was 90L. The filtrate completely removes the bacteria; then it is separated by an 80L industrial chromatographic column, with a water consumption of 500 liters and a temperature of 30°C to obtain the separated valine clear liquid. The separated supernatant was filtered through a sodium filter membrane with a molecular weight cut-off of 500 to remove small molecular impurities and pigments. The operating pressure was 1.2MPa, the temperature was 30°C, the dialyzed water volume was 1.5L, and then it was pre-concentrated through RO reverse osmosis membrane. The results are shown in the table below.
[0029] T(640nm) Volume (L) L-valine (g / L) Yield (%) fermentation broth 9.1 300 42.9 100 Ultrafiltration membra...
Embodiment 3
[0031] L-valine fermentation broth 4.5M 3 Bacteria are removed by microfiltration with a molecular weight cut-off of 800,000. The operating pressure is 0.4MPa, the temperature is 30°C, and the volume of dialysis water is 1.5 tons. The filtrate completely removes the bacteria; then it is separated by an 80L industrial chromatographic column, with a water consumption of 7 tons and a temperature of 30°C to obtain the separated valine supernatant. The separated supernatant was filtered through a sodium filter membrane with a molecular weight cut-off of 1000 to remove small molecular impurities and pigments. The operating pressure was 1.2MPa, the temperature was 30°C, the volume of dialysis water was 1.5L, and then it was pre-concentrated through RO reverse osmosis membrane. The results are shown in the table below.
[0032] T(640nm) Volume (M 3 ) L-valine (g / L) Yield (%) fermentation broth 9.2 4.5 42.5 100 Ultrafiltration membrane filtrate 75.1 5...
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