Method for extracting and separating L-isoleucine by membrane separation and plant chromatography separation
A technology of isoleucine and industrial chromatography, which is applied in the field of biochemical industry, can solve problems affecting product quality and yield, resin structure damage, and increase operating costs, etc., to achieve the reduction of ionic impurities and pigment content, yield and Effects of quality improvement and production cost reduction
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Embodiment 1
[0024] 4L of L-isoleucine fermentation broth is filtered through a microfiltration membrane with a molecular weight cut-off of 200,000 to remove bacteria. The operating pressure is 0.3MPa, the temperature is 30°C, and the volume of dialysis water is 1L. The filtrate completely removes bacteria; then it is separated by a 1L industrial chromatography column. The water consumption is 5 liters, and the temperature is 30° C. to obtain the separated isoleucine 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.
[0025] T(640nm) Volume (L) L-Isoleucine(g / L) Yield (%) fermentation broth 8.3 4.0 27.1 100 Microfiltration Membrane...
Embodiment 2
[0027] 300L of L-isoleucine 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 volume of dialysis water was 90L. The filtrate completely removed the bacteria; The water consumption was 500 liters, and the temperature was 30° C. to obtain the separated isoleucine 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.
[0028] T(640nm) Volume (L) L-Isoleucine(g / L) Yield (%) fermentation broth 9.1 300 28.9 100 Microfiltration Membrane Filtrate 75.2 334 25.7 98.9 Industria...
Embodiment 3
[0030] L-isoleucine fermentation broth 4.5M 3 The bacterial cells are removed by microfiltration with a molecular weight cut-off of 800,000. The operating pressure is 0.4 MPa, the temperature is 30°C, the dialysis water volume is 1.5 tons, and the filtrate completely removes the bacterial cells; 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 isoleucine 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.
[0031] T(640nm) Volume (M 3 ) L-Isoleucine(g / L) Yield (%) fermentation broth 9.2 4.5 28.6 100 Microfiltrat...
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