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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

Active Publication Date: 2009-08-12
WUXI JINGHAI AMINO ACID
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The general process of this process is: the fermentation broth is filtered to remove the bacteria, and the separation and extraction of L-valine from the fermentation broth using this process has the following problems: one is to use the method of filtration to remove the bacteria, because the bacteria are small, usually the bacteria The removal is not complete; the second is that the color value of the L-valine fermentation liquid is relatively high, and the decolorization of ordinary activated carbon is not complete and the amount is large, which affects the product quality and yield; the third is that there are many impurities and high content in the L-valine fermentation liquid , direct use of ion exchange method, the resin is seriously polluted, it is easy to cause the resin structure to be broken and lose the regeneration ability, which increases the operating cost. major issues
Membrane separation technology has been used in the separation and purification of fermentation products. There have been successful precedents, but there is no report on the separation and extraction of L-isoleucine from fermentation broth using membrane separation and industrial chromatographic separation technology.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

The invention relates to a method for extracting L-valine by combining membrane separation and industrial chromatography separation, belonging to the field of biochemical engineering. The method comprises the steps: (1) thalli is removed by fermentation liquor; (2) inorganic salt and other amino acids are efficiently separated by industrial chromatography; (3) impurity and pigment are removed by the fermentation liquor; (4) the fermentation liquor is concentrated and crystallized, etc. The method has the characteristics of mild reaction condition, simple and convenient operation, less separating steps, good selectivity, clean production and the like, overcomes the defects of lower yield, large sewage discharge capacity and high production intensity in the prior art, and ensures the yield and quality of the L-valine to be obviously improved.

Description

technical field [0001] The invention relates to a method for extracting and separating L-valine, in particular to a method for separating and extracting L-valine from a fermentation liquid by using a combination technology of membrane separation and industrial chromatographic separation. It belongs to the field of biochemical industry. Background technique [0002] As one of the branched-chain amino acids, L-valine is an essential amino acid for the human body and has various physiological functions. Because of its special structure and function, it occupies a particularly important position in the metabolism of human life. It is mainly used to prepare compound amino acid infusions, synthetic polypeptide drugs and food antioxidants, etc., especially in medical research and treatment, and is increasingly valued. . It is used in the treatment of blood-brain barrier, hepatic coma, chronic liver cirrhosis and renal failure, dietary treatment of congenital metabolic defects, tr...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C229/08C07C227/40B01D15/08B01D61/00
Inventor 宁健飞蔡立明
Owner WUXI JINGHAI AMINO ACID
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