Method for extracting and separating L-valine from fermentation liquor by employing membrane separation and electroosmosis combined technology

A technology of fermented liquid and valine, which is applied in the field of extraction and separation of L-valine, which can solve the problems of incomplete decolorization of activated carbon, broken resin structure, and increased number of resin regeneration, so as to reduce the decolorization process of activated carbon and impurities and the effects of pigment content reduction, yield and quality improvement

Inactive Publication Date: 2012-10-24
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: filter the fermentation broth to remove bacteria, and ion exchange to separate amino acids through the process of adsorption and elution. Using this process to separate and extract L-valine from the fermentation broth has the following problems: one is to use filtration to remove bacteria Because the bacteria are small, usually the bacteria are not completely removed; 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 dosage is large, which affects the product quality and yield; the third is L-valine There are many impurities and high content in the acid fermentation liquid, and the direct ion exchange method will cause serious resin pollution, which will easily cause the resin structure to be broken and lose its regeneration ability, which will increase the operating cost. At the same time, the high content of ionic substances will quickly saturate the resin , increase the number of resin regeneration, resulting in a large amount of sewage discharge and other problems
Membrane separation technology has been used in the separation and purification of fermentation products. There have been successful precedents, but the use of membrane separation and electrodialysis combined technology to separate and extract L-valine from fermentation broth has not been reported.

Method used

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  • Method for extracting and separating L-valine from fermentation liquor by employing membrane separation and electroosmosis combined technology

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] 4.2L of L-valine fermentation broth was filtered through ultrafiltration 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 amount of dialysis water was 1L. The filtrate completely removed the bacteria. Then, through a 6L combined electrodialysis membrane equipment at a temperature of 30°C, L-valine demineralized clear liquid was obtained. The demineralized clear liquid is filtered through a nanofiltration membrane with a molecular weight cut-off of 500 to remove impurities such as small molecular proteins and pigments. The operating pressure is 1.2MPa, the temperature is 30°C, and the dialysis water volume is 3.2L, and then pre-concentrated by RO reverse osmosis membrane. The results are shown in the table below:

[0031] Electrodialysis electrically driven membrane separator: the conductivity of the original solution: 33200μS / cm

[0032] Conductivity of demineralized clear liquid: 10...

Embodiment 2

[0037] The 330L L-valine fermentation broth was filtered through an ultrafiltration membrane with a molecular weight cut-off of 800,000 to remove the bacteria. The operating pressure was 0.35MPa, the temperature was 30°C, and the dialysis water volume was 100L. The filtrate completely removed the bacteria. Then through a 500L combined electrodialysis membrane equipment at a temperature of 30°C, a demineralized L-valine clear liquid is obtained. The demineralized clear liquid is filtered through a nanofiltration membrane with a molecular weight cutoff of 500 to remove impurities such as small molecular proteins and pigments. The operating pressure is 1.2MPa, the temperature is 30°C, and the dialysis water volume is 245L, and then pre-concentrated through the RO reverse osmosis membrane. The results are shown in the table below:

[0038] Electrodialysis electrically driven membrane separator: the conductivity of the original solution: 34200μS / cm

[0039] Conductivity of demineralize...

Embodiment 3

[0044] L-valine fermentation broth 4.6M 3 The bacteria are removed by ultrafiltration membrane with a molecular weight cut-off of 800,000. The operating pressure is 0.4MPa, the temperature is 30°C, and the dialysis water volume is 1.5 M. 3 . The filtrate completely removes the bacteria, and then passes 8M 3 The combined electrodialysis membrane equipment, the temperature is 30 ℃, to obtain the demineralized L-valine clear liquid. The demineralized clear liquid is filtered through a nanofiltration membrane with a molecular weight cut-off of 1000 to remove impurities such as small molecular proteins and pigments. The operating pressure is 1.2MPa, the temperature is 30°C, and the dialysis water volume is 3.6 M. 3 , And then pre-concentrated through RO reverse osmosis membrane. The results are shown in the table below:

[0045] Electrodialysis electrically driven membrane separator: the conductivity of the original solution: 33400μS / cm

[0046] Conductivity of demineralized clear liqu...

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Abstract

The invention discloses a method for extracting and separating L-valine from fermentation liquor by employing membrane separation and electroosmosis combined technology and belongs to the technical field of biochemical engineering. The method comprises the steps of (1) removing thallus from fermentation liquor; (2) carrying out electroosmosis to clear fermentation liquor to remove inorganic salt; (3) removing small-molecule protein and pigment impurities form clear desalted liquid; (4) carrying out preconcentration to the fermentation liquor with reverse osmosis membrance, and (5) concentrating and crystallizing the fermentation liquor. The method disclosed by the invention has the characteristics that the condition is mild, the operation is simple, the separation steps are less and the selectivity is good; the defects of low yield, large sewage discharge and high production intensity of the existing ion exchange technology are overcome, and the yield and quality of the L-valine are significantly 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 inorganic salts from L-valine fermentation broth using a combination of membrane separation and electrodialysis technology, and belongs to the technical 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 a variety of physiological functions. Because of its special structure and function, it occupies a particularly important position in human life metabolism. It is mainly used to formulate compound amino acid infusion, synthetic peptide drugs and food antioxidants, etc., especially its role in medical research and treatment, which has attracted increasing attention . It is used in the treatment of blood-brain barrier, hepatic coma, chronic liver cirrhosis and renal failure, dietary treatment of congenital metabolic...

Claims

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Application Information

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