Method for separating and extracting L-valine from broth with high efficiency

A technology of valine and fermentation broth, which is applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., can solve the problems of incomplete decolorization of ordinary activated carbon, limited product purity, and many impurities, and achieve automatic control and clean production, environmental protection, and high economic value-added effects

Inactive Publication Date: 2013-08-07
北京轻发生物技术中心 +2
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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
Although this process improves the total extraction yield of the product, different grades of products are produced to meet the different needs of the market, and part of the waste water in the ion exchange process is recycled to reduce environmental pollution. However, the purity of the product is limited.

Method used

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  • Method for separating and extracting L-valine from broth with high efficiency

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] 1. Microfiltration treatment

[0038] Inject the L-valine fermentation broth into an organic membrane microfiltration separation system with a membrane pore size of 50-100nm, control the operating temperature to 40°C, the operating pressure to 0.6MPa, and the average membrane flux to 73L / m 2 h, after removing the bacteria and some proteins in the fermentation broth, the microfiltration permeate and bacterial protein are obtained; the microfiltration permeate is transparent and clear, without visible suspended matter, and the light transmittance is ≥ 90%. After drying, it can be used as a high-protein feed additive; among them, the yield of L-valine after microfiltration treatment is 95.0%, and the protein removal rate is 91.7%;

[0039] 2. Ultrafiltration treatment

[0040]The microfiltration permeate is injected into the organic membrane ultrafiltration separation system with a membrane pore size of 1-10nm, the operating temperature is controlled at 35°C, the operatin...

Embodiment 2

[0052] 1. Microfiltration treatment

[0053] Inject the L-valine fermentation broth into an organic membrane microfiltration separation system with a membrane pore size of 50-100nm, control the operating temperature to 30°C, the operating pressure to 0.4MPa, and the average membrane flux to 75L / m 2 h, after removing the bacteria and some proteins in the fermentation broth, the microfiltration permeate and bacterial protein are obtained; the microfiltration permeate is transparent and clear, without visible suspended matter, and the light transmittance is ≥ 90%. After drying, it can be used as a high-protein feed additive; among them, the yield of L-valine after microfiltration treatment is 93.5%, and the protein removal rate is 93.5%;

[0054] 2. Ultrafiltration treatment

[0055] The microfiltration permeate is injected into the organic membrane ultrafiltration separation system with a membrane pore size of 1-10nm, the operating temperature is controlled at 20°C, the operati...

Embodiment 3

[0067] 1. Microfiltration treatment

[0068] Inject the L-valine fermentation broth into an organic membrane microfiltration separation system with a membrane pore size of 50-100nm, control the operating temperature at 20°C, the operating pressure at 1.0MPa, and the average membrane flux at 76L / m 2 h, after removing the bacteria and some proteins in the fermentation broth, the microfiltration permeate and bacterial protein are obtained; the microfiltration permeate is transparent and clear, without visible suspended matter, and the light transmittance is ≥ 90%. After drying, it can be used as a high-protein feed additive; among them, the yield of L-valine after microfiltration treatment is 95.2%, and the protein removal rate is 91.2%;

[0069] 2. Ultrafiltration treatment

[0070] The microfiltration permeate is injected into the organic membrane ultrafiltration separation system with a membrane pore size of 1-10nm, the operating temperature is controlled at 45°C, the operati...

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Abstract

The invention discloses a method for separating and extracting L-valine from broth with high efficiency, and microfiltration for the L-valine broth, ultrafiltration, condensation and crystallization are carried out in order, and an L-valine first crude product and a crude product mother liquor are obtained, and an ion exchange treatment is carried out for the crude product mother liquor, and the L-valine in the crude product mother liquor is further recycled, and after concentration and crystallization, a L-valine second crude product is prepared. The method provided by the invention has the advantages of high overall yield and prepared L-valine with high purity, and thalline proteins separated from the extraction treatment can be used as feed additives, and the eluate in the ion exchange treatment can be used as fertilizer, thereby realizing zero discharge of the ammonium-containing waste water with environment protection, and in addition reducing production cost and improving economic benefit.

Description

technical field [0001] The invention relates to the technical field of amino acid production, in particular to a method for extracting L-valine from fermentation broth. Background technique [0002] L-Valine is one of the eight essential amino acids that humans and animals cannot synthesize themselves but must rely on external sources. Because of its special structure and function, it plays a particularly important role in human life metabolism. At present, fermentation is the main method for producing L-valine. Usually L-valine fermentation broth includes valine, various metabolic by-products, culture medium residues, bacterial cells, etc. In order to obtain pure L-valine, valine must be separated from the fermentation broth and extract it. Abroad, represented by Ajinomoto, adopts the precipitation method to extract. According to the specific combination of the precipitant and valine, a precipitate is formed, and then separated and extracted. This method has the advantage...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C229/08C07C227/40
Inventor 邱博徐庆阳万红兵欧阳宇红曹文杰江衍哲龙辉
Owner 北京轻发生物技术中心
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