Separation and purification process for producing branched chain amino acid by using fermentation method

A branched-chain amino acid separation and purification technology, applied in organic chemistry, chemical instruments and methods, cyanide reaction preparation, etc., can solve problems such as environmental pollution, inability to separate heteroacids, complex processes, etc., to solve the problem of dosage and salt pollution , reduce acid and alkali consumption, and achieve high production efficiency

Inactive Publication Date: 2014-07-30
WUXI JINGHAI AMINO ACID
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the problems existing in fermentation production mainly include low acid production level of strains, high content of miscellaneous acids, and other amino acids produced by fermentation metabolism, especially neutral amino acids such as leucine, its molecular weight and chemical isoelectric point, and branched chain amino acids. It is very close to the extraction, and the ion exchange process is generally used to separate the impurity acids, and the process is complicated. The main disadvantage is that the ion exchange resin needs to be regenerated and eluted, and a large amount of acid and alkali will be used in the regeneration process, which makes the product purity low. And the yield is low; a large amount of ammonium nitrogen waste liquid will be produced after elution and regeneration, which will not only cost a lot of money due to the consumption of a large amount of acid and alkali, but also cause great pollution to the environment. consume a lot of water
Backward production technology limits scale production
Because the content of other amino acids in the product is difficult to solve, domestic high-end API products cannot meet the EU standards, so they cannot enter the international market to participate in the competition of APIs

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] Desalination of valine hydrochloride to extract high-purity amino acids

[0030] (1) The valine fermentation broth was passed through the sterilization film to obtain the fermentation serum, concentrated under reduced pressure, and dried at 80°C to obtain the crude product

[0031] (2) Primary salt preparation: use industrial hydrochloric acid at a concentration of 30%, according to the mass volume ratio of crude valine to hydrochloric acid as 1.5g:3mL (w / v), add crude valine to industrial hydrochloric acid, and dissolve it at 80°C Naturally cool to 30°C, filter to obtain the primary salt, and apply hydrochloric acid to the filtered primary salt mother liquor as the secondary salt.

[0032] (3) Secondary salt: Add 50% of the primary salt valine crude product into the primary hydrochloric acid mother liquor, dissolve at 80°C, cool naturally to 30°C, and filter to obtain the secondary salt.

[0033] (4) Add water to dissolve valine hydrochloride into a concentrated sa...

Embodiment 2

[0037] Desalination of Isoleucine Hydrochloride to Extract High Purity Amino Acid

[0038] (1) Pass the isoleucine fermentation broth through a sterilizing film to obtain a fermentation supernatant, concentrate under reduced pressure, and dry at 80°C to obtain a crude product.

[0039] (2) Primary salt preparation: use industrial hydrochloric acid at a concentration of 30%, according to the mass volume ratio of crude isoleucine to hydrochloric acid is 1.2g:3mL (w / v), add crude isoleucine to industrial hydrochloric acid, 80°C After dissolving, cool naturally to 30°C, filter to obtain the primary salt, and use the filtered primary salt mother liquor as the secondary salt to apply hydrochloric acid.

[0040] (3) Secondary salt: Add 50% of the primary salt isoleucine crude product into the primary hydrochloric acid mother liquor, dissolve at 80°C, cool naturally to 30°C, and filter to obtain the secondary salt.

[0041] (4) Isoleucine hydrochloride is dissolved in water to for...

Embodiment 3

[0045] Desalination of Leucine Hydrochloride to Extract High Purity Amino Acid

[0046] (1) Pass the leucine fermentation broth through the sterilization film to obtain the fermentation serum, concentrate under reduced pressure, and dry at 80°C to obtain the crude product

[0047] (2) Primary salt preparation: use industrial hydrochloric acid at a concentration of 30%, according to the mass volume ratio of crude leucine to hydrochloric acid is 1.8g:4mL (w / v), add crude leucine to industrial hydrochloric acid, dissolve at 80°C, Cool to 30°C, filter to obtain the primary salt, and use hydrochloric acid as the secondary salt with the filtered primary salt mother liquor.

[0048] (3) Secondary salt: Add 50% of the primary salt valine crude product into the primary hydrochloric acid mother liquor, dissolve at 80°C, cool to 30°C naturally, and filter to obtain the secondary salt.

[0049] (4) Dissolve leucine hydrochloride with water to form a concentrated salt solution with a c...

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PUM

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Abstract

The invention discloses a separation and purification process for producing branched chain amino acid by using a fermentation method. The process comprises the following steps: 1) preparing a rough product; 2) preparing branched chain amino acid salt by using a hydrochloric acid technique; 3) desalting to purify a multi-membrane combined system. As a rough fermentation finished product is adopted to prepare hydrochloride firstly, secondly, other amino acids are separated and purified, and subsequently the multi-membrane combination technique is adopted to replace an ion exchange technique, the acid and alkali consumption is reduced, the wastewater emission is reduced, and clean production, energy conservation and emission reduction are achieved; a fermentation liquid is partially desalted by using an electrodialysis technique in the multi-membrane combination technique, and the salt is removed by coupling the electrodialysis technique with the ion exchange technique, the problems of use amount of ion exchange resin recycled acid and alkali and salt contamination are effectively solved, and the water consumption is reduced.

Description

technical field [0001] The invention relates to a separation and purification process for producing branched-chain amino acids by fermentation. Background technique [0002] Domestic production of branched-chain amino acids is mainly based on fermentation technology. At present, the problems existing in fermentation production mainly include low acid production level of strains, high content of miscellaneous acids, and other amino acids produced by fermentation metabolism, especially neutral amino acids such as leucine, its molecular weight and chemical isoelectric point, and branched chain amino acids. It is very close to the extraction, and the ion exchange process is generally used to separate the impurity acids, and the process is complicated. The main disadvantage is that the ion exchange resin needs to be regenerated and eluted, and a large amount of acid and alkali will be used in the regeneration process, which makes the product purity low. And the yield is low; a l...

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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