Method for separating and purifying branched chain amino acid from fermentation broth

A branched-chain amino acid, separation and purification technology, applied in the field of separation and purification of branched-chain amino acids, can solve problems such as environmental pollution, inability to separate miscellaneous acids, consumption of large amounts of water, etc., to solve the problem of dosage and salt pollution, reduce acid-base consumption, and reduce waste water. The effect of emissions

Active Publication Date: 2018-10-26
WUXI JINGHAI AMINO ACID
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Now, the production of branched-chain amino acids mainly relies on microbial fermentation, but other amino acids will be produced during microbial fermentation. The molecular weight and chemical isoelectric point of these amino acids, especially neutral amino acids (such as leuc amino acids), are very close to branched-chain amino acids. Caused problems such as low acid production level and high heteroacid content in the process of microbial fermentation to produce branched chain amino acids
[0004] At present, the ion exchange method is often used to extract branched-chain amino acids in the fermentation broth of microorganisms. However, the ion exchange process cannot separate heteroacids and has many defects. For example, the ion exchange process steps are complicated and require regeneration and elution; ion exchange A large amount of acid and alkali will be used in the regeneration process of the process, resulting in low product purity and low yield; the ion exchange process will produce a large amount of ammonium nitrogen waste liquid after elution and regeneration, which will not only consume a large amount of acid and alkali It costs a lot of money and will cause great pollution to the environment. At the same time, the elution process will consume a lot of water
[0005] Therefore, the backwardness of separation technology limits the large-scale production of branched-chain amino acids, and because other amino acids in branched-chain amino acid products are difficult to remove, domestic high-end API products cannot meet 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

[0042] Embodiment 1: the separation and purification of valine

[0043] Specific steps are as follows:

[0044] (1) filter and sterilize the valine fermentation broth and concentrate it to 5 times, then spray-dry the concentrated fermentation broth to obtain crude valine;

[0045] (2) Mix the crude valine and hydrochloric acid according to a mass ratio of 1:3, and dissolve for the first time at 80° C. to obtain a crude valine solution;

[0046] (3) Filter the crude valine solution after being cooled to 25°C for the first time to obtain valine hydrochloride;

[0047] (4) adding valine hydrochloride into water according to a certain ratio, and dissolving for the second time at 80° C. to obtain a valine hydrochloride solution with a concentration of 5%;

[0048] (5) Filtrating and desalting the valine hydrochloride solution through a nanofiltration membrane, an ion exchange membrane, and an electrodialysis membrane to obtain a valine hydrochloride supernatant;

[0049] (6) Coo...

Embodiment 2

[0052] Embodiment 2: Separation and purification of isoleucine

[0053] Specific steps are as follows:

[0054] (1) filter and sterilize the isoleucine fermentation broth and concentrate it to 5 times, then spray-dry the concentrated fermentation broth to obtain crude isoleucine;

[0055] (2) mixing crude isoleucine and hydrochloric acid in a mass ratio of 1:3, and dissolving for the first time at 80° C. to obtain crude isoleucine solution;

[0056] (3) cooling the crude isoleucine solution to 25° C. for the first time and then filtering to obtain isoleucine hydrochloride;

[0057] (4) adding isoleucine hydrochloride into water according to a certain ratio, and dissolving for the second time at 80° C. to obtain a solution of isoleucine hydrochloride with a concentration of 7%;

[0058](5) Filtrating and desalting the isoleucine hydrochloride solution through a nanofiltration membrane, an ion exchange membrane, and an electrodialysis membrane to obtain an isoleucine hydrochlo...

Embodiment 3

[0062] Embodiment 3: Separation and purification of isoleucine

[0063] Specific steps are as follows:

[0064] (1) filtering and sterilizing the leucine fermentation broth and concentrating it to 5 times, and then spray-drying the concentrated fermentation broth to obtain crude leucine;

[0065] (2) Mixing the crude leucine and hydrochloric acid in a mass ratio of 1:3, and dissolving for the first time at 80° C. to obtain a crude leucine solution;

[0066] (3) Filtering the crude leucine solution after cooling down to 25°C for the first time to obtain leucine hydrochloride;

[0067] (4) adding leucine hydrochloride into water according to a certain ratio, and dissolving for the second time at 80° C. to obtain a leucine hydrochloride solution with a concentration of 4%;

[0068] (5) Filtering and desalting the leucine hydrochloride solution through a nanofiltration membrane, an ion exchange membrane, and an electrodialysis membrane to obtain a leucine hydrochloride supernata...

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Abstract

The invention discloses a method for separating and purifying branched chain amino acid from fermentation broth, and belongs to the technical field of microbial fermentation. According to the method disclosed by the invention, four-stage varying-temperature crystallization replaces conventional crystallization technology, wherein the clear liquid of branched chain amino acid hydrochloride is cooled for the second time to 60-80 DEG C for preliminary crystallization; then, constant-temperature crystal growing is performed at a constant temperature of 60-65 DEG C, and the third cooling is performed to 50-55 DEG C for secondary crystallization; finally, the fourth cooling is performed to 10-30 DEG C for final crystallization to obtain finished products of branched chain amino acid and hydrochloride thereof; The recovery rate of the finished products of branched chain amino acid and hydrochloride thereof prepared by the method can reach 90.1%, and the purity of the branched chain amino acidcan reach 99.9%.

Description

technical field [0001] The invention relates to a method for separating and purifying branched-chain amino acids from fermentation broth, and belongs to the technical field of microbial fermentation. Background technique [0002] Branched-chain amino acids refer to the three common amino acids found in proteins, consisting of leucine, valine, and isoleucine. This type of amino acid can promote the release of insulin and the release of growth hormone, which are two special ways to promote human anabolism and accelerate human muscle growth. Therefore, there is a huge market for BCAAs in sports supplements and health products. [0003] At present, the production of branched-chain amino acids mainly relies on microbial fermentation, but other amino acids will be produced during microbial fermentation. The molecular weight and chemical isoelectric point of these amino acids, especially neutral amino acids (such as leuc amino acids), are very close to branched-chain amino acids. ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C227/40C07C227/42C07C229/08
CPCC07C227/40C07C227/42C07C229/08
Inventor 宁健飞陈晓双蔡立明
Owner WUXI JINGHAI AMINO ACID
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