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Glutamic acid extraction crystallization process

A glutamic acid and process technology, which is applied in the field of glutamic acid extraction and crystallization process, can solve the problems of large amount of sewage, high treatment difficulty, poor protein quality, etc., and achieve the effect of increasing adsorption rate, increasing total yield and improving quality

Active Publication Date: 2016-06-08
内蒙古阜丰生物科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, this process has disadvantages such as large amount of sewage and high treatment difficulty, poor protein quality, low product quality, and large amount of acid and alkali.
[0004] In addition, some manufacturers adopt the continuous concentration isoelectric process to control the temperature of the glutamic acid fermentation liquid at 42-45°C after concentration, and then pour it into the isoelectric tank, and use sulfuric acid to control the pH of the isoelectric tank at about 3.2. Cool down in the cold tank, use a centrifuge to centrifuge glutamic acid, and discharge the centrifuged liquid to the sewage treatment plant. This process produces less sewage and does not have a separation process, but the yield and quality of glutamic acid are low

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

[0029] A kind of glutamic acid extraction crystallization process, it comprises the steps:

[0030] 1) Disc centrifuge separation: the glutamic acid fermentation liquid is separated by a disc centrifuge, and centrifuged into two parts, one part is the supernatant A6000L containing a small amount of bacterial protein, and the bacterial protein content is 0.1% (volume ratio) , the other part is the protein liquid B1500L containing a large amount of bacterial protein, and the bacterial protein content is 82% (volume ratio);

[0031] 2) Separation by decanter centrifuge: The protein liquid B1500L containing a large amount of bacterial protein is separated by a decanter centrifuge, and centrifuged into two parts, one part is the supernatant C1135L containing a small amount of bacterial protein, and the bacterial protein content is 0.45% (volume ratio ), the other part is a paste-like protein concentrate D389kg, the dry matter content of protein is 35% (mass ratio);

[0032] 3) Sec...

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PUM

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Abstract

The invention belongs to the field of amino acid production, and discloses a glutamic acid extraction crystallization process, characterized by comprising the following steps: (1) separating by a disc type centrifuge, (2) separating by a horizontal screw centrifuge, (3) secondarily separating by the disc type centrifuge, (4) mixing, (5) combining, (6) concentrating, (7) performing isoelectric treatment, (8) feeding a concentrated solution, (9) cooling, (10) centrifuging by a flat plate centrifuge, (11) performing ion exchange, and (12) drying a thallus. By adopting the process, energy conservation and emission reduction are realized, and meanwhile the quality and the extraction rate of glutamic acid are ensured.

Description

technical field [0001] The patent of the invention relates to a glutamic acid extraction and crystallization process, which belongs to the field of amino acid production. Background technique [0002] Glutamic acid is an acidic amino acid. The molecule contains two carboxyl groups, and its chemical name is α-aminoglutaric acid. Glutamic acid was discovered by Li Suxun in 1856. It is a colorless crystal with umami taste, slightly soluble in water, but soluble in hydrochloric acid solution, with an isoelectric point of 3.22. A large amount exists in cereal protein, and the content in animal brain is also more. Glutamic acid plays an important role in the protein metabolism process in organisms, and participates in many important chemical reactions in animals, plants and microorganisms. MSG is prepared from glutamic acid. [0003] At present, the extraction process commonly used by domestic glutamic acid manufacturers is the isoelectric and ionoelectric extraction process, ...

Claims

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Application Information

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IPC IPC(8): C07C229/24C07C227/40C12N1/00
CPCC07C227/40C12N1/00C07C229/24
Inventor 王均成丁兆堂张传森卢松张修军李晓永张春宇
Owner 内蒙古阜丰生物科技有限公司
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