Novel process for producing valine

A valine and new process technology, applied in the new process field of valine production, can solve problems such as product quality fluctuation, low product yield, passive production, etc., achieve standard production process, reduce production cost, and reduce environmental protection pressure Effect

Active Publication Date: 2009-11-18
JIANGSU SHENHUA PHARMA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, valine is basically produced by microbial fermentation. The extraction method: abroad, represented by Ajinomoto, adopts precipitation method to extract. According to the specific combination of precipitant and valine, a precipitate is formed, and then separated and extracted. This method has the advantages of extraction yield. However, there are technical problems of environmental pollution; domestically, the ion exchange method is mainly used for the extraction of valine, and the pH value of the fermented liquid after removing bacteria is lowered, and 732 cation exchange resin is used to separate valine And associated heteroacids, because the properties of associated heteroacids and valine are similar, generally 3-5 ion exchange columns are used for serial extraction, which leads to a large amount of waste water in the production process, and the product yield is low, generally at 60% Left and right, improper operation can easily cause fluctuations in product quality. In the production process, the quality of the finished product is often used to determine its grade and price, making production in a passive position.

Method used

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  • Novel process for producing valine

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Experimental program
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Effect test

Embodiment 1

[0016] 1) Preparation of crude valine and feed-grade valine: 70L of valine fermentation broth, with a content of 3.9%, was removed by ultrafiltration to remove macromolecular impurities such as bacteria, decolorized with activated carbon for injection, and then concentrated and crystallized under reduced pressure. Centrifuge to obtain the crude product of valine, 2.05kg of valine with a conversion purity of 100%, 7.15L of mother liquor, and a content of 9.5%, and the crude product mother liquor is spray-dried to obtain 0.92kg of feed grade valine with a content of 74%;

[0017] 2) Preparation of valine hydrochloride: slowly add the crude product into dilute hydrochloric acid with a volume of 35 L and a concentration of 6 mol / L, stir at 65°C until completely dissolved, then cool down to crystallize, and centrifuge to obtain valine hydrochloride and Valine hydrochloride mother liquor. Thin-plate chromatography was used to detect the purity of valine hydrochloride. If there were ...

Embodiment 2

[0026] 1), the preparation of valine crude product and feed grade valine

[0027] Valine fermented liquid 6.5L, content 4.2%. Macromolecular impurities such as bacteria were removed by ultrafiltration, decolorized by activated carbon for injection, concentrated and crystallized under reduced pressure, and centrifuged after cooling to obtain crude valine, 213g of valine with a conversion purity of 100%, 0.645L of mother liquor, content 9.3%, The crude product mother liquor was spray-dried to obtain 78.7g of feed grade valine with a content of 73.7%;

[0028] 2), preparation of valine hydrochloride

[0029] The crude product was slowly added to dilute hydrochloric acid with a volume of 3.4 L and a concentration of 6 mol / L, stirred at 70°C until it was completely dissolved, then cooled to crystallize, and centrifuged to obtain valine hydrochloride and valine hydrochloride mother liquor, thin plate layer Analyze and detect the purity of valine hydrochloride. If there are spots o...

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Abstract

The invention discloses a novel process for producing valine, which comprises the following steps: obtaining a valine zymotic fluid by a microbiological fermentation method, removing impurities such as thalli through an ultrafiltration membrane, concentrating and crystallizing to obtain a crude product of the valine, and performing spray drying on mother solution to produce a feed grade product; performing acid dissolution and recrystallization on the crude product of the valine, dissolving the obtained product by 10 to 15 times of water, then producing a pharmaceutical product through ion exchange treatment, decolorization by an eluent and crystallization, and then circularly using a mother solution through the ion exchange treatment; and diluting the mother solution obtained after the re-crystallization of the crude product, then producing a food grade product through ion exchange by the mother solution, and then circularly using the mother solution through the ion exchange treatment. The process greatly improves the total extraction yield of products, produces different levels of products to meet different demands of the market, and reduces environmental pollution by recoveringand reutilizing partial wastewater generated during the ion exchange.

Description

technical field [0001] The invention belongs to the technical field of amino acid production and relates to a new process for producing valine. Background technique [0002] As one of the branched chain amino acids, L-valine is mainly used in the preparation of compound amino acid infusions, synthetic polypeptide drugs and food antioxidants, etc., especially in medical research and treatment. With continuous deepening, its scope of application in the food and feed industry will be further expanded. At present, valine is basically produced by microbial fermentation. The extraction method: abroad, represented by Ajinomoto, adopts precipitation method to extract. According to the specific combination of precipitant and valine, a precipitate is formed, and then separated and extracted. This method has the advantages of extraction yield. However, there are technical problems of environmental pollution; domestically, the ion exchange method is mainly used for the extraction of va...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C229/08C07C227/40C07C227/42B01D15/04
Inventor 徐国华林永贤李晓永王子军张春宇
Owner JIANGSU SHENHUA PHARMA
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