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A method for separating valine from valine fermentation broth

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 constraints of large-scale production of valine industry, large consumption of chromatographic fillers, large amount of solvents, etc. problems, to achieve the effect of ensuring separation efficiency and service life, reducing equipment investment and production loss, and low operating costs

Active Publication Date: 2019-10-18
JIANGNAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The traditional simulated moving bed chromatographic separation technology has problems such as high operating cost, large amount of solvent, many control points, and large consumption of chromatographic packing materials, which restrict the large-scale production of valine industry
[0007] As can be seen from the above, at present, there is no research on the separation and purification of valine in valine fermentation broth by sequential simulated moving bed chromatography using chelating resin as filler

Method used

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  • A method for separating valine from valine fermentation broth
  • A method for separating valine from valine fermentation broth

Examples

Experimental program
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Effect test

Embodiment 1

[0034] refer to Figure 1~2 , a method for separating valine from valine fermentation broth, comprising the steps of:

[0035] (1) Add 100 parts by weight of macroporous styrene-divinylbenzene polymer, 50 parts by weight of paraformaldehyde, 200 parts by weight of anhydrous zinc chloride, 200 parts by weight of vitriol oil and 400 parts by weight of ice in the reactor Acetic acid, feed hydrogen chloride gas while stirring, and react for 12 hours; after the reaction, wash with deionized water to neutrality, wash with ethanol and acetone, and dry in vacuum for 24 hours to obtain chloromethylated polystyrene resin (CMCPS);

[0036] (2) Take 50 parts by weight of CMCPS obtained in step (1) in the reactor, add 100 parts by weight of glycidyl methacrylate, 1.5 parts by weight of cuprous bromide, 5 parts by weight of 2,2'-bipyridine and 20 parts by weight N,N-Dimethylamide density, first sealed with nitrogen, then evacuated, 70 ° C for 16 hours; Washing, vacuum drying for 24h, to o...

Embodiment 2

[0042] refer to Figure 1~2 , a method for separating valine from valine fermentation broth, comprising the steps of:

[0043] (1) Add 150 parts by weight of macroporous styrene-divinylbenzene polymer, 100 parts by weight of paraformaldehyde, 250 parts by weight of anhydrous zinc chloride, 300 parts by weight of vitriol oil and 550 parts by weight of ice in the reactor Acetic acid, while stirring hydrogen chloride gas. React for 12 hours; after the reaction, wash with deionized water to neutrality, wash with ethanol and acetone, and dry in vacuum for 24 hours to obtain chloromethylated polystyrene resin (CMCPS);

[0044] (2) Take 80 parts by weight of CMCPS in step (1) in the reactor, add 150 parts by weight of glycidyl methacrylate, 3 parts by weight of cuprous bromide, 10 parts by weight of 2,2'-bipyridine and 25 parts by weight N,N-Dimethylamide density, first sealed with nitrogen, then evacuated, and reacted at 70°C for 16h; Washing, vacuum drying for 24h, to obtain the...

Embodiment 3

[0050] refer to Figure 1~2 , a method for separating valine from valine fermentation broth, comprising the steps of:

[0051] (1) Add 200 parts by weight of macroporous styrene-divinylbenzene polymer, 150 parts by weight of paraformaldehyde, 300 parts by weight of anhydrous zinc chloride, 400 parts by weight of vitriol oil and 70 parts by weight of ice in the reactor Acetic acid, while stirring hydrogen chloride gas. React for 12 hours; after the reaction, wash with deionized water to neutrality, wash with ethanol and acetone, and dry in vacuum for 24 hours to obtain chloromethylated polystyrene resin (CMCPS);

[0052] (2) Get 100 parts by weight of CMCPS in step (1) in the reactor, add 200 parts by weight of glycidyl methacrylate, 5 parts by weight of cuprous bromide, 15 parts by weight of 2,2'-bipyridyl and 30 parts by weight Parts by weight of N,N-dimethylamide dense, first sealed and ventilated with nitrogen, then vacuumized, and reacted at 70°C for 16h; Acetone washin...

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Abstract

The invention discloses a method for separating valine from valine fermentation liquid. The method comprises the following steps: (1) preparing chelating resin; (2) preparing a sequential simulated moving bed; and (3) performing separation and purification. The method disclosed by the invention adopts the chromatographic technique of the sequential simulated moving bed filled with home-made metalchelating resin to separate and purify the valine, thereby improving the valine production rate, reducing the three wastes (waste water, waste gas and waste solid), lowering the operating cost and reducing the dosage of chromatographic packing.

Description

technical field [0001] The invention relates to the fields of biological fermentation and food, in particular to a technology for separating and purifying valine by using metal chelating resin and sequential simulated moving bed chromatography. Background technique [0002] Valine is one of the eight essential amino acids for the human body. It can promote the normal growth of the human body, repair tissues, regulate blood sugar, and provide needed energy. Valine can be synthesized from isobutyraldehyde, but the human body cannot produce valine itself, so external resources are needed to supplement the amount of valine required by the daily activities of the human body. However, as modern people pay more attention to high value-added products, in addition to satisfying the normal activities of the human body, valine is also made into various products with unique functions and is widely used in medicine, chemical industry, agriculture and in food and other fields. [0003] ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C229/08C07C227/40C08F8/24C08F212/08C08F257/02C08F220/32C08F8/32C08F8/42
CPCC07C227/40C08F8/24C08F8/32C08F8/42C08F257/02C07C229/08C08F212/08C08F220/325
Inventor 张军伟宋乾宁朱程旭金伟
Owner JIANGNAN UNIV