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Method for extracting and separating succinic acid from fermentation liquid by using macroporous adsorption resin

A technology for separating succinic acid and adsorption resin, applied in the separation/purification of carboxylic acid compounds, organic chemistry, etc., can solve the problems of unfavorable large-scale commercial production, poor impurity removal effect, complex types of impurities, etc., and achieve easy operation , low solvent consumption and mild process conditions

Active Publication Date: 2017-08-11
SHANGHAI UNIVERSITY OF ELECTRIC POWER
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the technical scheme announced by the above-mentioned patent, D3520 type, H103 type non-polar macroporous adsorption resin or D301 type weakly basic anion exchange resin are used as auxiliary separation means, and the pigment in the fermentation broth is subjected to one-time separation at a higher temperature. Adsorption and removal improves the purity of the product to a certain extent, but due to the complex types of impurities in the fermentation broth, in addition to pigments, it also contains a large amount of protein, inorganic salts, sugars and various microbial metabolites, etc., it is difficult to use a single type At the same time, the resin completely adsorbs and removes all the impurities therein, the impurity removal effect is often poor, and the product quality is poor, and this process has no concentration and enrichment effect on the active ingredient (succinic acid) in the fermentation broth, that is, decolorization The concentration of succinic acid in the fermentation broth before and after is basically unchanged. Therefore, if the concentration of succinic acid in the fermentation broth itself is low, the energy consumption in the subsequent evaporation and concentration process will be high, which is not conducive to large-scale commercial production.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] Concentration is the initial filtrate after the succinic acid fermented liquid of 12.7g / L is filtered through 50nm inorganic ceramic membrane, with the concentrated H of 98% (w / w) 2 SO 4 After adjusting its pH to 2.0, pass it into a water-cooled jacketed chromatography column equipped with 160 mL of macroporous adsorption resin NKA-9 at a flow rate of 1 BV / h at room temperature, and control the amount of loading on the column to be 60% of the saturated adsorption capacity of the resin.

[0037] Then pour hot water at 80°C into the jacket of the chromatography column. After the temperature of the chromatography column rises to 80°C, pour hot water at 80°C into the column at a flow rate of 0.5BV / h to elute 2BV, and collect the eluted liquid. Add 98% (w / w) concentrated H to the eluent 2 SO 4 After adjusting its pH to 2.0, it was evaporated under reduced pressure at 50° C. and a vacuum of 0.1 MPa, and concentrated to 20% of the original volume. Cool the concentrated sol...

Embodiment 2

[0040] Concentration is the succinic acid fermented liquid of 1.3g / L after 20nm inorganic ceramic membrane filter the primary filtrate, with the concentrated HNO of 65% (w / w) 3 After adjusting its pH to 2.0, pass it into a water-cooled jacketed chromatography column equipped with 160mL macroporous adsorption resin AB-8 at room temperature at a flow rate of 1BV / h, and control the concentration of the effluent to be 10% of the concentration of the feed.

[0041] Then pour hot water at 90°C into the jacket of the chromatography column. After the temperature of the chromatography column rises to 90°C, pour hot water at 90°C into the column at a flow rate of 0.5BV / h to elute 2BV, and collect the eluted liquid. Add 65% (w / w) concentrated HNO to the eluate 3 After adjusting its pH to 2.0, it was evaporated under reduced pressure at 60° C. and a vacuum of 0.1 MPa, and concentrated to 30% of the original volume. Cool the concentrated solution to 4°C and maintain it for 20 hours to pr...

Embodiment 3

[0044] A method for extracting and separating succinic acid from fermentation broth by using macroporous adsorption resin, the method specifically includes the following steps:

[0045] (1) select the ultrafiltration membrane that aperture is 10nm for use, adopt the method for ultrafiltration to filter, to the succinic acid fermented liquid that succinic acid mass concentration is 50g / L carry out pretreatment, remove solid particle and macromolecule impurity in fermented liquid, obtain pretreatment liquid;

[0046] (2) Utilize hydrochloric acid to adjust the pH value of the pretreatment liquid to 2.0, pass into the adsorption column that polar macroporous adsorption resin is housed afterwards, be 15 ℃ at adsorption temperature, the feed concentration of pretreatment liquid is 30.0g / Under the condition of L, utilize the polar macroporous adsorption resin to adsorb the succinic acid in the pretreatment liquid;

[0047] (3) Pass 95°C hot water into the adsorption column, and pe...

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Abstract

The invention relates to a method for extracting and separating succinic acid from fermentation liquid by using macroporous adsorption resin. The method includes the following steps that 1, succinic acid fermentation liquid is pretreated to remove solid particles and macromolecule impurities in the fermentation liquid and obtain pretreatment liquid; 2, the pretreatment liquid is regulated to be acidic and then delivered to an adsorption column loaded with the polar macroporous adsorption resin, and the polar macroporous adsorption resin is used for adsorption of succinic acid in the pretreatment liquid; 3, an eluting agent is introduced in the adsorption column for eluting to obtain succinic acid eluent; 4, the succinic acid eluent is regulated to be acidic, then concentration, crystallization, filtration and drying are conducted in sequence, and succinic acid is obtained. Compared with the prior art, the polar macroporous adsorption resin is used for extracting and separating high-impurity succinic acid from the succinic acid fermentation liquid, the process is mild in condition, energy consumption is low, operation is simple and convenient, few solvent is consumed, the process is short, and large-scale commercial production is easy to achieve.

Description

technical field [0001] The invention belongs to the technical field of biological separation engineering, and relates to a method for extracting and separating succinic acid from fermentation liquid by using a macroporous adsorption resin. Background technique [0002] Succinic acid, also known as succinic acid, is an important platform compound that can be derived from various bulk chemicals such as butanediol, tetrahydrofuran and γ-butyrolactone. The preparation method of succinic acid includes chemical synthesis method and microbial fermentation method. Among them, the chemical synthesis method needs to consume a large amount of petrochemical raw materials, and the energy consumption and cost are high; the microbial fermentation method uses biological resources with low cost and greenhouse gas carbon dioxide as raw materials. , under suitable conditions, succinic acid is produced by bacteria or other microorganisms through a specific metabolic pathway, which has many adva...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C51/47C07C51/43C07C55/10
CPCC07C51/43C07C51/47C07C55/10
Inventor 朱晟符昊范金辰闵宇霖徐群杰
Owner SHANGHAI UNIVERSITY OF ELECTRIC POWER
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