Method for extracting l-4-hydroxyisoleucine from fermentation catalytic liquid

A technology of hydroxyisoleucine and L-4-, applied in the field of separation and purification, can solve the problems of cost reduction, expensive raw materials, low extraction rate, etc.

Active Publication Date: 2021-03-19
HENAN JULONG BIOLOGICAL ENG CO LTD
View PDF1 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Limited by technology and cost, the output of L-4-hydroxyisoleucine in my country cannot meet the needs of domestic and foreign trade exports
Currently reported L-4-hydroxyisoleucine production methods include extraction, chemical synthesis, and enzymatic methods, but only the extraction method is used for industrial production and has disadvantages such as low extraction rate, difficult separation and purification, large demand for raw materials, and high cost. , the traditional chemical method, whether it is organic synthesis or chemical resolution, loses its competitiveness due to high production costs
In the biological method, the efficiency of the enzyme-catalyzed method is relatively high, but there are still problems such as cumbersome operation, expensive raw materials, and high production cost. At present, there is a lack of relevant technology that can be used in industrialized large-scale production. This method has now been able to formally Carry out large-scale industrial production, and the cost is greatly reduced, and the product meets the detection standard of pharmaceutical grade raw material L-4-hydroxyisoleucine

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Method for extracting l-4-hydroxyisoleucine from fermentation catalytic liquid
  • Method for extracting l-4-hydroxyisoleucine from fermentation catalytic liquid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0057] Method for extracting L-4-hydroxybiobine in fermentation catalysts comprising the steps of:

[0058] (1) L-4-hydroxyisineluminine fermentation catalytic solution was prepared by the following method:

[0059] 1 After the concentration of Escherichia coli resection of L-4-hydroxyisoleine, it is used in seed tank medium containing final concentration of 0.1 g / L amp, at 37 ° C, pH 7.0, and solubol control. Cultured in more than 25% of the OD of the bacteria 600 The value is 15 to obtain a seed liquid;

[0060] 2 The seed fluid obtained by step (1) is 10% in the fermentation tank medium according to the volume percentage of 15%, and the liquid is deeply ventilated under 36 ° C and then cooling to 32 ° C and the final concentration is 0.1 mmol / L. IPTG continues to culture until fermentation is completed, wherein the fermentation process residue is 0.05% by weight, and the oxygen is controlled after 20 ~ 35%, pH 7.0, and the amount of glucose is carbon. source;

[0061] 3 fer...

Embodiment 2

[0068] Method for extracting L-4-hydroxybiobine in fermentation catalysts comprising the steps of:

[0069] (1) L-4-hydroxyisineluminine fermentation catalytic solution was prepared by the following method:

[0070] 1 After the concentration of Escherichia coli resection of L-4-hydroxyisoleine, it is used in seed tank medium containing final concentration of 0.1 g / L amp, at 37 ° C, pH 7.0, and solubol control. Cultured in more than 25% of the OD of the bacteria 600 The value is 14 to obtain a seed liquid;

[0071] 2 The seed fluid obtained by step (1) is incorporated into the fermentor medium according to the volume percentage of 15%, and the liquid deep ventilated fermentation was cultured under 35 ° C and then cooled to 30 ° C and the final concentration was 0.1 mmol / L. IPTG continues to culture until fermentation is completed, wherein the fermentation process residue is 0.05% by weight or less, and the oxygen is controlled after 20 ~ 35%, pH 6.5, and the base glycoose is ap...

Embodiment 3

[0079] Method for extracting L-4-hydroxybiobine in fermentation catalysts comprising the steps of:

[0080] (1) L-4-hydroxyisineluminine fermentation catalytic solution was prepared by the following method:

[0081]1 After the concentration of Escherichia coli resection of L-4-hydroxyisoleine, it is used in seed tank medium containing final concentration of 0.1 g / L amp, at 37 ° C, pH 7.0, and solubol control. Cultured in more than 25% of the OD of the bacteria 600 The value is 16, resulting in a seed liquid;

[0082] 2 The seed liquid obtained by step (1) is 10% in the fermenter medium according to the volume percentage of 15%, and the liquid is deeply ventilated under 40 ° C, and then cool down to 32 ° C and the final concentration is 0.1 mmol / L. IPTG continues to culture until fermentation is completed, wherein the fermentation process residue is 0.05% or less, and the oxygen is controlled after 20 ~ 35%, pH 7.5, and the base glycoose is used as a carbon source. ;

[0083] 3...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

PropertyMeasurementUnit
pore sizeaaaaaaaaaa
transmittivityaaaaaaaaaa
Login to view more

Abstract

The invention relates to the technical field of separation and purification, in particular to a method for extracting L-4-hydroxyisoleucine from fermentation catalyst liquid. The steps of micro-filtration membrane filtering, super-filtration membrane filtering, ion exchange and the like are used for purifying and separating the L-4-hydroxyisoleucine in the L-4-hydroxyisoleucine fermentation catalyst liquid; the extraction system is simple and efficient; the flow process is simple; the implementation is easy; 732 cation resin adsorption is performed on filtration membrane clear liquid; ammoniawater with the ammonia content being 1.2 to 1.5 weight percent is used for elution; the ammonia salt content in the finished product can be reduced; the purity is improved; the alcohol sedimentation is used in primary crystallization; the yield of the primary coarse product can be improved by 50 percent or higher; in secondary crystallization, the alcohol sedimentation is used, the yield of a finished product can be improved by 50 percent or higher; in addition, the product liquid phase purity can be obviously improved; the final product total yield can reach 50 percent; the product purity isnot less than 95 percent. The method has the advantages that the efficiency is high; the cost is low; the large-scale industrial production is easy.

Description

Technical field [0001] The present invention relates to the field of separation and purification, and more particularly to a method of extracting L-4-hydroxyobine extracting a fermentation catalyst. Background technique [0002] L-4-hydroxyisoleucine (4-hydroxyisyisoleucine) is a non-protein amino acid present in nature. The study found that L-4-hydroxybiobiline has many aspects of promoting insulin secretion, improving insulin tolerance and regulation of blood lipids. The L-4-hydroxyisineluminine can not only promote the intake of glucose, but also reduce liver glucose output to improve insulin tolerance of the outer peripheral tissue. In contrast, insulin synthesis of L-4-hydroxybiobiline regulatory insulin-controlled insulin synthesis is strictly dependent on glucose concentration compared to current drugs that have been used to treat T2DM. Therefore, L-4-hydroxybiobine does not cause side effects such as hypoglycemia. At the same time, the L-4-hydroxybiobine can also effectiv...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Patents(China)
IPC IPC(8): C07C229/22C07C227/40C07C227/42C12P13/04C12R1/19
CPCC07B2200/07C07C227/40C07C227/42C12P13/04C07C229/22
Inventor 张孟涛路殿英魏鹏辉
Owner HENAN JULONG BIOLOGICAL ENG CO LTD
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products