Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Method for refining beta-thymidine in fermentation broth through ultrafiltration and ion exchange technology

A technology of ion exchange and fermented liquid, applied in the field of β-thymidine production, which can solve the problems of reduced membrane filtration speed, affecting product yield, cumbersome operation steps, etc., to improve product yield, reduce extraction and separation steps, and simple process reasonable effect

Inactive Publication Date: 2018-01-26
JIANGXI CHENGZHI BIOENG
View PDF4 Cites 4 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in this method, the β-thymidine fermentation liquid has passed through four times of membrane filtration according to the removal accuracy, and the operation steps are cumbersome and time-consuming, which affects the product yield.
And because the fermentation broth contains a large amount of metal ions, as the concentration factor increases during the membrane filtration process, metal salts will continue to be precipitated from the clear liquid, which will adhere to the surface of the membrane core during the membrane filtration process, resulting in subsequent membrane filtration. The filtration speed is reduced, and even the membrane pores are blocked, which greatly affects the filtration effect

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 refining beta-thymidine in fermentation broth through ultrafiltration and ion exchange technology
  • Method for refining beta-thymidine in fermentation broth through ultrafiltration and ion exchange technology
  • Method for refining beta-thymidine in fermentation broth through ultrafiltration and ion exchange technology

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] 100L of β-thymidine fermentation broth passed through a microfiltration membrane with a membrane pore size of 1000nm, the membrane entry pressure was 0.2MPa, the membrane exit pressure was 0.1MPa, and the operating temperature was 25°C. After the fermentation broth was concentrated 10 times, 20L of dialysis water was added. The filtrate passes through the 732-type cation-exchange resin column with a 2BV / H flow rate, and the positive column effluent is directly connected to the 717-type anion-exchange resin column with a 2BV / H flow rate. The ion exchange liquid passes through the ultrafiltration membrane with a molecular weight cut-off of 5000, the operating pressure is 1.4MPa, and the operating temperature is 30-35°C. After the ion exchange liquid is concentrated 15 times, 25L of dialysis water is added. The filtrate passes through 732-type cation exchange resin, 331-type anion-exchange resin, and HZ-818 resin in sequence. The resin chromatography effluent is concentrat...

Embodiment 2

[0029] 100L of β-thymidine fermentation broth passed through a microfiltration membrane with a membrane pore size of 200nm, the membrane entry pressure was 0.2MPa, the membrane exit pressure was 0.1MPa, and the operating temperature was 25°C. After the fermentation broth was concentrated 10 times, 30L of dialysis water was added. The filtrate passes through the 732-type cation-exchange resin column with a 2BV / H flow rate, and the positive column effluent is directly connected to the 717-type anion-exchange resin column with a 2BV / H flow rate. The ionotropic liquid passes through the ultrafiltration membrane with a molecular weight cut-off of 2000, the operating pressure is 1.4MPa, and the operating temperature is 30-35°C. After the ionotropic liquid is concentrated 15 times, 30L of dialysis water is added. According to the subsequent extraction method in Example 1, the β-thymidine crystals were vacuum-dried to obtain a total of 4.97 Kg of β-thymidine product. The purity of the...

Embodiment 3

[0032]100L of β-thymidine fermentation broth passed through a microfiltration membrane with a membrane pore size of 500nm, the membrane entry pressure was 0.2MPa, the membrane exit pressure was 0.1MPa, and the operating temperature was 25°C. After the fermentation broth was concentrated 10 times, 25L of dialysis water was added. The filtrate passes through an ultrafiltration membrane with a molecular weight cut-off of 2000, the operating pressure is 1.4MPa, and the operating temperature is 30-35°C. After the microfiltrate is concentrated by 15 times, 25 L of dialysis water is added. The ultrafiltrate passes through the 732-type cation exchange resin column with a 2BV / H flow rate, and the positive column effluent is directly connected to the 717-type anion-exchange resin column with a 2BV / H flow rate. According to the subsequent extraction method in Example 1, the β-thymidine crystals were vacuum-dried to obtain a total of 4.93 kg of β-thymidine product. The purity of the β-thy...

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
purityaaaaaaaaaa
Login to View More

Abstract

The invention discloses a method for refining beta-thymidine in a fermentation broth through an ultrafiltration and ion exchange technology. The method comprises (1) microfiltration of a fermentationbroth: treating the beta-thymidine fermentation broth through a filter film with film pore sizes of 50-1000nm, (2) ion exchange of the clean filtrate: treating the clean filtrate through cation and anion exchange columns to remove multivalent ions in the filtrate, (3) ultrafiltration of the ion exchange solution: treating the ion exchange solution through a filter film with molecular weight cut-off of 500-5000, and (4) chromatography concentration crystallization of the clean filtrate. The two-step film separation technology simplifies the existing multi-stage film separation process and extraction and separation processes are avoided. The ion exchange technology is used between two film separation processes so that the problem that a film separation rate is reduced because of concentration multiple improvement in the film separation process and metal salt precipitation in the practical production is solved. The method has the advantages of simple and reasonable processes, high extraction and separation degree, high yield and simple processes.

Description

technical field [0001] The invention relates to the technology in the field of production of β-thymidine, in particular to a method for refining β-thymidine in fermentation broth by ultrafiltration and ion exchange technology. Background technique [0002] β-thymidine, as a component of the genetic material deoxythymidine nucleic acid (DNA), exists in all biological cells and plays an important role in physiology. [0003] β-thymidine is the key intermediate for the synthesis of anti-AIDS antiviral drugs zidovudine and lamivudine in the pharmaceutical industry. One is to use 2-deoxy-N-phenylpentosamine as the starting material through chemical methods Synthesis of β-thymidine; one is to use Escherichia coli to ferment and produce β-thymidine with glucose and ammonia water as raw materials. However, due to the complex process of producing β-thymidine by chemical method, high requirements for production conditions, low product yield and high production cost, a series of defec...

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 Applications(China)
IPC IPC(8): C07H1/06C07H19/073
Inventor 夏颖
Owner JIANGXI CHENGZHI BIOENG
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products