Method for separating and purifying gamma-aminobutyric acid (GABA) from glutamine decarboxylase enzymolysis liquid
A glutamylamine decarboxylase enzymatic hydrolyzate, glutamylamine decarboxylase technology, applied in the field of bioengineering, can solve the problems of long γ-aminobutyric acid process steps, incomplete separation and purification, limited separation ability, etc. Conducive to the utilization of solidified concentrates, avoiding secondary pollution and high concentration multiples
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Example Embodiment
[0019] Example 1
[0020] The glutamylamine decarboxylase solution prepared by microbial fermentation, using sodium glutamate as the substrate, after enzymatic hydrolysis to obtain an enzymatic hydrolysis solution with a GABA content of 2-9g / L. The enzymatic hydrolysis solution is subjected to organic ultrafiltration with a cut-off molecular weight of 1000Da The membrane is filtered and clarified, the temperature of the material liquid is controlled at 20~60℃, the operating pressure is 0.1~0.3MPa, the flow rate of the membrane surface is 2~5.5m / s, when the concentration is 1 time, add dialysis water, the amount of dialysis water is 2 times enzymatic hydrolysis The liquid volume is concentrated after 5 times. The total filtration yield is 95-99%, the concentration factor is 5 times, the amount of filtrate is 2.5 times of enzymolysis solution, and the amount of concentrated solution is 0.5 times of enzymolysis solution. The filtrate is pumped into the cation and anion exchange res...
Example Embodiment
[0021] Example 2
[0022] Glutamine decarboxylase solution prepared by microbial fermentation, using sodium glutamate as a substrate, and enzymatic hydrolysis solution with a GABA content of 2-9g / L is obtained. The enzymatic hydrolysis solution uses a stainless steel ultrafiltration membrane with a membrane pore size of 20nm Filter and clarify, the temperature of the feed solution is controlled at 20~60℃, the operating pressure is 0.4~0.8MPa, the flow rate of the membrane surface is 2~5.5m / s, when the concentration is 5 times, add dialysis water, and the amount of dialysis water is 0.5 times the enzymatic hydrolysis solution The amount is concentrated after 10 times. The total filtration yield is 95-99%, the concentration factor is 10 times, the filtrate volume is 1.4 times the enzymolysis solution, and the concentrated solution volume is 0.1 times the enzymolysis solution. The filtrate is pumped into the cation and anion exchange resin columns in sequence, the column temperatur...
Example Embodiment
[0023] Example 3
[0024] The glutamylamine decarboxylase solution prepared by the extraction process uses glutamic acid as the substrate. After enzymolysis, the enzyme hydrolysis solution with the GABA content of 2-9g / L is obtained. The enzyme hydrolysis solution is carried out with a microfiltration membrane with a molecular weight of 100,000 Da. Filter and clarify, control the material liquid temperature at 20~60℃, the operating pressure is 0.4~0.8MPa, the membrane surface flow rate is 2~5.5m / s, when the concentration is 5 times, add dialysis water, the dialysis water volume is 0.4 times the enzymatic hydrolysis volume , End after concentration 10 times. The total filtration yield is 95-99%, the concentration factor is 10 times, the filtrate volume is 1.3 times the enzymolysis solution, and the concentrated solution volume is 0.1 times the enzymolysis solution. The filtrate is pumped into the cation-anion mixed bed ion exchange system, the column temperature is less than 40°C...
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap