A method for separating and extracting 2-ketobutyric acid from enzyme conversion solution
A technology for ketobutyric acid and enzymatic conversion, applied in the separation/purification of carboxylic acid compounds, organic chemistry, etc., can solve the problems of high production cost, low yield, low product purity, etc., to improve yield, avoid volatilization, good effect
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Embodiment 1
[0023] a. Take 5.0L of 2-ketobutyrate conversion solution (-ketobutyric acid content 42.3g / L), adjust the pH to 4.0 with hydrochloric acid, enter the microfiltration membrane separation system for microfiltration, and obtain the -ketobutyrate that removes the bacteria Acid microfiltrate; the microfiltration membrane separation system adopts a hollow fiber membrane separation system, the microfiltration membrane pore size is 0.2um, the operating temperature is 35°C, the pressure difference between the inlet membrane and the outlet membrane is 0.1Mpa, and the filtration process is divided into several times to add Top wash with purified water until the 2-ketobutyric acid content in the dope is lower than 2.0g / L, then shut down to obtain the 2-ketobutyric acid microfiltrate. The recovery rate of supernatant 2-ketobutyric acid reaches 96.2%, the cell removal rate is greater than 99.9%, and the membrane flux reaches 89L·(m 2 h) -1 .
[0024] b. Pump the clarified 2-ketobutyric ac...
Embodiment 2
[0031] Get 2-ketobutyrate enzyme conversion solution 6.8L (2-ketobutyric acid content 35.3g / L), regulate pH with hydrochloric acid and be 4.0, carry out microfiltration and ultrafiltration to remove protein according to the method for embodiment 1 (wherein , microfiltration conditions: the microfiltration membrane pore size is 0.1um, the temperature is 50 ° C, and the pressure difference between the inlet and outlet membranes is 0.05 MPa; the ultrafiltration conditions: the temperature is 20 ° C, the operating pressure difference is 0.05 MPa), and the weight of the ultrafiltrate is 1.5 % activated carbon for decolorization, temperature 45°C, stirring and decolorizing for 25min, filtering to obtain 2-ketobutyric acid decolorization solution, adjusting the pH to 11.0 with sodium hydroxide, adding 1.5% of the weight of the decolorization solution by activated carbon to adsorb flocculent protein, and then decompressing Evaporate to 18% of the original volume liquid to obtain 2-keto...
Embodiment 3
[0033] Get 8.4L of 2-ketobutyrate conversion solution (2-ketobutyric acid content 37.2g / L), adjust pH with hydrochloric acid to be 4.0, carry out microfiltration and ultrafiltration to remove protein according to the method for embodiment 1 (wherein , microfiltration conditions: the microfiltration membrane pore size is 0.1um, the temperature is 10°C, and the pressure difference between the inlet and outlet membranes is 0.1Mpa; the ultrafiltration conditions: the temperature is 50°C, the operating pressure difference is 0.08MPa), and the weight of the ultrafiltrate is 1.8 % activated carbon for decolorization, temperature 40°C, stirring and decolorizing for 30min, filtering to obtain 2-ketobutyric acid decolorization solution, adjusting the pH to 11.0 with sodium hydroxide, adding 1.8% of the weight of the decolorization solution by activated carbon to adsorb flocculent protein, and then decompressing Evaporate to 20% of the original volume liquid to obtain 2-ketobutyric acid c...
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