Method for producing high-purity isobutyramide
A technology of isobutyramide and production method, applied in the field of bioengineering, can solve the problems of complex process, low yield, difficult environmental protection requirements, etc., and achieves the effects of mild reaction conditions, simple preparation process and easy industrialization
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Embodiment 1
[0016] The nitrile hydratase catalyst used was Rhodococcus Rhodococcus sp. The production strain is obtained through fermentation and cultivation, and the activity of the nitrile hydratase catalyst is 721×10 4 mg·h -1 ·ml -1 .
[0017] 20Kg of fermented liquid is filtered and separated with a 0.1mm sintered metal filter, and then washed twice with 20Kg of deionized water to remove impurities in the nitrile hydratase catalyst to obtain 1Kg of nitrile hydratase catalyst.
[0018] In order to ensure that the final concentration of isobutyramide in the reaction solution is above 30%, and the reaction time is within 4 hours, add 120Kg of deionized water to the reactor, and add 1Kg of pre-cleaned nitrile hydratase catalyst to the reaction In the reactor, the stirrer was started, and the temperature of the reactor was controlled at 25°C. Then start to add isobutyronitrile in the reactor, and flow rate reduces gradually, and the flow rate at the beginning is 18Kg / h, and the flow r...
Embodiment 2
[0023] The nitrile hydratase catalyst used was obtained from the production strain of Nocardia sp through fermentation, and the activity of the nitrile hydratase catalyst was 789×10 4 mg·h -1 ·ml -1 .
[0024] 20Kg of fermented liquid is filtered and separated with a 0.1mm sintered metal filter, and then washed twice with 20Kg of deionized water to remove impurities in the nitrile hydratase catalyst to obtain 1Kg of nitrile hydratase catalyst.
[0025] Add 120 Kg of deionized water into the reactor, add 1 Kg of nitrile hydratase catalyst cleaned in advance into the reactor, start the stirrer, and control the temperature of the reactor at 25° C. Then start to add isobutyronitrile in the reactor, and flow rate reduces gradually, and the flow rate at the beginning is 18Kg / h, and the flow rate after 1 hour is reduced to 17Kg / h, and the flow rate after 2 hours is reduced to 14Kg / h, and after 3 hours The flow rate is reduced to 10Kg / h, and a total of 54Kg of isobutyronitrile has ...
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