Enzyme catalysis method for continuous synthesis of lauroyl maltose under organic phase
A technology of lauric acid ester and maltose, applied in the field of food biochemical industry, can solve the problems of batch production not suitable for large-scale industrial production, complicated separation work, slow reaction rate, etc., and achieves mild conditions, simple separation and purification, and increased yield Effect
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Embodiment 1
[0035] The concentration of adding maltose in the reactor at the beginning of the reaction is 25mmol / L (2.125g), 100mmol / L lauric acid acetone solution 250ml, 20g / L lipase, and then reacts and adds 8g / L maltose in the reactor every day, 100mmol / L L of lauric acid acetone solution enters the reactor with a flow rate of 0.36ml / min, and reacts for 10d. The yield and the amount of product obtained after separation and purification are shown in Table 1.
[0036] Table 1
[0037]
Embodiment 2
[0039]The concentration of maltose added in the reactor at the beginning of the reaction is 50mmol / L (4.275g), 250ml of 200mmol / L lauric acid acetone solution, 40g / L lipase, and then the reaction adds 12g / L maltose every day, the lauric acid of 200mmol / L The acetone solution enters the reactor at a flow rate of 0.2ml / min, and reacts for 10d. The yield and the amount of product obtained after separation and purification are shown in Table 2.
[0040] Table 2
[0041]
Embodiment 3
[0043] The concentration of maltose added in the reactor at the beginning of the reaction is 100mmol / L, 250ml of 300mmol / L lauric acid acetone solution, 60g / L lipase, and then the reaction adds 16g / L maltose every day, and the lauric acid acetone solution of 300mmol / L is added at 0.15 The flow rate of ml / min enters the reactor and reacts for 10d. The yield and the amount of product obtained after separation and purification are shown in Table 3.
[0044] table 3
[0045]
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