A method for preparing conjugated linoleic acid by coupling method using immobilized lipase as catalyst
A technology of immobilized lipase and conjugated linoleic acid, which is applied in the direction of fermentation, etc., can solve the problems of unsatisfactory industrial production, long reaction time, and low product quality, so as to improve the reuse rate, shorten the enzyme reaction time, and improve The effect of product quality
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Embodiment 1
[0047] (1) Take 100g of methyl ester conjugated material, add an appropriate amount of 50% sulfuric acid / water at 50 degrees to neutralize to pH=8, and then continue to acidify for 1 hour to obtain acidified methyl ester conjugated material, the methyl ester conjugated The content of methyl conjugated linoleate in the chemical material is 80wt%;
[0048] (2) Fill 5g of immobilized lipase in the enzyme reaction column, and keep the temperature of the enzyme reaction column at 45°C;
[0049] (3) Prepare the acidified methyl ester conjugated material obtained in step (1) and water at a mass ratio of 1:0.5 to form a reaction solution, stir the reaction solution evenly to obtain an emulsified system, and preheat it to 40°C, pass through a constant flow The pump is pumped into the enzyme reaction column prepared in step (2), the stirring speed is 100rpm / min, the flow rate is 0.5ml / min, and the reaction is continued for 4 hours to obtain the reaction product. Continue to use 50% sulf...
Embodiment 2
[0051] (1) Add 50% citric acid aqueous solution to 100 g of methyl ester conjugated material, neutralize to pH = 8, and then continue to acidify for 1 hour to obtain acidified methyl ester conjugated material. The methyl ester conjugated material is co- Conjugated linoleic acid methyl ester content is 80wt%;
[0052] (2) Fill 5g of immobilized lipase in the enzyme reaction column, and keep the temperature of the enzyme reaction column at 40°C;
[0053] (3) Prepare the acidified methyl ester conjugated material obtained in step (1) and water at a mass ratio of 1:0.5 to form a reaction solution, stir the reaction solution evenly, and preheat it to 40°C, and pump it into the step through a constant flow pump (2) In the prepared enzyme reaction column, the stirring speed is 100rpm / min, the flow rate is 0.5ml / min, and the reaction is continued for 4h, and the reaction product obtained is acidified to pH7. 0, and then centrifuged to obtain the oil phase, which is the final product....
Embodiment 3
[0055] Obtain the acidified methyl ester conjugated material according to the method of implementing the step (1) of 2, wherein the organic acid used for acidification is 50% aqueous solution of wolfberry acid, and the content of methyl conjugated linoleate in the methyl ester conjugated material is 80wt%.
[0056] The enzyme reaction column filled with immobilized lipase was prepared according to the method in Example 2.
[0057] The prepared acidified methyl ester conjugated material and water were formulated into a reaction solution at a mass ratio of 1:0.5, the reaction solution was stirred evenly, and preheated to 40°C, and pumped into the enzyme reaction column through a constant flow pump at a stirring speed of 100rpm / min, flow rate 0.5ml / min, continuous reaction for 4 hours, the obtained reaction product was acidified to about pH7.0 with 50% aqueous solution of wolfberry acid at 80°C, and then centrifuged to obtain the oil phase, which is the final product , determine...
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