Method for preparing diglyceride through continuous glycerolysis by enzyme method
A diglyceride and glycerol hydrolysis technology, which is applied in the field of enzymatic continuous preparation of diglyceride, can solve the problems of large solvent usage, reduced enzyme activity, and not easy to volatilize, so as to improve catalytic effect, prolong service life, and reduce recycling volume effect
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Embodiment 1
[0023] Put 100g of soybean oil and 20g of glycerin into the conical flask, then add 15mL of n-hexane, connect the condensing device, carry out magnetic stirring, and mix evenly, as figure 1 As shown, the reactant passed through two packed column reactors (10 cm in length, 1.5 cm in inner diameter, 3 cm in outer diameter, 55° C., with a condenser on top of the column) equipped with Novozyme 435 immobilized lipase at a flow rate of 0.5 mL / min. During the reaction process, the reactants (soybean oil, glycerin and n-hexane) were replenished in good time so as to conform to the ratio of raw materials and solvents in Table 1. Samples of different reaction times were collected respectively, and the organic solvent was removed by vacuum distillation (0.1Mpa, 70°C). , to obtain the product, analyzed by HPLC, the results are shown in Table 2.
Embodiment 2
[0025] Add 100g rapeseed oil and 15g glycerol into the Erlenmeyer flask and mix evenly, then add 18mL No. 6 solvent, carry out magnetic stirring, and the reactant passes through two packed column reactors (length 10cm , inner diameter 1.5cm, outer diameter 3cm, 60°C, with a condenser on top of the column). During the reaction, the reactants (rapeseed oil, glycerol and No. 6 solvent) were replenished in time to meet the ratio of raw materials and solvents in Table 1. All the other operations are the same as in Example 1. The results are shown in Table 2.
Embodiment 3
[0027] 100g of sunflower oil and 10g of glycerol were added into the Erlenmeyer flask and mixed evenly, then 15mL of pentane was added, and magnetically stirred, and the reactant passed through two packed column reactors (length 10cm) equipped with Novozyme 435 immobilized lipase at a flow rate of 1mL / min. , inner diameter 1.5cm, outer diameter 3cm, 50°C, column top with condenser). During the reaction, the reactants (sunflower oil, glycerol and pentane) were replenished in good time to meet the ratio of raw materials and solvents in Table 1. All the other operations are the same as in Example 1. The results are shown in Table 2.
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