Process for preparing diglyceride by enzyme method in organic medium system
A technology of diglyceride and enzymatic preparation, applied in biofuel, fermentation and other directions, can solve the problems of high viscosity of reaction substrate, slow reaction speed, lipase coating, etc., achieve easy separation, reduce negative effects, and improve enzyme effect of reactivity
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Embodiment 1
[0027] Be that the methyl alcohol of 1.5: 1 and 10g of jatropha oil and the tert-butanol based on oil volume 100% are packed into a stoppered Erlenmeyer flask and mixed uniformly, and placed in a reciprocating shaker that can automatically control the temperature and heated to 40 After ℃, add immobilized lipase Lipozyme TL with 5% oil mass to start the reaction, and filter and recover the immobilized lipase after 10 hours for reuse. The product is subjected to simple distillation to remove tert-butanol and methanol, and then 110°C vacuum distillation to remove residual tert-butanol and methanol, and then undergoes molecular distillation at 0.5Pa and 150°C to obtain fatty acid methyl ester and glyceride fractions respectively. Fatty acid methyl esters can be used as biodiesel, and glyceride fractions can be used as healthy oils and fats. The mass percentage of each component in the glyceride fraction is as follows: triglyceride 32.5%, diglyceride 53.4%, monoglyceride 13.8%, fre...
Embodiment 2
[0029] Ethanol and cottonseed oil (cottonseed oil 10g) with a molar ratio of 2:1, tert-butanol based on 120% of the oil volume, are packed into a stoppered Erlenmeyer flask and mixed evenly, and placed in a reciprocating shaker that can automatically control the temperature After heating to 60° C., 3% of the immobilized lipase Novozym 435 based on the oil mass was added to start the reaction, and after 6 hours, the immobilized lipase was recovered by filtration and reused. The product is subjected to simple distillation to remove tert-butanol and ethanol, and then 110°C vacuum distillation to remove residual tert-butanol and ethanol, and then undergoes molecular distillation at 0.5Pa and 150°C to obtain fatty acid ethyl ester and glyceride fractions respectively. Fatty acid ethyl esters can be used as biodiesel, and glyceride fractions can be used as healthy oils and fats. The mass percent content of each component in the glyceride fraction is as follows: triglyceride 22.1%, d...
Embodiment 3
[0031] Butanol and yeast fat (yeast fat 10g) with a molar ratio of 1:1, tert-butanol based on the fat volume of 60%, are packed into a stoppered Erlenmeyer flask and mixed evenly, and placed in a reciprocating shaker with automatic temperature control After heating to 35°C, 3% of the immobilized lipase Lipozyme RM based on the mass of the oil and 5% of the immobilized lipase Lipozyme TL based on the mass of the oil were added to start the reaction. After 15 hours, the immobilized lipase was recovered by filtration and reused. The product undergoes simple distillation to remove tert-butanol and butanol, and then undergoes vacuum distillation at 110°C to remove residual tert-butanol and butanol, and then carries out molecular distillation at 0.5 Pa and 150°C to obtain fatty acid butyl ester and glyceride fractions respectively. Fatty acid butyl esters can be used as biodiesel, and glyceride fractions can be used as healthy oils and fats. The mass percent content of each componen...
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