Method for preparing fatty glyceride
A technology of fatty acid glycerides and free fatty acids, which is applied in the field of synthetic fatty acid glycerides, can solve the problems of long time required for equilibrium and low conversion rate of fatty acids, and achieve the effects of reducing separation and purification steps, increasing conversion rate, and high efficiency
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Embodiment 1
[0025] Embodiment 1 (two-step enzymatic method)
[0026] The fatty acid by-products in deep-sea fish oil processing are taken as raw materials, and the fatty acid content is 99.5%, and the DHA content is 20% and the EPA content is 22%. Take 100g of this fatty acid and 100g of glycerin and mix them in a reaction vessel, add 4g of Lipozyme TL 100L (a lipase derived from Thermomyces lanuginosus) and 5g of water, put them in a glycerin bath at 50°C and react for 2h under stirring , The reaction esterification rate detected by liquid chromatography is 62%. Centrifuge the oil phase and glycerol phase in the above reaction, keep the glycerol phase for recycling, and dehydrate the oil phase; take 100g of the above oil phase and place it in a reaction vessel, add 1.6g Novozym435 lipase (a lipase derived from Candida antarctica) ), placed in a constant temperature magnetic stirrer at 55°C, and stirred and reacted for 5h under a vacuum of 100pa to obtain a reaction product, which was de...
Embodiment 2
[0027] Embodiment 2 (two-step enzymatic method)
[0028] Get the deodorized effluent in the deodorization and refining process of soybean oil as the reaction raw material, wherein the fatty acid content is 91.3%, get the compound 500g, glycerol 600g, water 11g, 5 g of L (lipase derived from Candida antarctica) was mixed and then placed in a reactor at 50° C. for a stirring reaction for 4 hours. The esterification rate of this reaction was detected by liquid chromatography to be 59%. The oil phase and glycerin phase in the above reaction were separated by centrifugation, the glycerin phase was retained for recycling, and the oil phase was dehydrated; 300 g of the above oil sample was added to 10 g of Novozym 435 lipase, stirred and reacted under 100 Pa vacuum for 4 hours to obtain the reaction product, the liquid phase Chromatographic detection shows that in the product at this time, the TAG content is 41.5%, the DAG content is 52.27%, the MAG is 3.51%, and the FFA is 2.74%. T...
Embodiment 3
[0029] Embodiment 3 (two-step enzymatic method)
[0030] Take acidified oil, a by-product of soybean oil refining, in which the fatty acid content is 51.5%, and the triglyceride content is 48.3%. Take 500g of the compound, 250g of glycerin, 11g of water, 5g of Lipozyme TL 100L lipase, mix and place in the reactor The reaction was stirred at 45°C for 4h. Centrifuge the oil phase and glycerin phase in the above reaction, keep the glycerin phase for recycling, and dehydrate the oil phase; take 400g of the above oil sample, add 8g of Novozym435 lipase, stir and react under 100Pa vacuum for 4h to obtain the reaction product, liquid chromatography It was detected that in the product at this time, the TAG content was 66.5%, the DAG content was 30.27%, the MAG content was 2.09%, and the FFA content was 1.14%; the esterification rate of fatty acid was 97.78%.
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