Preparation method of high-purity triglyceride type PUFA (Polyunsaturated Fatty Acid)
A triglyceride, high-purity technology, applied in the field of preparation of high-purity triglyceride-type PUFA, can solve the problem of low triglyceride purity, achieve good economy and environmental protection, and avoid oxidation
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Embodiment 1
[0021] Add glycerin 100g, PUFA concentrate 1000g (from tuna oil, PUFA composition is ALA 1.6%, AA 9.8%, EPA 7.8%, DPA 16.4%, DHA 50.8%), 10g lipase Novozym435, 20g molecular sieve (remove The moisture generated by the esterification reaction), the esterification reaction was carried out in a constant temperature magnetic stirrer at 50° C. at a stirring speed of 200 rpm. After the reaction is over, the reaction mixture is centrifuged or filtered to separate Novozym435, centrifuged to remove unreacted glycerol, and the esterification reaction product is recovered. The triglyceride content in the esterified product was analyzed by liquid chromatography to be 69.7%, the diglyceride content was 11.2%, the monoglyceride content was 4.7%, and the remaining fatty acid was 14.4%. After testing, the peroxide value of the oil phase is 2.1meq / Kg. Add 100g water and 10g partial glyceride lipase Lipase SMG1 to the esterification product (Wang W-f, Li T, Qin X-l, Ning Z-x, Yang B, Wang Y-h....
Embodiment 2
[0023] Add glycerin 100g, PUFA concentrate 1000g (from tuna oil, PUFA composition is ALA 1.6%, AA 9.8%, EPA 7.8%, DPA 16.4%, DHA 50.8%), 10g lipase Novozym435, 20g molecular sieve to remove reaction vessel The generated moisture was esterified in a constant temperature magnetic stirrer at 50° C. at a stirring speed of 200 rpm. After the reaction is over, the reaction mixture is centrifuged or filtered to separate Novozym435, centrifuged to remove unreacted glycerol, and the esterification reaction product is recovered. The triglyceride content in the esterified product was analyzed by liquid chromatography to be 69.7%, the diglyceride content was 11.2%, the monoglyceride content was 4.7%, and the remaining fatty acid was 14.4%. After testing, the peroxide value of the oil phase is 2.1meq / Kg. 100 g of water and 10 g of partial glyceride lipase Lipase SMG1 were added to the esterification product, and the hydrolysis reaction was carried out in a constant temperature magnetic st...
Embodiment 3
[0025]Add 100g of glycerin, 900g of CLA ethyl ester concentrate (CLA content is 80.3%), 10g of lipase Novozym435 into the reaction vessel, and carry out esterification at a constant temperature magnetic stirrer at 50°C at a stirring speed of 200rpm under a vacuum of 100Pa reaction. After the reaction is over, the reaction mixture is centrifuged or filtered to separate Novozym435, centrifuged to remove unreacted glycerol, and the esterification reaction product is recovered. The content of triglyceride in the esterified product was analyzed by liquid chromatography to be 70.5%; the content of diglyceride was 11.5%; the content of monoglyceride was 4.4%; and the remaining fatty acid was 13.6%. After testing, the peroxide value of the oil phase is 2.0meq / Kg. 100 g of water and 10 g of partial glyceride lipase Lipase SMG1 were added to the esterification product, and the hydrolysis reaction was carried out in a constant temperature magnetic stirrer at 2° C. at a stirring speed of...
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