Method for producing functional grease containing rich phytosterin ester from high-acid-value vegetable oil
A technology of phytosterol esters and high-acid value oils, which is applied in the direction of fermentation, can solve problems that have not yet been involved, and achieve the effects of reducing chemical deacidification steps, simple equipment, and mild reaction conditions
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Embodiment 1
[0025] A method for producing functional oil rich in phytosterol esters by utilizing high acid value vegetable oil, comprising the steps of:
[0026] (1) Pretreatment of raw materials: the reaction solvent (n-hexane) is dehydrated by anhydrous sodium sulfate (moisture<0.1wt%), and sitosterol (phytosterol) is vacuum-dried at 80°C for 12h (moisture<1wt%), high acid value The oil is rice bran oil (moisture <0.2wt%, acid value 20mgKOH / g);
[0027] (2) Input of reaction raw materials: 5L n-hexane, 207g phytosterol (sitosterol, 100mM), rice bran oil 1400g (acid value 20mgKOH / g, containing free fatty acid 100mM), molecular sieve (addition is 50g / L, i.e. 250g ) into the reaction kettle, adding 200ppm of natural vitamin E antioxidant, heating to 45°C, stirring and ultrasonic treatment (the time is 30 minutes, the power of ultrasonic treatment is 100w, and the ultrasonic frequency is 25Hz) to obtain a premix;
[0028] (3) Enzymatic transesterification reaction: add 25g (5g / L) Candida a...
Embodiment 2
[0031] A method for producing functional oil rich in phytosterol esters by utilizing high acid value vegetable oil, comprising the steps of:
[0032] (1) Pretreatment of raw materials: the reaction solvent (isooctane) adopts anhydrous sodium sulfate to remove water (moisture<0.1wt%), stigmasterol (phytosterol) is vacuum-dried at 100°C for 10h (moisture<1wt%), high acid Wheat germ oil (moisture <0.2wt%, acid value 40mgKOH / g) for oil and fat;
[0033] (2) Putting in the reaction raw materials: with 5L isooctane, 414g phytosterol (stigmasterol 200mM), 700g of wheat germ oil (acid value 40mgKOH / g, containing free fatty acid 100mM), molecular sieve (addition is 50g / L, namely 250g), add fat-soluble tea polyphenol antioxidant 150ppm, add to the reaction kettle, heat to 55 ° C, stir and sonicate (the time is 50 minutes, the power of sonication is 200w, and the ultrasonic frequency is 30Hz), to obtain the premix;
[0034](3) Enzymatic transesterification: 100 g (20 g / L) of Candida ant...
Embodiment 3
[0037] A method for producing functional oil rich in phytosterol esters by utilizing high acid value vegetable oil, comprising the steps of:
[0038] (1) Pretreatment of raw materials: the reaction solvent (n-heptane) uses anhydrous sodium sulfate to remove water (moisture<0.1wt%), brassicasterol is vacuum-dried at 120°C for 8h (moisture<wt%), and the high acid value oil is used Rice bran oil (moisture <0.2wt%, acid value 100mgKOH / g);
[0039] (2) Input of reaction raw materials: with 5L n-heptane, 828g phytosterol (brassicasterol 400mM), rice bran oil 280g (acid value 100mgKOH / g, containing fatty acid 80mM), molecular sieve (addition is 50g / L, namely 250g ), adding L ascorbyl palmitate antioxidant 200ppm, adding to the reaction kettle, heating to 60°C, stirring and ultrasonic treatment (the time is 60 minutes, the power of ultrasonic treatment is 300w, and the ultrasonic frequency is 40Hz), to obtain the premix;
[0040] (3) Enzymatic transesterification reaction: 200 g (40 ...
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