A method for producing functional oil rich in phytosterol esters by utilizing high acid value vegetable oil
A technology for phytosterol esters and high-acid-value oils and fats, applied in the direction of fermentation, etc., can solve the problems that have not yet been involved, and achieve the effects of reducing chemical deacidification steps, simple equipment, and not easy to be oxidized.
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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 content<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) Ca...
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) Input of reaction raw materials: 5L isooctane, 414g phytosterol (stigmasterol 200mM), wheat germ oil 700g (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 perform ultrasonic treatment (the time is 50 minutes, the power of ultrasonic treatment is 200w, and the ultrasonic frequency is 30Hz) to obtain a premix;
[0034](3) Enzymatic transesterification: 100 g (20 g / L) of ...
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
[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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