Preparation method for epoxidized plant oil
A technology for epoxidized vegetable oil and vegetable oil, which is applied in the field of enzymatic preparation of epoxidized vegetable oil, can solve the problems of many side reactions and low yield in the epoxidation process, and achieves good economy and environmental protection, high yield and process simple effect
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Embodiment 1
[0024] Add soybean oil 900g in reaction vessel, hydrogen peroxide (containing hydrogen peroxide 30%) 500g (the mol ratio of hydrogen peroxide and soybean oil is about 6:1), partial glyceride lipase Lipase G50 (purchased from Japan Amano company) 9 g, 900 g of glycerin, and the epoxidation reaction was carried out in a constant temperature magnetic stirrer at 45° C. at a stirring speed of 600 rpm for 24 h. After the reaction is over, the reaction mixture is centrifuged or settled to separate and recover the oil phase and the glycerin phase. After testing, its acid value is 0.25 and epoxy value is 5.3. The content of epoxy fatty acid triglyceride in the product analyzed by liquid chromatography-mass spectrometry is 98.5%, and the content of epoxy fatty acid diglyceride and monoester is 1.2%.
Embodiment 2
[0026] Add soybean oil 900g in reaction vessel, hydrogen peroxide (containing hydrogen peroxide 30%) 500g (the mol ratio of hydrogen peroxide and soybean oil is about 6:1), 9g partial glyceride lipase Lipase SMG1, glycerol 900g, at 30 The epoxidation reaction was carried out at a constant temperature magnetic stirrer at 600 rpm for 24 h. After the reaction is over, the reaction mixture is centrifuged or settled to separate and recover the oil phase and the glycerin phase. After testing, its acid value is 0.14 and epoxy value is 5.1. The content of epoxy fatty acid triglyceride in the product analyzed by liquid chromatography-mass spectrometry was 98.7%, and the content of epoxy fatty acid diglyceride and monoester was 1.3%.
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