Method for preparing methyl oleate from vegetable oil under catalysis of silicon dioxide-supported heteropolyacid
A technology of immobilized heteropolyacid and silica, which is applied in the direction of fatty acid esterification, etc., can solve the problems of difficult separation of catalyst and product, complicated process, and many impurities
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Embodiment 1
[0018] 1g solid catalyst (the mass ratio of phosphotungstic heteropolyacid and silicon dioxide is 1: 50), 30g soybean oil, and 3g methanol are put into the flask, stirred, heated, the reaction temperature is 70°C, and the reaction time is 3 hours. After the reaction was cooled, the catalyst was removed by filtration and vacuum distillation. The yield of methyl oleate was 30.2%.
Embodiment 2
[0020] 3g solid catalyst (the mass ratio of phosphotungstic heteropolyacid and silicon dioxide is 1: 50), 30g soybean oil, and 3g methanol are put into the flask, stirred, heated, and the reaction temperature is 70°C, and the reaction time is 3 hours. After the reaction was cooled, the catalyst was removed by filtration and vacuum distillation, the yield of methyl oleate was 38.3%.
Embodiment 3
[0022] 1g solid catalyst (the mass ratio of phosphotungstic heteropolyacid and silicon dioxide is 1: 10), 30g soybean oil, and 3g methanol are put into the flask, stirred, heated, the reaction temperature is 70°C, and the reaction time is 3 hours. After the reaction was cooled, the catalyst was removed by filtration and vacuum distillation, the yield of methyl oleate was 52.3%.
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