Method for preparing biological diesel oil by using solid acid base double-function catalyst
An acid-base dual function, biodiesel technology, applied in chemical instruments and methods, physical/chemical process catalysts, biofuels, etc., can solve the problems of complex post-treatment process, difficult separation of methanol and by-product glycerol, and high equipment requirements
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Embodiment 1
[0017] In a 500ml three-necked bottle, add 100.00g of rapeseed crude oil and the required amount of methanol according to the ratio of alcohol to oil molar ratio of 40:1, and when the temperature reaches 65°C under mechanical stirring, add 20% of rapeseed crude oil Al 2 o 3 -K 2 CO 3 Catalyst 20.0g, react for 10 hours at 60-65°C under normal pressure, then filter to separate the solid catalyst Al 2 o 3 -K 2 CO 3 , the liquid phase is distilled to recover methanol, and then the liquid phase is transferred to a separatory funnel and left to stand. The upper layer is crude biodiesel, and the lower layer is the by-product glycerin. The composition of crude biodiesel was analyzed by gas phase, and the content of fatty acid methyl ester was 98.1%.
Embodiment 2
[0019] In a 500ml three-necked bottle, add 100.00g of animal and vegetable oils and fats, gutter oils, catering waste oils, waste oils, oily crops, oily plants, microbial fermented oils, microalgae oils, and oils at a molar ratio of alcohol to oil of 3:1. Deodorized distillate, oil bottoms, acidified oil, any one or a mixture of several of them and the required amount of methanol, add 5% of the mass of the raw oil Al under mechanical stirring 2 o 3 -K 2 CO 3 Add 5.0 g of catalyst, add 30 mL of tetrahydrofuran, and react for 0.5 hour at a pressure of 25 MPa and a reaction temperature of 300° C. After the reaction is finished, filter while hot to separate the solid catalyst Al 2 o 3 -K 2 CO 3 , the liquid phase is distilled to recover methanol, the liquid phase is transferred to a separatory funnel, and left to stand, the upper layer is crude biodiesel, and the lower layer is the by-product glycerin. The composition of the mixture is analyzed by gas phase, and the content...
Embodiment 3
[0021]In a 500ml three-necked bottle, add 100.00g of rapeseed crude oil and the required amount of methanol according to the ratio of alcohol to oil molar ratio of 15:1, and when the temperature reaches 65°C under mechanical stirring, add 0.1% of the raw material oil The bifunctional catalyst is 0.1 g, and the reaction temperature is 60-65° C., and the reaction time is 4 hours under normal pressure. After the reaction is completed, filter while it is hot to separate the solid catalyst, re-distill the liquid phase to recover methanol, transfer the liquid phase to a separatory funnel, and let it stand still. The upper layer is crude biodiesel, and the lower layer is the by-product glycerin. Composition of the mixture through gas phase analysis, the content of fatty acid methyl ester in crude biodiesel is more than 90.0% (wherein using bifunctional catalyst Al 2 o 3 -SiO 2 -KCl, the content of fatty acid methyl ester is 92.1%).
[0022] The above bifunctional catalyst is Cs-Ba...
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