Method for preparing biodiesel
A biodiesel and oil technology, applied in biofuels, petroleum industry, liquid carbonaceous fuels, etc., can solve the problems of long processing flow, difficult separation of fatty acid ester layer and glycerin layer, and large amount of acid catalysts, etc. The effect of reducing the production of soap
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Embodiment 1
[0022] Add waste oil and methanol with an acid value of 29mgKOH / g into the autoclave together, the mass ratio of alcohol to oil is 0.17:1, add zinc hydroxide with a weight of 0.6% of the grease as a catalyst, and stir in the autoclave at a temperature of 140°C and a pressure of 0.7Mpa. Under the condition of a speed of 200 rpm, react for 3.5 hours to obtain a crude reaction product for distillation, remove excess methanol at the bottom of the kettle < 150°C, recover and reuse methanol, and separate the remaining materials into the glycerin phase. The mixed ester phase was distilled under reduced pressure to obtain biodiesel with a yield of 95.1% and an acid value of 3.6 mgKOH / g.
Embodiment 2
[0024] Add waste oil with an acid value of 66mgKOH / g and methanol together into the autoclave, the mass ratio of alcohol to oil is 0.20:1, add zinc hydroxide with a weight of 0.9% of the grease as a catalyst, and stir in the autoclave at a temperature of 120°C and a pressure of 0.4Mpa. Under the condition of a speed of 200 rpm, react for 3.5 hours to obtain a crude reaction product for distillation, remove excess methanol at the bottom of the kettle < 150°C, recover and reuse methanol, and separate the remaining materials into the glycerin phase. The mixed ester phase was distilled under reduced pressure to obtain biodiesel with a yield of 93.5% and an acid value of 0.97 mgKOH / g.
Embodiment 3
[0028] Add waste oil and methanol with an acid value of 66mgKOH / g into the autoclave together, the mass ratio of alcohol to oil is 0.20:1, add zirconium hydroxide with 0.9% of the weight of grease as a catalyst, and stir in the autoclave at a temperature of 140°C and a pressure of 0.7Mpa. Under the condition of a speed of 200 rpm, react for 3.5 hours to obtain a crude reaction product for distillation, remove excess methanol at the bottom of the kettle < 150°C, recover and reuse methanol, and separate the remaining materials into the glycerin phase. The mixed ester phase was distilled under reduced pressure, and the yield of biodiesel was 49%.
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