Process for preparing biodiesel and nervonic acid by using purpleblow maple oil as raw material
A technology of biodiesel and maple ingot, applied in the direction of biofuel, biological raw materials, chemical instruments and methods, etc., can solve the problems of ineffective use of by-products and high energy consumption, increase comprehensive utilization benefits, simple production process, The effect of reducing production costs
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Embodiment 1
[0016] Put 400g of maple ingot refined oil and 120g of methanol into a 1000ml three-neck round bottom flask, place it in an electric heating constant temperature jacket, stir evenly, and then add 8g of SO 4 2- / ZrO 2 , heated to 70 ° C, stirred and refluxed, and reacted for 3 hours, then stopped heating and stirring. The reactants were then poured into a centrifuge cup and centrifuged to separate the SO 4 2- / ZrO 2 , the crude methyl ester and crude glycerin were left to separate layers, and the upper layer was distilled to remove methanol, and was distilled in a distillation pot with a pressure of 1250 Pa and a temperature of 170 ° C to obtain 396 g of biodiesel. The mass fraction of fatty acid methyl ester in the biodiesel product determined by gas chromatography is 99.2%, which is in line with the main performance index of 0# diesel. Methanol was distilled off in the lower layer to obtain 39.5 g of glycerin. The bottom liquid was further distilled under the conditions...
Embodiment 2
[0018] Put 400g of maple ingot refined oil and 140g of ethanol into a 1000ml three-necked round-bottomed flask, place it in an electric heating thermostat, stir evenly, and then add 8g of SO 4 2- / ZrO 2 , heated to 80°C, stirred and refluxed, and reacted for 3 hours, then stopped heating and stirring. The reactants were then poured into a centrifuge cup and centrifuged to separate the SO 4 2- / ZrO 2 , the crude methyl ester and crude glycerin were left standing to separate layers, the upper layer was distilled to remove methanol, and the pressure was 500 Pa, and the temperature was distilled in a distillation pot at a temperature of 140° C. to obtain 394 g of biodiesel. The mass fraction of fatty acid methyl ester in the biodiesel product determined by gas chromatography is 98.4%, which is in line with the main performance index of 0# diesel. Methanol was distilled off in the lower layer to obtain 39.0 g of glycerin. The bottom liquid was further distilled at a pressure ...
Embodiment 3
[0020] Put 400g Yuanbao maple refined oil and 120g methanol into a 1000ml three-neck round bottom flask, place it in an electric heating constant temperature jacket, stir evenly, and then add 6g SO 4 2- / TiO 2 , heated to 70°C, stirred and refluxed, and stopped heating and stirring after reacting for 4 hours. The reactants were then poured into a centrifuge cup and centrifuged to separate the SO 4 2- / TiO 2 , the crude methyl ester and crude glycerin were left to stand and layered, the upper layer was distilled to remove methanol, and distilled in a distillation still with a pressure of 2000Pa and a temperature of 200°C to obtain 395g of biodiesel, and the fatty acid formaldehyde in the biodiesel product obtained was determined by gas chromatography. The mass fraction of ester is 99.1%, which meets the main performance index of 0# diesel. Methanol was distilled off in the lower layer to obtain 38.5 g of glycerin. The bottom liquid was further distilled under the conditio...
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