Method for continuously synthesizing citral through tubular reactor
A tubular reactor, citral technology, applied in chemical instruments and methods, preparation of organic compounds, preparation of carbon-based compounds, etc., can solve the problems of low catalyst activity, unsuitable for industrial production, harsh reaction conditions, etc. The effect of continuous reaction, small equipment footprint, and simple equipment
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Embodiment 1
[0026] Add 500 g of dehydrolinalool and 2 g of cuprous bromide successively to a 1000 mL one-necked bottle, stir evenly, heat to 80°C until cuprous bromide is completely dissolved in the solution, and then add 8 g of acetylacetonate oxide to the solution Titanium and 40 g of cinnamic acid were stirred evenly, and the above-mentioned mixed solution was injected into a tubular reactor preheated to 160 °C through a syringe pump, and the flow rate was controlled at 75 mL / min. The time for the solution to flow through the tubular reactor was For 2 min, through gas chromatography detection and analysis, the conversion rate of raw material dehydrolinalool is 100%, and the product citral content is 92%. The solution flowing out through the tubular reactor is collected, and 450 g citral is obtained by rectification under reduced pressure. , the yield is 90%.
Embodiment 2
[0028] Add 500 g of dehydrolinalool and 2 g of cuprous chloride to a 1000 mL single-necked bottle in sequence, stir evenly, heat to 80°C until cuprous bromide is completely dissolved in the solution, and then add 8 g of acetylacetonate oxide to the solution Titanium and 40 g of cinnamic acid were stirred evenly, and the above-mentioned mixed solution was injected into a tubular reactor preheated to 160 °C through a syringe pump, and the flow rate was controlled at 75 mL / min. The time for the solution to flow through the tubular reactor was For 2 min, through gas chromatography detection and analysis, the conversion rate of raw material dehydrolinalool is 100%, and the product citral content is 91%. The solution flowing out through the tubular reactor is collected, and 445 g citral is obtained by rectification under reduced pressure. , the yield is 89%.
Embodiment 3
[0030] Add 500 g of dehydrolinalool and 2 g of cuprous chloride to a 1000 mL single-necked bottle in sequence, stir evenly, heat to 80°C until cuprous bromide is completely dissolved in the solution, and then add 5 g of acetylacetonate oxide to the solution Titanium and 30 g of sorbic acid were stirred evenly, and the above-mentioned mixed solution was injected into a tubular reactor preheated to 160°C through a syringe pump, and the flow rate was controlled at 50 mL / min. The time for the solution to flow through the tubular reactor was For 3 min, through gas chromatography detection and analysis, the conversion rate of raw material dehydrolinalool is 100%, and the product citral content is 89%. The solution flowing out through the tubular reactor is collected, and 440 g citral is obtained by rectification under reduced pressure. , the yield is 88%.
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