A method and device for preparing tea aroma ketone
A technology of tea aroma ketone and isophorone, which is applied in the field of direct catalytic oxidation of α-isophorone to prepare tea aroma ketone, can solve the problems of low conversion rate and large amount of catalyst, and achieve high conversion rate, conversion rate and No reduction in selectivity and small amount of catalyst
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Embodiment 1
[0024] Add 100 kg of α-isophorone, 3.5 kg of N-hydroxyphthalimide (or 3,4,5,6-tetrachloro-N-hydroxyphthalimide) into the reaction kettle (1) imine 6.5 kg or N-hydroxysuccinimide 2.5 kg), open the condenser, pass oxygen to remove the air in the reactor and pipeline. Close the exhaust valve (6), open the ventilation valve (7), and turn on the air pump (4) to circulate oxygen. The temperature of the reactor was raised to 65°C, and the reaction was carried out for 10 hours. During this period, when the pressure of the pressure gauge (8) decreases, oxygen is supplemented intermittently through the oxygen source (9) to maintain the atmospheric pressure at about 1.0 MPa, and the drain valve (5) is intermittently opened to release the water generated by the reaction to prevent the water level from being too high And return to the reactor (1). After the reaction is completed, the conversion rate of α-isophorone in the reaction kettle is 34-38% according to gas phase analysis, and the...
Embodiment 2
[0026] Add 100 kg of α-isophorone and 12 kg of N-hydroxyphthalimide into the reaction kettle (1), open the condenser, and ventilate the air in the reaction kettle and the pipeline through oxygen. Close the exhaust valve (6), open the ventilation valve (7), and turn on the air pump (4) to circulate oxygen. The temperature of the reaction kettle was raised to 95° C., and the reaction was carried out for 5 hours. During this period, when the pressure of the pressure gauge (8) decreases, oxygen is supplemented intermittently through the oxygen source (9) to maintain the atmospheric pressure at about 1.0 MPa, and the drain valve (5) is intermittently opened to drain water to prevent water from flowing back into the reactor (1) . After the reaction was completed, the conversion rate of α-isophorone in the reaction kettle was analyzed by gas phase to be 45%, and the selectivity of tea aroma ketone was 81%.
Embodiment 3
[0028] Add 100 kg of α-isophorone and 6 kg of N-hydroxyphthalimide into the reaction kettle (1), open the condenser, open the exhaust valve (6), close the vent valve (7), and open Air pump (4) feeds air. The temperature of the reaction kettle was raised to 55° C., and the reaction was carried out for 15 hours. Open the drain valve (5) intermittently to release the water generated by the reaction, so as to prevent the water level from returning to the reactor (1) due to excessive water level. After the reaction was completed, the conversion rate of α-isophorone in the reaction kettle by gas phase analysis was 35%, and the selectivity of tea aroma ketone was 91%.
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