Method for continuous production of hexafluoroacetone
A technology of hexafluoroacetone and hexafluoropropylene, which is applied in the field of continuous production of hexafluoroacetone, can solve the problems of difficult control of the reaction process, low conversion rate and selectivity, and influence on product quality, so as to avoid overheating, improve selectivity and The effect of conversion rate and excellent mass transfer effect
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Embodiment 1
[0038] AlCl 3Prepare a suspension with hydrofluoroether at a mass ratio of 1:50, heat the suspension through a heat exchanger to a reaction temperature of 60°C, pump it into a circulating loop reactor, and mix oxygen and hexafluoropropylene at a mass ratio of 5:1 Configure the mixed gas, pass the mixed gas into the reactor through the compressor, the mass ratio of the mixed gas and the catalyst suspension is 1:30, the reaction temperature is controlled at 50°C, the injection speed of the Venturi mixer is 70m / s, and the reaction stays The time is 5 minutes, the gas part is extracted, and the finished product of hexafluoroacetone is obtained after low-temperature rectification. The reaction conversion rate and selectivity are respectively 98.20% and 99.45% through gas chromatography detection. After 5 cycles of the reaction solution, the reaction conversion rate and selectivity sex were 97.02%, 98.86%.
Embodiment 2
[0040] AlCl 3 , KF and hydrofluoroether to prepare a suspension according to the mass ratio of 1:1:100, heat the suspension through a heat exchanger to a reaction temperature of 60°C, pump it into a circulating loop reactor, and mix oxygen and hexafluoropropylene by mass The mixed gas is configured at a ratio of 3:1, and the mixed gas is fed into the reactor through the compressor. The mass ratio of the mixed gas and the catalyst suspension is 1:20, the reaction temperature is controlled at 60°C, and the injection speed of the Venturi mixer is 70m / s, the reaction residence time is 3min, the gas part is taken out, and the finished product of hexafluoroacetone is obtained after low-temperature rectification. The reaction conversion rate and selectivity are respectively 98.90% and 99.03% through gas chromatography detection. After 8 cycles of the reaction solution, the reaction The conversion and selectivity were 97.38% and 98.93%, respectively.
Embodiment 3
[0042] AlCl 3 , AgI and fluorocarbon according to the mass ratio of 1:1:300 to prepare a suspension, heat the suspension through a heat exchanger to a reaction temperature of 60°C, pump it into the circulation loop reactor, and mix oxygen and hexafluoropropylene according to the mass ratio The mixed gas is configured at 1:1, and the mixed gas is fed into the reactor through the compressor. The mass ratio of the mixed gas and the catalyst suspension is 1:10, the reaction temperature is controlled at 60°C, and the injection speed of the Venturi mixer is 50m / s , the reaction residence time is 5min, the gas part is produced, and the finished product of hexafluoroacetone is obtained after low-temperature rectification. The reaction conversion rate and selectivity are respectively 98.63% and 99.52% through gas chromatography detection. After 6 cycles of the reaction solution, the reaction conversion The rate and selectivity were 97.68% and 99.03%, respectively.
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