Method for preparation of trifluoro acetyl chloride with trifluoroethane chlorinated mixture
A technology of trifluoroacetyl chloride and trifluoroethane, which is applied in the field of compound preparation, can solve problems such as difficult realization and harsh reactor requirements, and achieve the effects of improving production efficiency, shortening time, and reducing equipment investment and energy consumption.
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Embodiment 1
[0020] Add 5L of trifluoroethane chlorination mixture into 10L enamel kettle, the mixture is composed of: 90% trifluorochloroethane, 9% trifluorodichloroethane and 1% trifluorotrichloroethane, inside the reactor A 2kW mercury lamp is installed. Continuously feed oxygen and chlorine under stirring, flow rate is 500ml / min and 400ml / min respectively, turn on mercury lamp after 15 minutes, carry out photochemical oxidation reaction by mercury lamp radiation, react at 0.09Mpa, material bubble point temperature (about 5°C). The reactants are continuously discharged from the gas phase outlet on the upper part of the reactor in the form of gas phase, and the liquid level in the reactor is kept constant by continuously adding trifluoroethane chlorination mixture through the dropping funnel, and the supplementary speed is determined by the reaction rate; the continuously discharged reactants include reaction Vaporized trifluoroethane chlorination mixture, product trifluoroacetyl chlori...
Embodiment 2
[0024] The difference of embodiment 2 reaction and embodiment 1 is that the chlorination mixture among the embodiment 2 consists of: 9% trifluorochloroethane, 90% trifluorodichloroethane and 1% trifluorotrichloroethane, The flow rate of chlorine gas is 250ml / min, and the reaction is carried out at 0.31MPa and the bubble point temperature of the material in the reactor (about 60°C). Other conditions were the same as in Experiment 1, except for trifluoroethane chlorination mixture, oxygen, chlorine and hydrogen chloride gas, trifluoroacetyl chloride accounted for 91% of the gas phase products, and a total of 10.3 mol of trifluoroacetyl chloride was generated. The content of trifluorotrichloroethane in the bottom liquid is 7.14%.
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