A kind of photooxidative preparation method of haloacetyl chloride
A halogenated acetyl and photooxidation technology, applied in the field of photooxidative preparation of halogenated acetyl chloride, can solve the problems of reducing the utilization rate of raw materials, harsh reaction conditions, easy by-products and the like, and achieves the improvement of utilization rate of raw materials and reaction conditions. Mild, avoids the effect of acid chloride photolysis
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Embodiment 1
[0035] A copper sulfate solution with a concentration of 35.0g / L is poured into the quartz cold trap continuously and circularly at a flow rate of 11L / min as a filter solution to filter out ultraviolet light with a wavelength of less than 300nm. Oxygen and HCFC-123 are injected into the mixer at a molar ratio of 1.5:1, mixed and vaporized, and then passed into the reactor for photooxidation reaction. The reaction temperature is 40°C, the residence time is 3s, and the power of the metal halide lamp is 700W. The reaction has been running continuously for one month, and the reactor and components have no obvious corrosion. Sampling and analysis at the outlet of the reactor showed that the conversion rate of HCFC-123 was 97.1%, and the selectivity of trifluoroacetyl chloride was 99.6%.
Embodiment 2
[0037] A copper sulfate solution with a concentration of 20.0g / L is continuously injected into the quartz cold trap with a flow rate of 10L / min as a filter solution to filter out ultraviolet light with a wavelength of less than 300nm. Ozone and HCFC-123 are injected into the mixer at a molar ratio of 1.5:1, mixed and vaporized, and then passed into the reactor for photooxidation reaction. The reaction temperature is 30°C, the residence time is 3s, and the power of the high-pressure mercury lamp is 700W. The reaction has been running continuously for one month, and the reactor and components have no obvious corrosion. Sampling and analysis at the outlet of the reactor showed that the conversion rate of HCFC-123 was 98.3%, and the selectivity of trifluoroacetyl chloride was 99.9%.
Embodiment 3
[0039] A copper sulfate solution with a concentration of 50.0g / L is continuously injected into the quartz cold trap at a flow rate of 22L / min as a filter solution to filter out ultraviolet light with a wavelength of less than 300nm. Oxygen and HCFC-132a are injected into the mixer at a molar ratio of 2.5:1, mixed and vaporized, and then passed into the reactor for photooxidation reaction. The reaction temperature is 50°C, the residence time is 6s, and the power of the medium-pressure mercury lamp is 500W. The reaction has been running continuously for one month, and the reactor and components have no obvious corrosion. Sampling and analysis at the outlet of the reactor showed that the conversion rate of HCFC-132a was 96.6%, and the selectivity of difluoroacetyl chloride was 99.5%.
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