Method for synthesizing 2, 5-dichlorobenzotrifluoride through continuous flow catalytic chlorination
A technology of dichlorotrifluorotoluene, stream synthesis, applied in chemical instruments and methods, organic chemistry, halogenated hydrocarbon preparation and other directions, to achieve the effects of stable product quality, stable production process and broad application prospects
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Embodiment 1
[0036] Embodiment 1, utilize continuous flow reactor to synthesize the method for 2,5-dichlorobenzotrifluoride
[0037] The continuous flow reactor includes a gas-liquid mixing module, a reaction module, and a gas-liquid separation module connected in sequence. The reaction scheme is as follows:
[0038]
[0039] The reaction operates as follows:
[0040] Take 50g of o-chlorobenzotrifluoride, mix with 5g of ferric chloride and 0.5g of bromobenzene evenly, transport it into the gas-liquid mixing module through a metering pump, and the flow rate is 10mL / min; transport chlorine gas into the gas-liquid mixing module through a gas flow meter, The flow rate is 6L / min. After staying in the gas-liquid mixing module for 0.5 minutes, enter the reaction module for a full reaction. The residence time in the reaction module is 10 minutes, and the temperature of the gas-liquid mixing module and the reaction module is set to 0°C. Then enter the gas-liquid separation module to collect t...
Embodiment 2
[0042] Embodiment 2, utilize continuous flow reactor to synthesize the method for 2,5-dichlorobenzotrifluoride
[0043] Referring to the method of Example 1, 2,5-dichlorobenzotrifluoride was synthesized by using a continuous flow reactor, the only difference being that no cocatalyst bromobenzene was added. The GC purity of the pure 2,5-dichlorotrifluorotoluene obtained in Example 2 was 98.5%, and the yield was 55%.
Embodiment 3
[0044] Embodiment 3, utilize continuous flow reactor to synthesize the method for 2,5-dichlorobenzotrifluoride
[0045] Referring to the method of Example 1, 2,5-dichlorobenzotrifluoride was synthesized by using a continuous flow reactor, the only difference being that neither the catalyst ferric chloride nor the promoter ferric chloride was added. The GC purity of the pure 2,5-dichlorobenzotrifluoride obtained in Example 3 was 95.5%, and the yield was 34%.
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