Method for preparing bromo-2-methylpropane through bromination of tertiary butanol in continuous flow micro-channel reactor
A technology of microchannel reactor and channel reactor, which is applied in chemical instruments and methods, preparation of halogenated hydrocarbons, organic chemistry, etc., can solve the problems of large consumption of concentrated sulfuric acid, large consumption of raw materials, environmental pollution, etc., to avoid Severely corroded equipment, reduced generation of waste acid, and excellent corrosion resistance
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Embodiment 1
[0028] (1) Device used: continuous flow microchannel reactor (straight channel functional module + "heart-shaped" structural functional module), refer to image 3 Determine the connection mode of the microchannel reactor, the number of mixed reaction modules is determined according to the flow rate and reaction residence time, and the heat transfer medium is heat transfer oil.
[0029] (2) Set the volume flow rate ratio of each metering pump 4, pump 5, and pump 6 as tert-butanol: hydrobromic acid: concentrated sulfuric acid = 10: 14.5: 5.9, and put the three streams of materials into each straight channel preheating module respectively , set the temperature of the heat exchanger to 60°C; after preheating, pour them into the "heart-shaped" structural functional module for mixing and then react. Finally, the molar ratio of tert-butanol, hydrobromic acid and concentrated sulfuric acid is 1:1:1. The reaction residence time is 95s, the pressure is 1.2bar, and the reaction product ...
Embodiment 2
[0032] (1) Device used: continuous flow microchannel reactor (straight channel functional module + droplet channel), refer to image 3 Determine the connection mode of the microchannel reactor, the number of mixed reaction modules is determined according to the flow rate and reaction residence time, and the heat transfer medium is heat transfer oil.
[0033] (2) Set the volume flow rate ratio of each metering pump 4, pump 5, and pump 6 as tert-butanol: hydrobromic acid: concentrated sulfuric acid = 10: 17.5: 5.9, and put the three streams of materials into the functional modules of each straight channel for pre-treatment. Heat, set the temperature of the heat exchanger to 30°C; after preheating, pour them into the drop-shaped channel of the micro-mixer for mixing and then react. Finally, the molar ratio of tert-butanol, hydrobromic acid and concentrated sulfuric acid is 1:1.2:1. The reaction residence time is 86s, the pressure is 1.6bar, and the reaction product flows out of ...
Embodiment 3
[0036](1) The device used: continuous flow microchannel reactor (straight channel functional module + spherical baffle plate channel), refer to image 3 Determine the connection mode of the microchannel reactor, the number of mixed reaction modules is determined according to the flow rate and reaction residence time, and the heat transfer medium is heat transfer oil.
[0037] (2) Set the volume flow rate ratio of each metering pump 4, pump 5, and pump 6 as tert-butanol: hydrobromic acid: concentrated sulfuric acid = 10: 21.8: 5.9, and put the three streams of materials into the functional modules of each straight channel for pre-treatment. Heat, set the temperature of the heat exchanger to 30 ° C; after preheating, put them into the spherical channel of the micro-mixer with baffle plate for mixing and then react. Finally, the molar ratio of tert-butanol, hydrobromic acid and concentrated sulfuric acid is 1:1.5:1. The reaction residence time is 76s, the pressure is 2bar, and t...
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