Novel synthetic method of halogenated aromatic hydrocarbon
A technology of halogenated aromatic hydrocarbons and synthesis methods, which is applied in the field of preparation of pesticide chemical intermediate products, can solve the problems of low chlorine gas absorption utilization rate and low reaction yield, and achieve remarkable economic and social benefits, convenient operation, Effect of reduction of by-products and exhaust emissions
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Embodiment 1
[0026] (1) Chlorination step: put 630g of p-chlorotoluene into a dehydration kettle, heat to 80°C to remove water to obtain 629g of p-chlorobenzotrifluoride, put it into a 3L chlorination reaction kettle, heat up to 110°C, add 63g of chlorinated Copper catalyst (added in 4 batches, each batch 10-20g), start to pass dry chlorine gas, flow 40-80 m 3 / h, then add the catalyst every 30 minutes, control the temperature at 110-112°C, and the reaction time is 24 hours. After sampling and analyzing the chlorinated material as qualified, stop the chlorine flow. The p-chlorotrichlorotoluene produced by chlorination is pumped into the chlorination tank for use, and the tail gas generated by the reaction is sent to the tail gas absorption device.
[0027] (2) Fluorination step: Press 4 moles of p-chlorotrichlorotoluene and 12 moles of anhydrous hydrogen fluoride into a 3L fluorination reaction kettle, open the frozen brine system, press hydrogen fluoride into the fluorination kettle with...
Embodiment 2
[0031] (1) Chlorination step: put 630g of p-chlorotoluene into the dehydration kettle, heat to 80°C to remove water to obtain 629g of p-chlorobenzotrifluoride, put it into a 3L chlorination reaction kettle, raise the temperature to 110°C, add 60g of chlorinated Copper catalyst (added in 4 batches, 15g in each batch), and dry chlorine gas was introduced at the flow rate of 40-80 m 3 / h, then add the catalyst every 30 minutes, control the temperature at 110-112°C, and the reaction time is 22 hours. After sampling and analyzing the chlorinated material as qualified, stop the chlorine flow. The p-chlorotrichlorotoluene produced by chlorination is pumped into the chlorination tank for use, and the tail gas generated by the reaction is sent to the tail gas absorption device.
[0032] (2) Fluorination step: Press 4 moles of p-chlorotrichlorotoluene and 13 moles of anhydrous hydrogen fluoride into a 3L fluorination reaction kettle, open the frozen brine system, press hydrogen fluorid...
Embodiment 3
[0036] (1) Chlorination step: Put 470kg of p-chlorotoluene into the dehydration kettle and heat it to 80°C to remove water, then pump it into a 3000L chlorination kettle, raise the temperature to 110°C, add 30kg (add in 4 batches, 7-8kg per batch ) cuprous chloride catalyst, and start to feed the chlorine gas vaporized by the gasifier into the chlorination kettle with a flow rate of 40-80 m 3 / h, while cooling water is passed into the jacket of the chlorination kettle, and catalyst is added every half hour, the temperature is controlled at 110-112°C, and the reaction time is 24 hours. After sampling and analyzing the chlorinated material as qualified, stop the chlorine flow. The p-chlorotrichlorotoluene produced by chlorination is pumped into the chlorination tank for use, and the tail gas generated by the reaction is sent to the tail gas absorption device.
[0037] (2) Fluorination step: pump 690kg of p-chlorotrichlorotoluene into the high level tank for metering and put it i...
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