A kind of method for preparing 2,5-dichloronitrobenzene by continuous nitration
A technology of dichloronitrobenzene and p-dichlorobenzene, which is applied in 2 fields, can solve the problems of an emulsified layer at the interface of an oil phase and an acid phase, a large amount of waste acid circulating, and achieves stable product quality, improvement of reaction modulus, and suppression of The effect of emulsification
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[0024] 1. The production device is composed of 3 nitration kettles and 1 extraction kettle. The total volume of the 3 nitration kettles is 2.5m3 and 1.5m3 respectively. 3 、1.5m 3 , the effective volume is: 1.2m 3 、1.1m 3 、1.1m 3 ; The total volume of the extraction kettle is 1.5m 3 , the effective volume is 1.1m 3 , process control 1 # Nitrification tank temperature 58 ~ 62 ℃, 2 # Nitrification tank temperature 65 ~ 68 ℃; 3 # The temperature of the nitration tank is 65-68°C; the temperature of the extraction tank is 68-70°C; the reaction modulus is 3-4, and the concentration of sulfuric acid is 82-83%. Enter 320L / h p-dichlorobenzene to the extraction kettle, and the acidic p-dichlorobenzene flows into the extraction kettle for 1 # Nitrification kettle, to 1 # 175L / h of 97% sulfuric acid and 120L / h of 98% nitric acid are fed into the nitrification kettle, and the nitrification liquid is successively lifted to the next level of nitrification kettle through the lifters o...
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