A kind of continuous synthesis 2, the method for 4-dinitroanisole
A technology of dinitroanisole and dinitrochlorobenzene, applied in the field of continuous chemical synthesis, can solve the problems of long cycle, large amount of waste water, high cost, etc., and achieve low pollution, low cost, safe and reliable process Effect
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Embodiment 1
[0022] (1) 2,4-dinitrochlorobenzene (CDB) in a molten state at 65°C, methanol at 20°C and 30% liquid caustic soda solution with a mass fraction of 20°C are continuously added to the In the reactor, keep the temperature in the reactor constant at 65°C;
[0023] (2) The synthetic reaction solution enters the evaporator continuously, and the methanol enters the rectification tower from the vapor phase outlet of the evaporator, and from the top of the rectification tower to the recovery bottle, it contains 2,4-dinitroanisole (DNAN), chlorinated The sodium aqueous solution enters the washing tank continuously from the liquid phase outlet of the evaporator;
[0024] (3) After being washed with hot water at 95°C in the washing tank, it enters the separator for static separation, and the separated wastewater is collected for unified treatment. The product 2,4-dinitroanisole (DNAN) is collected and then dried, weighed, analysis test;
[0025] Through analysis and testing, it was foun...
Embodiment 2
[0027] (1) Continuously transport methanol, liquid caustic soda, and molten 2,4-dinitrochlorobenzene (CDB) to corresponding raw material head tanks respectively;
[0028] (2) The lye, methanol and 2,4-dinitrochlorobenzene (CDB) are continuously added to the reactor from the head tank at a mass ratio of 1:0.72:5, and the temperature of the reactor is set at 65°C under normal pressure. , the reaction liquid enters the curing machine continuously through the lifting system of the reactor, and the setting temperature of the curing machine is 65°C and normal pressure;
[0029] (3) The mixed material in the aging machine enters the evaporator continuously through the lifting system, and the evaporator adopts a tank-type self-circulation mode, and the reaction liquid after removing methanol continuously enters the first washing tank from the side of the evaporator, and the evaporator evaporates Methanol and water vapor continuously enter the methanol rectification tower. The tower is...
Embodiment 3
[0035] (1) Continuously transport methanol, liquid caustic soda, and molten 2,4-dinitrochlorobenzene (CDB) to corresponding raw material head tanks respectively;
[0036] (2) Lye, methanol and 2,4-dinitrochlorobenzene (CDB) are continuously added to the reaction kettle from the head tank at a mass ratio of 1:0.72:8, and the reaction kettle is set at a temperature of 62°C and normal pressure , the reaction liquid enters the curing machine continuously through the lifting system of the reactor, and the setting temperature of the curing machine is 62°C and normal pressure;
[0037] (3) The mixed material in the aging machine enters the evaporator continuously through the lifting system, and the evaporator adopts a tank-type self-circulation mode, and the reaction liquid after removing methanol continuously enters the first washing tank from the side of the evaporator, and the evaporator evaporates Methanol and water vapor continuously enter the methanol rectification tower. The t...
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