A kind of chloroacetic acid chlorination mother liquor treatment method
A treatment method, the technology of chloroacetic acid, applied in the field of treatment of chloroacetic acid chlorination mother liquor, can solve the problems of high unit consumption of acetic anhydride, expensive raw materials, increase of by-products of hydrogenation reaction, etc., so as to save acetic anhydride consumption and reduce the possibility , reduce the effect of by-products
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Embodiment 1
[0024] The chlorination mother liquor is heated by the heater 1; the heated chlorination mother liquor and water enter the hydrolysis reactor 2 respectively, the temperature of the mother liquor increases, and part of the acetyl chloride evaporates; the unevaporated acetyl chloride and water are hydrolyzed with water in the hydrolysis reactor 2 reaction; after the hydrolysis reaction, the chlorinated mother liquor enters the auxiliary hydrolysis reactor 4 for flash evaporation, and HCL is separated and enters the absorption device; the mother liquor after flash evaporation is pumped into the hydrogenation reactor 7 through the pump 6, and reacts under the action of the catalyst, and the reaction The final HCL enters the absorption device, and the chlorinated mother liquor enters the distillation or crystallization process.
Embodiment 2
[0026] The chlorination mother liquor is heated by the heater 1; the heated chlorination mother liquor and water enter the hydrolysis reactor 2 respectively, the temperature of the mother liquor increases, and part of the acetyl chloride evaporates; the unevaporated acetyl chloride and water are hydrolyzed with water in the hydrolysis reactor 2 Reaction; a steam jacket 3 is installed outside the hydrolysis reactor 2 to further increase the temperature of the chlorination mother liquor and reduce the saturation content of acetyl chloride; after the hydrolysis reaction, the chlorination mother liquor enters the auxiliary hydrolysis reactor 4 for flash evaporation, and the separated HCL enters the absorption device; The flash evaporated mother liquor enters the hydrogenation reactor 7 through the pump 6, and reacts under the action of the catalyst. The reacted HCL enters the absorption device, and the chlorinated mother liquor enters the distillation or crystallization process.
Embodiment 3
[0028] The chlorination mother liquor is heated by the heater 1; the heated chlorination mother liquor and water enter the hydrolysis reactor 2 respectively, the temperature of the mother liquor increases, and part of the acetyl chloride evaporates; the unevaporated acetyl chloride and water are hydrolyzed with water in the hydrolysis reactor 2 reaction; the steam jacket 3 is installed outside the hydrolysis reactor 2 to further increase the temperature of the chlorination mother liquor and reduce the saturation content of acetyl chloride; after the hydrolysis reaction, the chlorination mother liquor enters the auxiliary hydrolysis reactor 4 for flash evaporation, and the auxiliary hydrolysis reactor 4 is installed and stirred The device promotes the hydrolysis reaction to be fully carried out, and the separated HCL enters the absorption device; the mother liquor after flashing is pumped into the hydrogenation reactor 7 through the pump 6, and reacts under the action of the cata...
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