Continuous preparation method of DAB (3,3'-diaminobenzidine)
A technology for tetraaminobiphenyl and dichlorobenzidine is applied in the field of preparing 3,3',4,4'-tetraaminobiphenyl, and can solve the problems of unsuitable continuous production, large pollution, low production efficiency and the like, To achieve the effect of simplified operation, high production efficiency and short reaction time
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Embodiment 1
[0028] The molten 3,3'-dichlorobenzidine is injected into the primary reactor through a high-pressure pump at a flow rate of 150 grams / hour, and the mixture of ammoniacal liquor and copper chloride with a mass fraction of 25% is injected at a flow rate of 900 grams / hour ( Among them, the flow rate of copper chloride is 6 g / hour) into the first-stage reaction kettle through the pump, and the ammoniation reaction is carried out at 0.4MPa and 140°C. The residence time of the first-stage reaction kettle is 5 minutes, and the residence time of the second-level reaction kettle is 10 Minutes, the residence time of the three-stage reactor is 5 minutes, and the reaction to be detected is complete, and the material is decompressed and discharged from the pressure-relief valve of the three-stage reactor, and the discharge is sent to a recovery device, and excess ammonia is distilled, and then separated to obtain 124.4 g / h, purity (HPLC) 98.17% of 3,3',4,4'-tetraaminobiphenyl, total yiel...
Embodiment 2
[0030] The molten 3,3'-dichlorobenzidine is injected into the primary reactor through a high-pressure pump at a flow rate of 150 g / h, and the mass fraction is 20% ammoniacal liquor and cupric chloride at a flow rate of 900 g / h (wherein The flow rate of copper chloride is 5 g / hour) into the first-stage reaction kettle through the pump, and the ammoniation reaction is carried out at 90°C. Stay for 10 minutes, until the detection reaction is complete, after depressurizing and discharging the material from the pressure reducing valve of the three-stage reactor, the material is sent to the recovery device, the excess ammonia is distilled, and then separated to obtain 122.7 g / h, purity (HPLC) 98.5% 3,3′,4,4′-tetraaminobiphenyl, the total yield is 95.3%.
Embodiment 3
[0032] The molten 3,3'-dichlorobenzidine is injected into the primary reactor through a high-pressure pump at a flow rate of 150 grams / hour, and the mass fraction is a mixture of 30% ammoniacal liquor and cupric chloride at a flow rate of 900 grams / hour (wherein The flow rate of copper chloride is 3 g / hour) pumped into the first-stage reactor for ammoniation reaction at 0.3MPa and 120°C. The first-stage reactor stays for 8 minutes, the second-stage reactor stays for 12 minutes, and the third The first-stage reactor stays for 8 minutes. After the detection reaction is complete, the material is decompressed and discharged from the pressure-relief valve of the third-stage reactor. 98.9% of 3,3′,4,4′-tetraaminobiphenyl, the total yield is 96.1%.
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