Method for continuously preparing p-aminodiphenylamine
A technology of p-aminodiphenylamine and nitrodiphenylamine, which is applied in the field of synthesis of p-aminodiphenylamine, can solve the problems of large catalyst loss, high labor intensity, and low catalytic activity, and achieve reduced dosage, improved product quality, and high activity Effect
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Embodiment 1
[0022] Add 50g of supported palladium-carbon catalyst with a content of 1% into the fixed bed reactor, continuously add 31.25% methanol and 68.75% aniline to the fixed bed reactor with a pump, raise the temperature to 60°C, and preheat the catalyst with a mass concentration of 15%. 4-Nitrosodiphenylamine and the above-mentioned methanol and aniline solution with a concentration of 5% 4-nitrodiphenylamine are brought to 60°C, and the above solution is added to the fixed-bed reactor with a pump, and the flow rate of the solution is adjusted to 0.2mL / min. The hydrogen pressure is 0.5 MPa, the hydrogen flow rate is 100mL / min, the reaction residence time is 200min, and the reaction materials are regularly sampled and analyzed. The conversion rate of the raw materials is 91.1%, and the selectivity is 93.2%. Distillation treatment to obtain p-aminodiphenylamine.
Embodiment 2
[0024] Add 40g of 2% supported palladium-carbon catalyst into the fixed-bed reactor, add 18.75% ethanol and 81.25% aniline to the fixed-bed reactor continuously with a pump, raise the temperature to 80°C, and preheat 4 -Nitrosodiphenylamine and the above-mentioned ethanol and aniline solution with a concentration of 10% of 4-nitrodiphenylamine to 60°C, add the above solution into the fixed-bed reactor with a pump, adjust the flow rate of the solution to 0.2mL / min, hydrogen The pressure was 1.5 MPa, the hydrogen flow rate was 50mL / min, the reaction residence time was 90min, and the reaction materials were regularly sampled and analyzed. The conversion rate of the raw materials was 94.1%, and the selectivity was 95.0%. Distillation treatment to obtain p-aminodiphenylamine.
Embodiment 3
[0026] Add 30g of supported palladium-carbon catalyst with a content of 3% to the fixed bed reactor, continuously add 50% methanol and 50% aniline to the fixed bed reactor with a pump, raise the temperature to 90°C, and preheat the catalyst with a mass concentration of 12%. 4-nitrosodiphenylamine and methanol and aniline solution with a concentration of 8% of 4-nitrodiphenylamine to 60 ° C, the above solution is added to the fixed bed reactor with a pump, and the flow rate of the solution is adjusted to 0.2mL / min, hydrogen The pressure was 2.0 MPa, the hydrogen flow rate was 40 mL / min, and the reaction residence time was 100 min. The reaction materials were regularly sampled and analyzed. The conversion rate of the raw materials was 95.1%, and the selectivity was 96.0%. Distillation treatment to obtain p-aminodiphenylamine.
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