A kind of continuous preparation method of 1-aminoanthraquinone
A technology of aminoanthraquinone and nitroanthraquinone, applied in chemical instruments and methods, preparation of organic compounds, chemical recovery, etc., can solve problems such as environmental pollution and restricted applications, achieve precise control of reaction conditions, high conversion rate, The effect of efficient production
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Embodiment 1
[0014] Palladium carbon with a mass percentage of Pd of 5% is first filled inside the fixed bed.
[0015] Mix and stir 100 g of 1-nitroanthraquinone with a purity of 99% and 2 L of toluene to form a 1-nitroanthraquinone-toluene mixture, and output it at a flow rate of 0.2 mL / min and a flow rate of 2.66 mL / min. Hydrogen is mixed, then the temperature is raised to 50°C, and the mixed raw materials enter the fixed bed (and the volume ratio of the total volume to the Pd / C catalyst after mixing 1-nitroanthraquinone and toluene is 100:5) for hydrogenation reaction, hydrogenation The response time is 100s.
[0016] The reaction liquid flowing out after the hydrogenation reaction is mixed with ammonia water (introduction rate is 0.05ml / min), and the excess H in the hydrogenation reaction is released at the same time. 2 , and then mixed with oxygen (flow rate 1.8mL / min), the residence time in the oxidation reaction module after mixing was 100s, and the oxidation reaction temperature w...
Embodiment 2
[0020] Palladium carbon with a mass percentage of Pd of 5% is first filled inside the fixed bed.
[0021] Mix and stir 100 g of 1-nitroanthraquinone with a purity of 99% and 2 L of toluene to form a 1-nitroanthraquinone-toluene mixture, and output it at a flow rate of 0.2 mL / min, and a flow rate of 2.66 mL / min The hydrogen gas is mixed, and then the temperature is raised to 80°C. The mixed raw materials enter the fixed bed (and the volume ratio of the total volume of 1-nitroanthraquinone and toluene to the Pd / C catalyst is 100:5) for hydrogenation reaction. The hydrogenation reaction time is 80s.
[0022] The reaction liquid flowing out after the hydrogenation reaction is mixed with ammonia water (0.05ml / min), and the excess H in the hydrogenation reaction is released at the same time. 2 , and then mixed with oxygen (flow rate 1.8 mL / min). After mixing, the residence time in the oxidation reaction module was 80s, and the oxidation reaction temperature was controlled at 80°C. ...
Embodiment 3
[0026] Palladium carbon with a mass percentage of Pd of 5% is first filled inside the fixed bed.
[0027] Mix and stir 100 g of 1-nitroanthraquinone with a purity of 99% and 2 L of toluene to form a 1-nitroanthraquinone-toluene mixture, and output it at a flow rate of 0.2 mL / min and a flow rate of 2.66 mL / min. Hydrogen is mixed, and then the temperature is raised to 100°C. The mixed raw materials enter the fixed bed (and the volume ratio of the total volume to the Pd / C catalyst after mixing 1-nitroanthraquinone and toluene is 100:5) for hydrogenation reaction, hydrogenation The response time is 50s.
[0028] The reaction liquid flowing out after the hydrogenation reaction is mixed with ammonia water (0.05ml / min), and the excess H in the hydrogenation reaction is released at the same time. 2 , and then mixed with oxygen (flow rate 1.8mL / min), the residence time in the oxidation reaction module after mixing is 50s, and the oxidation reaction temperature is controlled at 100°C. ...
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