Method of producing 1-aminonaphthalene through fixed bed hydrogenation process
A technology of aminonaphthalene and hydrogenation method, which is applied to the preparation of amino compounds, chemical instruments and methods, and the preparation of organic compounds. High hydrogenation activity and resistance to sulfur toxicity, high reaction conversion rate and yield, simple and convenient recovery method
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[0021] The preparation process of the supported nickel catalyst is as follows: the preparation process of the supported nickel catalyst is: the soluble nickel salt and the nitrate react under the action of the precipitant to obtain precipitation, filter the distilled water and wash, and then dry to obtain the crude product of the supported catalyst. The solid is calcined at 200-600° C. for 2-5 hours under a nitrogen atmosphere, and at 300-550° C. for 2-4 hours under a hydrogen atmosphere to obtain a supported nickel catalyst.
[0022] Wherein, the nitrate includes one or both of magnesium nitrate and aluminum nitrate; the precipitation agent includes sodium silicate or sodium carbonate.
[0023] The obtained supported nickel catalyst has a clover shape. The main features are as follows: 1. High mechanical strength (>20N / cm); 2. High physical surface area (100-300m 2 / g); 3. The pore size can be adjusted (6~12nm) to adapt to different molecular sizes; 4. The surface area of ...
Embodiment 1
[0025] Dissolve 1-nitronaphthalene in ethanol for later use, and the weight ratio of 1-nitronaphthalene to ethanol is 1:2. Fill the Ni / MgAlO catalyst in the reactor, raise the temperature to 170°C under a flowing hydrogen atmosphere, pass through the phosphating solution to start phosphine (the phosphating solution is a triphenylphosphine solution with a mass concentration of 7.5%), and after the phosphination is completed, hydrogen air Speed is 500h -1 , the temperature was raised to 300°C and the aging was started for 4h.
[0026] The fixed-bed feed pump pumps the 1-nitronaphthalene solution into the fixed-bed reactor, and feeds hydrogen to control the fixed-bed temperature at 200°C, hydrogen pressure at 3.0MPa, and space velocity at 0.25h -1 , carry out the hydrogenation reaction, and at the same time use the reflux pump to pump out the reaction solution flowing out from the fixed bed, the flow rate of the feed pump is 40ml / h, collect the reaction solution, and obtain 1-...
Embodiment 2
[0028] This embodiment is basically the same as Embodiment 1, the only difference being that the temperature of the fixed bed is controlled to 130°C. After 4000 hours of continuous production, the product conversion rate is 99.6%, and the yield is 99.2%; after more than 5000 hours, the conversion rate is 98%, and the yield is 97.8%.
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