Preparation method of o-fluoroaniline
A technology of o-fluoroaniline and o-fluoronitrobenzene, which is applied in the field of preparation of o-fluoroaniline, can solve problems affecting product yield, achieve the effects of increasing yield and purity, improving reaction efficiency, and reducing defluorination rate
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Embodiment 1
[0025] Fill the continuous reactor with water, replace it with nitrogen for 3 times, then raise the temperature to 80°C, add 150kg of o-fluoronitrobenzene into the reactor every hour, and mix 1.0kg of catalyst, 0.01kg of hypophosphorous acid and 550kg of water at the same time Add it into the continuous reactor after uniformity, and feed 12kg of hydrogen into the continuous reactor at the same time to ensure the pressure of 2.0MPa, and keep feeding continuously. After 24 hours, the reaction ends, and the product passes through the layered tank. Layers can be reused and the lower layer is the product. After testing, the yield of the product was 99.0%, and the percentage content of the dehalogenated product was 0.02%.
Embodiment 2
[0027] Fill the continuous reactor with water, replace it with nitrogen for 3 times, then raise the temperature to 80°C, add 150kg of o-fluoronitrobenzene into the reactor every hour, and mix 2.0kg of catalyst, 0.03kg of hypophosphorous acid and 550kg of water at the same time Add it into the continuous reactor after uniformity, and feed 12kg of hydrogen into the continuous reactor at the same time to ensure the pressure of 2.0MPa, and keep feeding continuously. After 24 hours, the reaction ends, and the product passes through the layered tank. Layers can be reused and the lower layer is the product. After testing, the yield of the product was 99.06%, and the percentage content of the dehalogenated product was 0.02%.
Embodiment 3
[0029] Fill the continuous reactor with water, replace it with nitrogen for 3 times, then raise the temperature to 80°C, add 150kg of o-fluoronitrobenzene into the reactor every hour, and mix 1.2kg of catalyst, 0.02kg of hypophosphorous acid and 550kg of water at the same time Add it into the continuous reactor after uniformity, and feed 12kg of hydrogen into the continuous reactor at the same time to ensure the pressure of 2.0MPa, and keep feeding continuously. After 24 hours, the reaction ends, and the product passes through the layered tank. Layers can be reused and the lower layer is the product. After testing, the yield of the product was 99.06%, and the percentage content of the dehalogenated product was 0.02%.
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