Preparation method of N-phenyl-tetrahydro-2-naphthylamine
A technology of naphthylamine and phenyl, which is applied in the field of preparation of N-phenyltetrahydro-2-naphthylamine, can solve the problems of unsuitable purchase of raw materials, long reaction time, complicated operation, etc., and achieves less generation of three wastes and easy reaction. Control, the effect of high reaction yield
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[0015] In the industrial field, the preparation method of N-phenyltetrahydro-2-naphthylamine can be according to the method that the inventor develops, preferably utilizes N-phenyl-2-naphthylamine in polar protic solvent-methanol or ethanol, The crude product of N-phenyltetrahydro-2-naphthylamine was obtained by heating and reducing hydrogenation under catalysis. To describe the method in detail, methanol or ethanol is preferably used as the reaction solvent, and the catalyst is preferably metal nickel or palladium carbon. In addition, the reaction temperature ranges from 95°C to 105°C, preferably from 95°C to 100°C.
[0016] In addition, the present invention can also be used for the hydrogenation reduction reaction of similar compounds containing methyl, methoxy, amino and other groups.
Embodiment 1
[0020] Add 1kg of N-phenyl-2-naphthylamine, 0.12kg of RaneyNi, 1.6kg of methanol into a 5L autoclave, seal the autoclave, evacuate it twice with hydrogen, let it stand for 30min, then inject 6MPa, heat up to 100℃ for reaction Until the hydrogen pressure no longer changes. The supernatant was taken from the reaction solution, and the nickel in the lower layer continued to be applied mechanically and filtered. Evaporate 50% of the filtrate, stir and cool at room temperature, crystallize, cool to below 10°C, filter, rinse the filter cake with a small amount of methanol and drain to obtain 0.58 kg of crude product, liquid phase content 97.5%, yield: 57%.
Embodiment 2
[0022] Add 1 kg of N-phenyl-2-naphthylamine and 0.12 kg of RaneyNi (recycled) and 1.6 kg of methanol to a 5L autoclave, seal the autoclave, and evacuate it twice with hydrogen. React at 100°C until the hydrogen pressure no longer changes. Cool down, release pressure. The supernatant was taken from the reaction solution, and the nickel in the lower layer continued to be applied mechanically and filtered. The filtrate was evaporated to 50%, stirred and cooled at room temperature, and crystallized. Cool down to below 10°C, filter, rinse the filter cake with a small amount of methanol and drain to obtain 0.56 kg of crude product, liquid phase content 97.1%, yield: 55%.
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