Preparation method of N-methyl-4-methoxyaniline
A technology of methoxyaniline and methyl, which is applied in the field of preparation of N-methyl-4-methoxyaniline, can solve the problems of high raw material price, high energy consumption, and high reaction temperature, and achieve stable catalyst performance and reduce Difficult to separate, easy to operate
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[0014] The invention provides a kind of preparation method of N-methyl-4-methoxyaniline, comprises the following steps:
[0015] Mix p-nitroanisole, paraformaldehyde and a catalyst, and undergo a reduction reaction in a hydrogen atmosphere to obtain N-methyl-4-methoxyaniline.
[0016] In the present invention, unless otherwise specified, all raw material components are commercially available products well known to those skilled in the art.
[0017] In the present invention, described catalyzer is preferably one or more in Raney nickel, palladium carbon and platinum carbon; There is no special limitation on the proportioning ratio, and it may be mixed according to any proportioning ratio.
[0018] In the present invention, the molar ratio of the p-nitroanisole to the aldehyde group in paraformaldehyde is preferably 1: (1-10), more preferably 1: (2-8), most preferably 1: (4~6).
[0019] In the present invention, the mass ratio of the catalyst to nitroanisole is preferably (1-...
Embodiment 1
[0030] Mix 1mol p-nitroanisole, 1.5mol paraformaldehyde and 7.65g Raney nickel catalyst, replace the oxygen in the reaction environment with nitrogen until the oxygen content in the reaction environment≤0.50V%. With a heating rate of 3°C / min, the temperature of the reaction system was raised to 98±1°C and maintained, and hydrogen gas was introduced to control the reaction pressure to 1.50MPa. Process sampling detection analysis, when the conversion rate of p-nitroanisole is 0.50%, stop passing hydrogen; the reaction time at this time is 4h, and then through cooling, catalyst separation, and rectification, N-methyl-4-methoxy Aniline, the product yield is 86.20%.
Embodiment 2
[0032] Mix 1mol p-nitroanisole, 3mol paraformaldehyde and 7.65g Raney nickel catalyst, replace the oxygen in the reaction environment with nitrogen, to the oxygen content≤0.50V% in the reaction environment, under stirring condition, with 3 The heating rate of °C / min is used to raise the temperature of the reaction system to 98±1 °C and maintain it. Hydrogen gas is introduced to control the reaction pressure to 1.50 MPa. Process sampling detection and analysis, when the conversion rate of p-nitroanisole is 0.50%, stop passing hydrogen; the reaction time at this time is 3.8h, and then through cooling, catalyst separation, and rectification, N-methyl-4-methanol is obtained Oxygenated aniline, the product yield is 87.6%.
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