Process for preparing ortho-aminophenol by virtue of continuous catalytic hydrogenation
An o-aminophenol, catalytic hydrogenation technology, applied in the preparation of organic compounds, preparation of aminohydroxy compounds, catalysts for physical/chemical processes, etc., can solve the problems of harsh reaction conditions, poor product quality, large labor, etc. The effect of less investment, higher production costs, and less labor
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Embodiment 1
[0027] A process for preparing o-aminophenol by continuous catalytic hydrogenation, using o-nitrophenol as raw material, using Pd / Al 2 o 3 The catalyst is used for continuous catalytic hydrogenation in a fixed-bed reactor, and the target product o-aminophenol is obtained after separation and purification. Its reaction equation is:
[0028]
[0029] Specific steps include:
[0030] (1) Dissolve 1.0Kg of o-nitrophenol in 3L of ethanol-water solution with a volume fraction of 50%, preheat to 70°C, and feed continuously with a metering pump. 3 / h flow rate into the Pd / Al 2 o 3 In the fixed bed reactor of the catalyst, hydrogen gas is introduced at the same time to carry out continuous catalytic hydrogenation reduction reaction. The reaction temperature is 120°C and the reaction pressure is 1.0MPa. The reaction feed liquid enters the cooling tank and is cooled to 35°C by circulating water;
[0031] The Pd / Al 2 o 3 The mass fraction that Pd accounts for catalyst is 15% in ...
Embodiment 2
[0035] A process for preparing o-aminophenol by continuous catalytic hydrogenation, using o-nitrophenol as raw material, using Pd / Al 2 o 3 The catalyst is used for continuous catalytic hydrogenation in a fixed-bed reactor, and the target product o-aminophenol is obtained after separation and purification. Its reaction equation is:
[0036]
[0037] Specific steps include:
[0038] (1) Dissolve 1.0Kg of o-nitrophenol in 4.5L of ethanol-water solution with a volume fraction of 70%, preheat to 75°C, and feed continuously with a metering pump to 0.23m 3 / h flow rate into the Pd / Al 2 o 3 In the fixed bed reactor of the catalyst, hydrogen gas is fed at the same time to carry out continuous catalytic hydrogenation reduction reaction. The reaction temperature is 95°C and the reaction pressure is 1.5MPa. The reaction feed liquid enters the cooling tank and is cooled to 45°C by circulating water;
[0039] The Pd / Al 2 o 3 In the catalyst, the mass fraction of Pd in the cataly...
Embodiment 3
[0043] A process for preparing o-aminophenol by continuous catalytic hydrogenation, using o-nitrophenol as raw material, using Pd / Al 2 o 3 The catalyst is used for continuous catalytic hydrogenation in a fixed-bed reactor, and the target product o-aminophenol is obtained after separation and purification. Its reaction equation is:
[0044]
[0045] Specific steps include:
[0046] (1) Dissolve 1Kg of o-nitrophenol in 4.5L of ethanol-water solution with a volume fraction of 85%, preheat to 80°C, and feed continuously with a metering pump. 3 / h flow rate into the Pd / Al 2 o 3 In the fixed bed reactor of the catalyst, hydrogen gas is introduced at the same time to carry out continuous catalytic hydrogenation reduction reaction. The reaction temperature is 70°C and the reaction pressure is 2.0MPa. The reaction feed liquid enters the cooling tank and is cooled to 38°C by circulating water;
[0047] The Pd / Al 2 o 3 The mass fraction that Pd accounts for catalyst is 20% in t...
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