Preparation method of 2,4-dimethoxyaniline
A technology of dimethoxyaniline and dimethoxynitrobenzene, which is applied in the field of preparation of 2,4-dimethoxyaniline, can solve problems such as excessive three wastes, serious equipment corrosion, and environmental pollution
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Embodiment 1
[0095] A kind of preparation method of 2,4-dimethoxyaniline, take 2,4-dimethoxynitrobenzene as raw material, adopt Pd / Al 2 o 3 The catalyst is used for continuous catalytic hydrogenation reaction in the reactor. After the catalyst is separated and recovered, the reducing solution is desolvated and purified to obtain the target product 2,4-dimethoxyaniline.
[0096] Specific steps include:
[0097] (1) Put 5000kg of methanol and 1250kg of 2,4-dimethoxynitrobenzene into the chemical material tank, follow-up feeding is carried out according to the ratio, stir evenly, pump them into the first-stage hydrogenation reactor, add Pd / Al 2 o 3 Catalyst 125kg, the particle size of the catalyst is 10nm, pass through the nitrogen replacement system three times, then pass through the hydrogen replacement system three times, start stirring, raise the temperature to 90-100°C, and pump it into the first-stage hydrogenation tank at a flow rate of 6000L / h The raw material solution of 2,4-dim...
Embodiment 2
[0101] (1) Put 5000kg of methanol and 1250kg of 2,4-dimethoxynitrobenzene into the chemical feed tank, and follow up the ratio of feeding, stir evenly, pump them into the first-stage hydrogenation reactor, and add Pd / Al 2 o 3 125kg of catalyst, the particle size of the catalyst is 500μm; pass through the nitrogen replacement system three times, then pass through the hydrogen replacement system three times, start stirring, raise the temperature to 80-90°C, and pump it into the first-stage hydrogenation tank at a flow rate of 5000L / h The raw material solution of 2,4-dimethoxynitrobenzene is passed into H 2 , control the hydrogen pressure in the system to 3.0MPa, and add Pd / Al to the primary hydrogenation reactor every 3h 2 o 3 Catalyst 2.5kg, after the material in the primary hydrogenation kettle gradually increases, it flows into the secondary hydrogenation kettle through the overflow port, the material stays in the hydrogenation kettle for about 2-3h, and the reaction is qua...
Embodiment 3
[0105] (1) 12500kg of methanol and 1250kg of 2,4-dimethoxynitrobenzene are put into the chemical feed tank, and the subsequent feeding is stirred evenly according to the ratio. Al 2 o 3 Catalyst 125kg, the particle size of the catalyst is 10nm; pass through the nitrogen replacement system three times, then pass through the hydrogen replacement system three times, start stirring, raise the temperature to 90-100°C, and pump it into the first-stage hydrogenation tank at a flow rate of 6000L / h The raw material solution of 2,4-dimethoxynitrobenzene is passed into H 2 , control the hydrogen pressure in the system to 3.0MPa, and add Pd / Al to the primary hydrogenation reactor every 3h 2 o 3 Catalyst 2.5kg, after the material in the primary hydrogenation kettle gradually increases, it flows into the secondary hydrogenation kettle through the overflow port, the material stays in the hydrogenation kettle for about 2-3h, and the reaction is qualified (with 2,4-di Methoxynitrobenzene r...
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