Process for the preparation of aromatic amines
Aromatic amines are produced by catalytic hydrogenation of aromatic nitro compounds. The reaction mixture generated by this hydrogenation is then worked up by distillation in a manner which makes it possible to substantially free the amine of water with increased energy efficiency. Water free of amine and low boilers and the low boiling materials are also obtained.
1. A process for the preparation of an aromatic amine by catalytic hydrogenation of the corresponding aromatic nitro compound and the purification thereof by distillation comprising:
a) hydrogenating the aromatic nitro compound in liquid phase at a temperature of from 100 to 200° C. in a reaction vessel in the presence of a catalyst to form a reaction mixture containing amine and water and to generate heat,
b) separating water from the reaction mixture containing amine and water by a single distillation in a distillation column to obtain a purified amine containing water in an amount of less than 20 wt. %, based on the weight of the mixture,
c) using at least a portion of the heat from the hydrogenation of step a), either directly or indirectly, to heat the distillation in step b), and
d) operating the distillation column with an absolute head pressure of less than 1 bar.
2. The process of claim 1 in which the heat generated in step a) is used to convert water to steam and this steam is then used to heat the distillation in step b).
3. The process of claim 2 in which the steam produced has an absolute pressure of from 1 to 12 bar.
4. The process of claim 2 in which the heat generated in step a) supplies sufficient energy to satisfy at least 50% of the energy requirement of the distillation in step b).
5. The process of claim 1 in which the aromatic nitro compound is nitrobenzene, nitrotoluene or dinitrotoluene.
6. The process of claim 1 in which the water is removed as a sidestream in the single distillation step.
7. The process of claim 1 in which the heat generated in step a) supplies sufficient energy to satisfy at least 50% of the energy requirement for the distillation in step b).