Treatment method of residues from nitrotoluene rectification kettle
A technology for mononitrotoluene and rectification still residues, which is applied to the field of treatment of mononitrotoluene (MNT) rectification still residues, can solve the problems of complicated process, waste water generation, long treatment process flow, etc. simple craftsmanship
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Embodiment 1
[0016] Embodiment 1: according to the following steps, handle the residue of a nitrotoluene rectification still
[0017] (1) Put the rectification still residue, solvent ethanol, and nickel catalyst into the hydrogenation reactor at a mass ratio of 1:0.5:0.02, and carry out hydrogenation reduction with hydrogen under the conditions of controlling the reaction temperature at 80°C and the pressure at 0.5MPa Reaction, the mononitrotoluene in the still residue reacts with hydrogen to produce methylaniline, and dinitrotoluene reacts with hydrogen to generate diaminotoluene;
[0018] (2) After the hydrogenation reaction is completed, the hydrogenation liquid enters the filter, separates the catalyst in it, and then enters the desolventization tower to remove the solvent, and the separated catalyst and solvent are returned to the hydrogenation reduction process for recycling;
[0019] (3) The hydrogenated liquid after precipitating enters the oil-water separator, separates the water ...
Embodiment 2
[0022] Embodiment 2: according to the following steps, process the residue of nitrotoluene rectification
[0023] (1) Put the rectification still residue, solvent methanol, and nickel catalyst into the hydrogenation reactor at a mass ratio of 1:1:0.03, and carry out hydrogenation reduction with hydrogen under the conditions of controlling the reaction temperature at 100°C and the pressure at 1.0MPa Reaction, the mononitrotoluene in the still residue reacts with hydrogen to produce methylaniline, and dinitrotoluene reacts with hydrogen to generate diaminotoluene;
[0024] (2) After the hydrogenation reaction is completed, the hydrogenation liquid enters the filter, separates the catalyst in it, and then enters the desolventization tower to remove the solvent, and the separated catalyst and solvent are returned to the hydrogenation reduction process for recycling;
[0025] (3) The hydrogenated liquid after precipitating enters the oil-water separator, separates the water in it, ...
Embodiment 3
[0028] Embodiment 3: according to the following steps to process mononitrotoluene rectification still residue
[0029] (1) Put the rectification still residue, solvent methanol, and nickel catalyst into the hydrogenation reactor at a mass ratio of 1:1.5:0.04, and carry out hydrogenation reduction with hydrogen under the conditions of controlling the reaction temperature at 120°C and the pressure at 1.5MPa Reaction, the mononitrotoluene in the still residue reacts with hydrogen to produce methylaniline, and dinitrotoluene reacts with hydrogen to generate diaminotoluene;
[0030] (2) After the hydrogenation reaction is completed, the hydrogenation liquid enters the filter, separates the catalyst in it, and then enters the desolventization tower to remove the solvent, and the separated catalyst and solvent are returned to the hydrogenation reduction process for recycling;
[0031] (3) The hydrogenated liquid after precipitating enters the oil-water separator, separates the water ...
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