Kinetic Modeling of 2,4-Dinitrotoluene Hydrogenation over Pd/C
The kinetics of liquid phase hydrogenation of 2,4-dinitrotoluene (2,4-DNT) to 2,4-diaminotoluene (2,4-DAT) were studied in ethanol with a 5% Pd/C catalyst using a slurry reactor, in the temperature range between 278 and 323 K and at a pressure of 0.1 MPa. the reaction pathway has been described by a...
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Veröffentlicht in: | Industrial & engineering chemistry research 1995-07, Vol.34 (7), p.2226-2231 |
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Format: | Artikel |
Sprache: | eng |
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Zusammenfassung: | The kinetics of liquid phase hydrogenation of 2,4-dinitrotoluene (2,4-DNT) to 2,4-diaminotoluene (2,4-DAT) were studied in ethanol with a 5% Pd/C catalyst using a slurry reactor, in the temperature range between 278 and 323 K and at a pressure of 0.1 MPa. the reaction pathway has been described by a Langmuir-Hinshelwood model with a noncompetitive adsorption of the organic species and hydrogen on the active sites. Different reaction mechanisms have been tested. The best fitting of the experimental data was obtained with a reaction mechanism involving three parallel routes leading from 2,4-DNT to 4-(hydroxyamino)-2-nitrotoluene (4HA2NT), 4-amino-2-nitrotoluene (4A2NT), and 2-amino-4-nitrotoluene (2A4NT) which are then hydrogenated to 2,4-DAT through a series of consecutive reactions. The rate constants and activation energy for each reaction step have been reported. |
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ISSN: | 0888-5885 1520-5045 |
DOI: | 10.1021/ie00046a003 |