Abstract
The kinetics of pyridine hydrogenation was studied at high hydrogen pressures on a Mo-Al oxide and a Co-Mo-Al oxide catalyst. The rate equation was found to be r = kPpyrPH2n/Ppyro, in which n is 1.5 at 300 and 375 °C and 1.0 at 250 °C. This rate equation can be derived assuming strong adsorption of pyridine and its products with identical adsorption constants.
The (hydro)cracking of piperidine appears to have a low order in hydrogen, probably lower than 0.5.
The adsorption behavior of nitrogen bases and hydrogen on alumina and the molybdenum-containing catalysts was investigated by the gas chromatographic method. The adsorption of the nitrogen bases appeared to be very strong on both catalysts, and varied in the order piperidine > pyridine > ammonia.
Hydrogen also showed a strong adsorption. Hydrogen and nitrogen bases appeared to adsorb on different sites.
Original language | English |
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Pages (from-to) | 220-230 |
Journal | Journal of catalysis |
Volume | 31 |
Issue number | 2 |
DOIs | |
Publication status | Published - 1973 |