1989 Volume 15 Issue 2 Pages 435-437
The dehydrogenation of methylcyclohexane was carried out in a differential fixed-bed reactor at 781 K and atmospheric pressure, and the deactivation rates of Pt-, PtRe-Al2O3 and the sulfided catalysts were compared. The presence of Re and presulfiding of the catalysts resulted in improved stability. Continuous addition of H2S at a concentration of 50 ppm in feed was effective for maintaining the activity with Pt during only the first few hours of operation, while it caused a marked decrease in the initial activity with PtRe. The experimental results were interpreted by the ensemble effect.