Abstract

Al 2O 3-supported Mo, Ni, NiMo, and Rh catalysts, prepared by sequential aqueous impregnation and in situ sulfidation, were investigated in the hydrodenitrogenation (HDN) of quinoline at 643 K and 3 MPa and in the hydrodesulfurisation (HDS) of thiophene at 673 K and 0.1 MPa. The Ni and Mo catalysts had a very low conversion of quinoline to hydrocarbons which improved only slightly in the presence of phosphate. The Rh catalysts had a high conversion and a high selectivity for propylcyclohexane and showed no deactivation with time. The addition of Ni to MO/Al 2O 3 and of phosphate to NiMo/Al 2O 3 and Rh/Al 2O 3 catalysts increased the HDN conversion significantly. The selectivity for propylbenzene and the apparent HDN activation energy increased with increasing P-loading. Ni increased the thiophene conversion of Mo/Al 2O 3, but phosphate had almost no influence on the HDS activity of NiMo/Al 2O 3 and Rh/Al 2O 3. The effect of phosphate is due to a combination of structural and catalytic factors. Phosphate improves the activity by inducing the formation of the type II NiMoS structure, but also, especially at high Ni loading, lowers the activity by inducing a decrease in the dispersion of the NiMoS phases and a segregation of Ni 3S 2. Phosphate also promotes the S- and N-elimination reactions, but this only has an influence on the overall catalyst activity if the preceding hydrogenation reactions are not rate determining.

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