Affiliation: | aCatalysis and Chemical Reaction Engineering Laboratories, Department of Chemical Engineering, University of Saskatchewan, Saskatoon, SK S7N 5A9, Canada bSyncrude Edmonton Research Centre, Edmonton, AB T6N 1H4, Canada |
Abstract: | A series of phosphorus promoted γ-Al2O3 supported NiMo carbide catalysts with 0–4.5 wt.% P, 13 wt.% Mo and 2.5 wt.% Ni were synthesized and characterized by elemental analysis, pulsed CO chemisorption, BET surface area measurement, X-ray diffraction, near-edge X-ray absorption fine structure, DRIFT spectroscopy of CO adsorption and H2 temperature programmed reduction. X-ray diffraction patterns and CO uptake showed the P addition to NiMo/γ-Al2O3 carbide, increased the dispersion of β-Mo2C particles. DRIFT spectra of adsorbed CO revealed that P addition to NiMo/γ-Al2O3 carbide catalyst not only increases the dispersion of Ni-Mo carbide phase, but also changes the nature of surface active sites. The hydrodenitrogenation (HDN) and hydrodesulfurization (HDS) activities of these P promoted NiMo/γ-Al2O3 carbide catalysts were performed in trickle bed reactor using light gas oil (LGO) derived from Athabasca bitumen and model feed containing quinoline and dibenzothiophene at industrial conditions. The P added NiMo/γ-Al2O3 carbide catalysts showed enhanced HDN activity compared to the NiMo/γ-Al2O3 catalysts with both the feed stocks. The P had almost no influence on the HDS activity of NiMo/γ-Al2O3 carbide with LGO and dibenzothiophene. P addition to NiMo/γ-Al2O3 carbide accelerated C N bond breaking and thus increased the HDN activity. |