Abstract
Ni-W catalysts were prepared by impregnation of commercial γ-alumina and silica supports. The sulfidation, performed directly after drying at 100°C, yielded fully sulfided Ni-W species on both supports (SEM-EDAX, XPS, XRD). At optimal metals loading (∼50 wt% NiO + WO3, Ni/W = 2), the sulfided catalysts had similar texture (N2 adsorption) and displayed similar activity in dibenzothiophene hydrodesulfurization (DBT HDS), while the activity of the Ni-W/SiO2 catalyst in toluene hydrogenation (HYD) was six times higher than that of Ni-W/Al2O3. This is due to the more than two times higher WS2 slabs stacking number in Ni-W/SiO2 compared with Ni-W/Al2O3 (XRD, HR-TEM), yielding stronger adsorption of toluene (TPD).
Original language | English |
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Pages (from-to) | 47-54 |
Number of pages | 8 |
Journal | Catalysis Letters |
Volume | 77 |
Issue number | 1-3 |
DOIs | |
State | Published - 1 Dec 2001 |
Keywords
- DBT hydrodesulfurization
- Morphology
- Ni-W-S catalyst
- TEM
- TPD
- Toluene hydrogenation
- γ-alumina and silica supports
ASJC Scopus subject areas
- Catalysis
- Chemistry (all)