Characterization of γ-alumina-supported Molybdenum oxide and tungsten oxide; reducibility of the oxidic state versus hydrodesulfurization activity of the sulfided state

Thiophene hydrodesulfurization and butene hydrogenation have been determined for MoO 3 γ- Al 2 O 3 WO 3 γ- Al 2 O 3 , and Re 2 O 7 γ- Al 2 O 3 catalysts, using a microf-low reactor operating at atmospheric pressure. Catalysts have been prepared by various methods, viz., ion exchange, gas-phase adsor...

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Bibliographic Details
Published inJournal of catalysis Vol. 76; no. 2; pp. 241 - 253
Main Authors Thomas, R., van Oers, E.M., de Beer, V.H.J., Medema, J., Moulijn, J.A.
Format Journal Article
LanguageEnglish
Published Elsevier Inc 01.08.1982
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Summary:Thiophene hydrodesulfurization and butene hydrogenation have been determined for MoO 3 γ- Al 2 O 3 WO 3 γ- Al 2 O 3 , and Re 2 O 7 γ- Al 2 O 3 catalysts, using a microf-low reactor operating at atmospheric pressure. Catalysts have been prepared by various methods, viz., ion exchange, gas-phase adsorption, dry and wet impregnation of γ-Al 2O 3 as well as impregnation of boehmite. The catalysts have been prepared on a surface coverage basis. The catalysts were characterized by X-ray diffraction, surface area and pore volume measurements, and temperature-programmed reduction (TPR). MoO 3 γ- Al 2 O 3 and WO 3 γ- Al 2 O 3 catalysts prepared by dry and wet impregnation give essentially the same results. A correlation exists between the reducibility of oxidic MoO 3 γ- Al 2 O 3 and WO 3 γ- Al 2 O 3 catalysts prepared by dry and wet impregnation, and the hydrodesulfurization activity of the sulfided samples. The higher the reducibility, the higher the hydrodesulfurization activity. This correlation also holds for MoO 3 γ- Al 2 O 3 catalysts prepared by other methods, viz., ion exchange, gas-phase adsorption, and impregnation of boehmite, and for Re 2 O 7 γ- Al 2 O 3 catalysts prepared by dry impregnation. Butene hydrogenation activity of sulfided MoO 3 γ- Al 2 O 3 and WO 3 γ- Al 2 O 3 catalysts also correlates with reducibility. This correlation is qualitatively the same as that found for hydrodesulfurization. For Re 2 O 7 γ- Al 2 O 3 catalysts this is not the case. The ratio between hydrodesulfurization activity and hydrogenation activity decreases in the order W → Mo → Re. TPR is a time-saving screening technique for unpromoted well-dispersed hydrodesulfurization catalysts.
ISSN:0021-9517
1090-2694
DOI:10.1016/0021-9517(82)90255-X