“…Monometallic catalysts MoO x /TiO 2 (2 wt % Mo) and Pd/TiO 2 (0.3 wt % Pd) were prepared by incipient wetness impregnation of aqueous solutions of (NH 4 ) 6 Mo 7 O 24 ·4H 2 O and Pd(NO 3 ) 2 ·2H 2 O on TiO 2 (P25) as reported previously by Nacy et al Monometallic catalysts were then dried overnight at 393 K and calcined in air at 773 K for 3 h. The MoO x -M/TiO 2 (2 wt % Mo, M/Mo molar ratio = 0.14) catalysts with varying hydrogen dissociating metal (M = Pd, Pt, Rh) were prepared by incipient wetness impregnation of aqueous solutions of Pd(NO 3 ) 2 ·2H 2 O, H 2 PtCl 6 ·6H 2 O, and RhCl 3 · x H 2 O on TiO 2 (P25); followed by drying at 393 K for 12 h. The samples were then impregnated with an aqueous solution of (NH 4 ) 6 Mo 7 O 24 ·4H 2 O, dried at 393 K for 12 h, and calcined in air at 773 K for 3 h. For supported catalyst M′O x -Pd/TiO 2 (2 wt % M′, Pd/M′ molar ratio = 0.14) with varying oxophilic metals (M′ = Mo, Re, W), an aqueous solution of Pd(NO 3 ) 2 ·2H 2 O was deposited by incipient wetness on TiO 2 (P25), then dried at 393 K for 12 h. The dried powders were then impregnated with (NH 4 ) 6 Mo 7 O 24 ·4H 2 O, NH 4 ReO 4 , and (NH 4 ) 10 W 12 O 41 · x H 2 O; dried at 393 K for 12 h; and calcined in air at 773 K for 3 h. Catalysts with varying supports were prepared by incipient wetness impregnation of aqueous solutions of Pd(NO 3 ) 2 ·2H 2 O on TiO 2 (P25), ZrO 2 , γ-Al 2 O 3 , and SiO 2 . After drying the samples at 393 K for 12 h, an aqueous solution of (NH 4 ) 6 Mo 7 O 24 ·4H 2 O was deposited by incipient wetness impregnation prior to calcination in air at 773 K for 3 h. Metal loadings on the catalyst with varying supports was 0.3 wt % Pd and 2 wt % Mo.…”