NiPt catalysts supported on SAPO-11 zeolite were synthesized with the aim to inquire into the influence of the support's Si/Al molar ratio (0.075–0.60) on the activity and selectivity of the catalysts in the hydrodeoxygenation of anisole. An increase in Si content led to a reduction in the crystallinity of SAPO-11, attributed to the higher number of SiO2 islands (extra-framework silica species). Acidity of supports and catalysts passed through the maximum at a Si/Al molar ratio of 0.15 and then decreased with further increase in Si/Al ratio. All the NiPt/SAPO-11 catalysts demonstrated high activity in the hydrodeoxygenation of anisole in a batch reactor at 250 °C and 6.8 MPa of H2 pressure, achieving conversions of 96–98 % at 6 h reaction time. The best activity results were obtained with the NiPt/SAPO-11 catalysts with Si/Al molar ratios in the supports between 0.30 and 0.60. Supports with lower Si/Al molar ratios (0.075 and 0.15) resulted in lower activity, which was attributed to an increase in the fraction of NiAl2O4 with Ni2+ species non-reducible upon the activation conditions used (400 °C, 4 h). Regarding selectivity to cyclohexane, catalysts with intermediate Si/Al ratios (0.15–0.45) exhibited higher selectivity (∼94–96 %) than other catalysts, attributed to their elevated acidity as measured by temperature-programmed desorption of ammonia. Finally, the experimental data were fitted to a kinetic model that considered the hydrogenation-deoxygenation pathway, correlating the kinetic constants with the metal-acid characteristics of the catalysts, namely, the amount of reduced Ni and total amount of acid sites.
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