Abstract
Unsupported, high surface area MoP and Ni2P catalysts were synthesized by adding citric acid (CA) to solutions of ammonium heptamolybdate and diammonium hydrogen phosphate or nickel nitrate and diammonium hydrogen phosphate, respectively, followed by drying (397 K), calcination (773 K), and reduction in H2 (923 K). The addition of CA increased the surface area, decreased the particle size, and increased the CO uptake of the MoP and Ni2P catalysts. At 623 K and 4.4 MPa, the Ni2P was 2.3 times more active than the MoP on a mass basis and 6 times more active on a site basis for the hydrodeoxygenation of 4-methylphenol. However, the Ni2P catalysts deactivated due to non-selective carbon deposition on the catalyst surface. Oxidation was excluded as a potential cause of deactivation over the Ni2P catalysts. The rate of deactivation was well described by an exponential decay law. Deactivation was eliminated by operation at higher H2 pressures (5.3 and 6.1 MPa) but the hydrogenation selectivity of the Ni2P increased at these conditions. No deactivation was observed over the MoP catalysts at the conditions of the present study.
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Acknowledgments
Financial support from the Natural Science and Engineering Research Council (NSERC) of Canada is gratefully acknowledged. The authors also wish to thank Bradford Ross from the Bioimaging Facility in the Department of Botany at the University of British Columbia for TEM measurements.
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Whiffen, V.M.L., Smith, K.J. A Comparative Study of 4-Methylphenol Hydrodeoxygenation Over High Surface Area MoP and Ni2P. Top Catal 55, 981–990 (2012). https://doi.org/10.1007/s11244-012-9883-2
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DOI: https://doi.org/10.1007/s11244-012-9883-2