Eclectic trimetallic Ni–Co–Ru catalyst for the dry reforming of methane

Abstract

Ru-promoted Ni–Co catalysts supported on MgO–Al2O3 are tested for dry reforming activity in a fixed-bed reactor at atmospheric pressure. The effect of temperature and contact time is investigated, and the catalysts maintain high stability for up to 47 h on stream. The support surface area significantly affects dispersion, and whisker carbon is observed in spent samples with pore sizes higher than 15 nm. H2-TPR studies reveal the presence of spinels that are not completely reducible, yet the catalysts give remarkable activity. Four synthesis methods are tested for the support, with the sol-gel method in neutral conditions providing the best performance, with a small compromise on activity but a significant improvement in catalyst stability and no whisker carbon formation. Further work will optimize the Ni/Co ratio in the active phase to decrease the carbon buildup on the catalysts. © 2020 Hydrogen Energy Publications LLC

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Cobalt, Methane dry reforming, Nickel, Ruthenium, Whisker carbon, Alumina, Aluminum oxide, Atmospheric pressure, Carbon, Catalyst activity, Chemical reactors, Magnesia, Pore size, Sol-gel process, Sol-gels, Carbon formation, Catalyst stability, Dry reforming-of-methane, Effect of temperature, Fixed bed reactor, Neutral conditions, Support surfaces, Synthesis method, Catalyst supports

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