Mechanistic study of the dry reforming of propane to synthesis gas over a Ni/Mg(Al)O catalyst

Abstract

The dry reforming of propane to synthesis gas over 2 wt.% Ni/Mg(Al)O has been investigated by means of partial pressure variation experiments, kinetic isotope effect and isotopic tracer studies, all at 600 °C. Partial pressure variation experiments gave reaction orders of 0.18 and 0.36 with respect to propane and carbon dioxide, respectively, indicating a high surface coverage under the chosen test conditions (C 3H 8:CO 2:H 2:N 2 (%) = 10:30:10:50, GHSV = 13333 ml/h g cat). Switching to a deuterated feed did not induce any kinetic isotope effect, revealing that C H bond rupture is not involved in the rate-limiting step. Isotopic tracer studies showed that the reverse water-gas shift reaction approaches equilibrium under the applied test conditions, demonstrating that CO 2 activation is fast. Temperature-programmed deuteration of a used catalyst showed that C 3 species dominate among the hydrocarbon species on the catalyst surface. Together, the above results led to the conclusion that C C bond rupture is the rate-determining step of reaction. Isotopic tracer studies further showed (1) that methane is mainly formed as a primary product of reaction by propane dissociation followed by hydrogenation on Ni sites, and (2) the primary reaction selectivity favors C oxidation to CO over C hydrogenation to methane. Co-feeding methane and propane with CO 2 showed that propane is converted significantly faster than methane.