Alexander Parastaev

TL;DR: In this article, the particle size of the support (ceria-zirconia) can be used to tune the metal-support interactions, resulting in a substantially enhanced CO2 hydrogenation rate.

TL;DR: In this paper, the Pd/CeO2 single-atom catalysts were compared in low-temperature CO oxidation and display drastically different structural dynamics under the reaction conditions, showing that the oxidized Pd atoms in the impregnated catalyst were prone to reduction and sintering during CO oxidation whereas they remained intact on the surface of Pd-doped CeO2 derived by flame spray pyrolysis.

TL;DR: Non‐oxidative dehydroaromatization of methane (MDA) is shown to be governed by a hydrocarbon pool mechanism in which benzene is derived from secondary reactions of confined polyaromatic carbon species with the initial products of methane activation.

TL;DR: It is shown that catalyst productivity can be improved by nearly an order of magnitude by raising the reaction pressure to 15 bar, resulting in a lower coke selectivity and better utilization of the zeolite micropore space.

TL;DR: In this article, the promotional effect of MnO on Ni catalysts supported on silica-modified γ-Al2O3 (SA) was investigated in CO2 and CO methanation on catalysts with Mn/Ni atomic ratios between 0 and 0.25.