3 research outputs found

    Temperature-Dependent Kinetic Studies of the Chlorine Evolution Reaction over RuO<sub>2</sub>(110) Model Electrodes

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    Ultrathin single-crystalline RuO<sub>2</sub>(110) films supported on Ru(0001) are employed as model electrodes to extract kinetic information about the industrially important chlorine evolution reaction (CER) in a 5M concentrated NaCl solution under well-defined electrochemical conditions and variable temperatures. A combination of chronoamperometry (CA) and online electrochemical mass spectrometry (OLEMS) experiments provides insight into the selectivity issue: At pH = 0.9, the CER dominates over oxygen evolution, whereas at pH = 3.5, oxygen evolution and other parasitic side reactions contribute mostly to the total current density. From temperature-dependent CA data for pH = 0.9, we determine the apparent free activation energy of the CER over RuO<sub>2</sub>(110) to be 0.91 eV, which compares reasonably well with the theoretical value of 0.79 eV derived from first-principles microkinetics. The experimentally determined apparent free activation energy of 0.91 eV is considered as a benchmark for assessing future improved theoretical modeling from first principles

    Promoted Iron Nanocrystals Obtained via Ligand Exchange as Active and Selective Catalysts for Synthesis Gas Conversion

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    Colloidal synthesis routes have been recently used to fabricate heterogeneous catalysts with more controllable and homogeneous properties. Herein a method was developed to modify the surface composition of colloidal nanocrystal catalysts and to purposely introduce specific atoms via ligands and change the catalyst reactivity. Organic ligands adsorbed on the surface of iron oxide catalysts were exchanged with inorganic species such as Na<sub>2</sub>S, not only to provide an active surface but also to introduce controlled amounts of Na and S acting as promoters for the catalytic process. The catalyst composition was optimized for the Fischer–Tropsch direct conversion of synthesis gas into lower olefins. At industrially relevant conditions, these nanocrystal-based catalysts with controlled composition were more active, selective, and stable than catalysts with similar composition but synthesized using conventional methods, possibly due to their homogeneity of properties and synergic interaction of iron and promoters

    Ex Situ and Operando Studies on the Role of Copper in Cu-Promoted SiO<sub>2</sub>–MgO Catalysts for the Lebedev Ethanol-to-Butadiene Process

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    Dehydrogenation promoters greatly enhance the performance of SiO<sub>2</sub>–MgO catalysts in the Lebedev process. Here, the effect of preparation method and order of addition of Cu on the structure and performance of Cu-promoted SiO<sub>2</sub>–MgO materials is detailed. Addition of Cu to MgO via incipient wetness impregnation (IWI) or coprecipitation (CP) prior to wet-kneading with SiO<sub>2</sub> gave similar butadiene yields (∼40%) as when Cu was added to the already wet-kneaded catalyst. In contrast, the catalyst prepared by impregnation of Cu on SiO<sub>2</sub> first proved to be the worst catalyst of the series. TEM, XRD, and XPS analyses suggested that, for all catalyst materials, Cu<sup>2+</sup> forms a solid solution with MgO. This was confirmed by UV–vis, XANES, and EXAFS data, with Cu being found in a distorted octahedral geometry. As a result, the acid–base properties, as determined by Pyridine- and CDCl<sub>3</sub>–IR as well as NH<sub>3</sub>-TPD, are modified, contributing to the improved performance. Operando XANES and EXAFS studies of the evolution of the copper species showed that Cu<sup>2+</sup>, the only species initially present, is extensively reduced to a mixture of Cu<sup>0</sup> and Cu<sup>+</sup>, leaving only a limited amount of unreduced Cu<sup>2+</sup>. This formation of Cu<sup>0</sup> is the result of the reducing environment of the Lebedev process and is thought to be mainly responsible for the improved performance of the Cu-promoted catalysts
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