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