9 research outputs found
Mechanistic Study of Low-Temperature CO<sub>2</sub> Hydrogenation over Modified Rh/Al<sub>2</sub>O<sub>3</sub> Catalysts
The
hydrogenation of CO<sub>2</sub> on Rh/Al<sub>2</sub>O<sub>3</sub> catalysts
modified with Ni and K was studied by in situ and operando
DRIFTS spectroscopy comprising transient and isotopic exchange experiments
to study the influence of this modification on the catalytic performance
in CO and methane formation at 250–350 °C and to gain
mechanistic insight. Catalytic testing and spectroscopic studies revealed
that the modification with particularly K promotes the formation of
CO being the highest over Rh, K, Ni/Al<sub>2</sub>O<sub>3</sub>, whereas
methane formation is preferred over the unmodified catalyst. It was
found that CO<sub>2</sub> does not dissociatively adsorb but is adsorbed
at the support, forming mainly hydrogen carbonate, and in the presence
of K, also carbonate species. The dissociative adsorption of H<sub>2</sub> proceeds on Rh. The activated H<sub>2</sub> reacts mainly
with the hydrogen carbonate species forming CO adsorbed on Rh and
formate (F1) species stably adsorbed on the support. On the K-containing
catalysts, an additional formate species (F2) was identified as more
reactive than F1 formate and can act as a reaction intermediate in
the CO formation pathway. Furthermore, adsorbed formyl species were
detected, which are assumed to be intermediates in the methanation
reaction. The modifying additives change the surroundings of the Rh
particles. This influences the strength of CO adsorption and the activation
ability of Rh for H<sub>2</sub> dissociation. Thus, desorption of
the formed CO from the catalyst surface is favored, and the methanation
of CO is hindered. The modification with K enhances the ability for
CO<sub>2</sub> fixation by formation of additional carbonate species
which cover adsorption sites for unreactive F1 formate species and
favors the formation of reactive F2 formate species
Ternary VZrAlON Oxynitrides - Efficient Catalysts for the Ammoxidation of 3‑Picoline
Starting from previous binary VZrON
(VAlON) oxynitrides with high
(low) activity and low (high) selectivity, a new class of ternary
VZrAlON catalysts has been developed for the ammoxidation of 3-picoline
to 3-cyanopyridine (3-CP), which combine the beneficial properties
of the binary oxynitrides, leading to improved selectivity at retained
high activity and to the highest space-time yield of 3-CP ever measured
(488 g L<sup>–1</sup> h<sup>–1</sup>). This is attributed
to the formation of a special −⊡–V<sup>5+</sup>(O)–N–AlÂ(Zr)– surface moiety consisting of a
V<sup>5+</sup>î—»O species in the vicinity of a surface nitrogen
and an anion vacancy occupied by an electron, which is supposed to
provide optimum conditions for a double Mars–van Krevelen mechanism
comprising activation of gas-phase oxygen and ammonia via reversible
incorporation into the catalyst surface as well as an efficient electron
transport
Effects of Imidazole-Type Ligands in Cu<sup>I</sup>/TEMPO-Mediated Aerobic Alcohol Oxidation
Selective aerobic
oxidation of benzyl alcohol to benzaldehyde by
a (bpy)ÂCu<sup>I</sup>(IM)/TEMPO catalyst (IM represents differently
substituted imidazoles) has been studied by simultaneous operando
electron paramagnetic resonance/UV–vis/attentuated total reflectance
infrared spectroscopy in combination with cyclic voltammetry to explore
the particular role of imidazole in terms of ligand and/or base as
well as of its substitution pattern on the catalytic performance.
For molar ratios of IM/Cu ≥ 2, a (bpy)ÂCu<sup>I/II</sup>(IM)<sub>a</sub>(IM)<sub>b</sub> complex is formed, in which the Cu–N
distances and/or angles for the two IM ligands a and b are different.
The coordination of a second IM molecule boosts the oxidation of Cu<sup>I</sup> to Cu<sup>II</sup> and, thus, helps to activate O<sub>2</sub> by electron transfer from Cu<sup>I</sup> to O<sub>2</sub>. The rates
of Cu<sup>I</sup> oxidation and Cu<sup>II</sup> reduction and, thus,
the rates of benzaldehyde formation depend on R of the R–N
moiety in the IM ligand. Oxidation is fastest for R = H and alkyl,
while reduction is slowest for R = H. The Cu<sup>I</sup>/Cu<sup>II</sup> interplay leads to decreasing total benzaldehyde formation rates
in the order R (I+ effect) > R (conjugated system) > R = H
Heterostructured Copper–Ceria and Iron–Ceria Nanorods: Role of Morphology, Redox, and Acid Properties in Catalytic Diesel Soot Combustion
This
work reports the synthesis of heterostructured copper–ceria
and iron–ceria nanorods and the role of their morphology, redox,
and acid properties in catalytic diesel soot combustion. Microscopy
images show the presence of nanocrystalline CuO (9.5 ± 0.5 nm)
and Fe<sub>2</sub>O<sub>3</sub> (7.3 ± 0.5 nm) particles on the
surface of CeO<sub>2</sub> nanorods (diameter is 8.5 ± 2 nm and
length within 16–89 nm). In addition to diffraction peaks of
CuO and Fe<sub>2</sub>O<sub>3</sub> nanocrystallites, X-ray diffraction
(XRD) studies reveal doping of Cu<sup>2+</sup> and Fe<sup>3+</sup> ions into the fluorite lattice of CeO<sub>2</sub>, hence abundant
oxygen vacancies in the Cu/CeO<sub>2</sub> and Fe/CeO<sub>2</sub> nanorods,
as evidenced by Raman spectroscopy studies. XRD and Raman spectroscopy
studies further show substantial perturbations in Cu/CeO<sub>2</sub> rods, resulting in an improved reducibility of bulk cerium oxide
and formation of abundant Lewis acid sites, as investigated by H<sub>2</sub>-temperature-programmed reduction and pyridine-adsorbed Fourier
transform infrared studies, respectively. The Cu/CeO<sub>2</sub> rods
catalyze the soot oxidation reaction at the lowest temperatures under
both tight contact (Cu/CeO<sub>2</sub>; T50 = 358 °C, temperature
at which 50% soot conversion is achieved, followed by Fe/CeO<sub>2</sub>; T50 = 368 °C and CeO<sub>2</sub>; T50 = 433 °C) and loose
contact conditions (Cu/CeO<sub>2</sub>; T50 = 419 °C and Fe/CeO<sub>2</sub>; T50 = 435 °C). A possible mechanism based on the synergetic
effect of redox and acid properties of Cu/CeO<sub>2</sub> nanorods
was proposed: acid sites can activate soot particles to form reactive
carbon species, which are oxidized by gaseous oxygen/lattice oxygen
activated in the oxygen vacancies (redox sites) of ceria rods
Efficient VO<sub><i>x</i></sub>/Ce<sub>1–<i>x</i></sub>Ti<sub><i>x</i></sub>O<sub>2</sub> Catalysts for Low-Temperature NH<sub>3</sub>‑SCR: Reaction Mechanism and Active Sites Assessed by in Situ/Operando Spectroscopy
Supported V<sub>2</sub>O<sub>5</sub>/Ce<sub>1–<i>x</i></sub>Ti<sub><i>x</i></sub>O<sub>2</sub> (3, 5, and 7 wt
% V; <i>x</i> = 0, 0.1, 0.3, 0.5, 1) and bare supports have
been tested in the selective catalytic reduction (SCR) of NO by NH<sub>3</sub> at different gas hourly space velocities (GHSVs) and were
comprehensively characterized using XRD, pseudo in situ XPS, and UV–vis
DRS as well as EPR and DRIFTS in in situ and operando mode. The best
V/Ce<sub>1–<i>x</i></sub>Ti<sub><i>x</i></sub>O<sub>2</sub> (<i>x</i> = 0.3, 0.5) catalysts showed
almost 100% NO conversion and N<sub>2</sub> selectivity already at
190 °C with a GHSV value of 70000 h<sup>–1</sup>, which
belongs to the best performances observed so far in low-temperature
NH<sub>3</sub>-SCR of NO. The corresponding bare supports still converted
around 80% to N<sub>2</sub> under the same conditions. On bare supports,
SCR proceeds via a Langmuir–Hinshelwood mechanism comprising
the reaction of adsorbed surface nitrates with adsorbed NH<sub>3</sub>. On V/Ce<sub>1–<i>x</i></sub>Ti<sub><i>x</i></sub>O<sub>2</sub>, nitrate formation is not possible, and an Eley–Rideal
mechanism is working in which gaseous NO reacts with adsorbed NH<sub>3</sub> and NH<sub>4</sub><sup>+</sup>. Lewis and Brønsted acid
sites, though adsorption of NH<sub>3</sub>, do not scale with the
catalytic activity, which is governed rather by the redox ability
of the materials. This is boosted in the supports by replacing Ce
with the more redox active Ti and in catalysts by tight connection
of vanadyl species via O bridges to the support surface forming −Ce–O–VÂ(î—»O)–O–Ti–
units in which the equilibrium valence state of V under reaction conditions
is close to +5
Control of Bridging Ligands in [(V<sub>2</sub>O<sub>3</sub>)<sub>2</sub>(RXO<sub>3</sub>)<sub>4</sub>⊂F]<sup>−</sup> Cage Complexes: A Unique Way To Tune Their Chemical Properties
In this work, the new organic–inorganic
hybrid compound Ph<sub>4</sub>PÂ[(V<sub>2</sub>O<sub>3</sub>)<sub>2</sub>(PhAsO<sub>3</sub>)<sub>4</sub>⊂F] (<b>VAsF</b>) has
been prepared and characterized by single-crystal XRD and multinuclear
magnetic resonance (<sup>1</sup>H, <sup>19</sup>F, <sup>31</sup>P,
and <sup>51</sup>V). Redox properties and thermal stability have been
investigated by EPR, cyclic voltammetry, and thermal analysis in comparison
to its Ph<sub>4</sub>PÂ[(V<sub>2</sub>O<sub>3</sub>)<sub>2</sub>(PhPO<sub>3</sub>)<sub>4</sub>⊂F] (<b>VPF</b>) analogue. The <b>VAsF</b> cluster has a lower redox potential and higher electrochemical
stability in solution, while it is thermally less stable in the solid
state. Density functional theory (DFT) calculations showed that the
difference in the redox potential is due to the different electron
affinities of <b>VPF</b> and <b>VAsF</b>. With this approach
of modifying the type of the ligand of the molecular vanadium cage,
we hope to enhance the utility of such compounds as building blocks
for the design of new hybrid materials with desirable properties
Hierarchical ZSM‑5 Materials for an Enhanced Formation of Gasoline-Range Hydrocarbons and Light Olefins in Catalytic Cracking of Triglyceride-Rich Biomass
A hierarchical ZSM-5 material with
a high fraction of mesoporosity
coupled to well-preserved intrinsic zeolite characteristics has been
successfully prepared by postsynthesis modifications involving optimization
of base treatment and subsequent strong acid washing of commercial
Al-rich ZSM-5 (parent ZSM-5). The resulting hierarchical ZSM-5 material
was thoroughly characterized before being tested in the cracking of
triglyceride-rich biomass, i.e., model feedstock triolein and real
feedstock waste cooking oil under fluid catalytic cracking conditions.
The results show that the introduction of intracrystalline mesoporosity
enhances the utilization of zeolite acid sites by the enlarged external
surface, leading to an increased conversion. At the same time, it
partially suppresses the undesired secondary reactions by shortening
micropore diffusion path lengths. With such a hierarchical ZSM-5 material,
higher selectivities toward the desired products, i.e., gasoline-range
hydrocarbons and light olefins, than with commercial ZSM-5 have been
achieved
Solar Hydrogen Production by Plasmonic Au–TiO<sub>2</sub> Catalysts: Impact of Synthesis Protocol and TiO<sub>2</sub> Phase on Charge Transfer Efficiency and H<sub>2</sub> Evolution Rates
The activity of plasmonic Au–TiO<sub>2</sub> catalysts for
solar hydrogen production from H<sub>2</sub>O/MeOH mixtures was found
to depend strongly on the support phase (anatase, rutile, brookite,
or composites thereof) as well as on specific structural properties
caused by the method of Au deposition (sol-immobilization, photodeposition,
or deposition–precipitation). Structural and electronic rationale
have been identified for this behavior. Using a combination of spectroscopic
in situ techniques (EPR, XANES, and UV–vis spectroscopy), the
formation of plasmonic Au particles from precursor species was monitored,
and the charge-carrier separation and stabilization under photocatalytic
conditions was explored in relation to H<sub>2</sub> evolution rates.
By in situ EPR spectroscopy, it was directly shown that abundant surface
vacancies and surface OH groups enhance the stabilization of separated
electrons and holes, whereas the enrichment of Ti<sup>3+</sup> in
the support lattice hampers an efficient electron transport. Under
the given experimental conditions, these properties were most efficiently
generated by depositing gold particles on anatase/rutile composites
using the deposition–precipitation technique
Structure–Activity Relationships in Bulk Polymeric and Sol–Gel-Derived Carbon Nitrides during Photocatalytic Hydrogen Production
Photocatalytic hydrogen evolution
rates and structural properties
as well as charge separation, electron transfer, and stabilization
have been analyzed in advanced sol–gel-derived carbon nitrides
(SG-CN) pyrolyzed at different temperatures (350–600 °C)
and in bulk polymeric carbon nitride reference samples (CN) by XRD,
XPS, FTIR, UV–vis, Raman, and photoluminescence as well as
by in situ EPR spectroscopy. SG-CN samples show about 20 times higher
H<sub>2</sub> production rates than bulk CN. This is due to their
porous structure, partial disorder, and high surface area which favor
short travel distances and fast trapping of separated electrons on
the surface where they are available for reaction with protons. In
contrast, most of the excited electrons in bulk polymeric CN return
quickly to the valence band upon undesired emission of light, which
is responsible for their low catalytic activity