Pure monoclinic (m) and tetragonal (t) zirconia nanoparticles were readily synthesized from the reaction of inorganic zirconium salts (e.g., hydrated zirconyl nitrate) and urea in water and methanol, respectively, via a facile solvothermal method. The role of the solvents was crucial in the formation of the pure ZrO(2) phases, whereas their purity was essentially insensitive to other variables, including reaction temperature, reactant concentration, pH, and zirconium salts. Water as the solvent led to the transformation of hydrous ZrO(2) precipitates initially formed with tetragonal structures to thermodynamically more stable m-ZrO(2) via the dissolution-precipitation process, whereas methanol favored the removal of water molecules from the precursors via their reaction with urea, consequently maintaining the tetragonal structures. The obtained tetragonal samples were found to possess superior hydrothermal stability compared to those reported previously, which provides the possibility for systematically studying the effects of ZrO(2) phases on many catalytic reactions involving water as a reactant or product. Using these pure m- and t-ZrO(2) phases as supports, dispersed MoO(x) catalysts were synthesized at MoO(x) surface densities of approximately 5.0 Mo/nm(2), which is close to one monolayer of coverage. Characterization by X-ray diffraction and Raman spectroscopy confirmed that the pure ZrO(2) phases remained unchanged in the presence of the MoO(x) domains and the MoO(x) domains existed preferentially as 2D polymolybdate structures. The catalysts were subsequently examined for selective methanol oxidation as a test reaction. m-ZrO(2) support led to 2-fold greater oxidation rates than for t-ZrO(2) support, reflecting the higher intrinsic reactivity of the MoO(x) domains on m-ZrO(2). This is consistent with their higher reducibility probed by temperature-programmed reduction with H(2) (H(2) TPR). These observed effects of the ZrO(2) phases provide the basis for designing catalysts with tunable redox properties and reactivity.
Supported VO
x
/TiO2-rod catalysts
were studied by 51V MAS NMR at high field using a sample
spinning rate of 55 kHz. The superior spectral resolution allows for
the observation of at least five vanadate species. The assignment
of these vanadate species was carried out by quantum chemical calculations
of 51V NMR chemical shifts of model V surface structures.
Methanol oxidative dehydrogenation (ODH) was used to establish a correlation
between catalytic activity and the various surface V sites. It is
found that monomeric V species are predominant at low vanadium loadings
with two 51V NMR peaks observed at about −502 and
−529 ppm. V dimers with two bridged oxygens result in a peak
at about −555 ppm. Vanadate dimers and polyvanadates connected
by one bridged oxygen atom between two adjacent V atoms resonate at
about −630 ppm. A positive correlation is found between the
V dimers, giving rise to the −555 ppm peak, and the ODH rate,
and an even better correlation is obtained by including V monomer
contributions. This result suggests that surface V dimers related
to the −555 ppm peak and monomers are the primary active sites
for the methanol ODH reaction. Furthermore, a portion of the V species
is found to be invisible to NMR and the level of such invisibility
increases with decreasing V loading levels, suggesting the existence
of paramagnetic V species at the surface. These paramagnetic V species
are also found to be much less active in methanol ODH.
Metal-support interaction predominately determines the electronic structure of metal atoms in single-atom catalysts (SACs), largely affecting their catalytic performance. However, directly tuning the metal-support interaction in oxide supported SACs remains challenging. Here, we report a new strategy to subtly regulate the strong covalent metal-support interaction (CMSI) of Pt/CoFe2O4 SACs by a simple water soaking treatment. Detailed studies reveal that the CMSI is weakened by the bonding of H+, generated from water dissociation, onto the interface of Pt-O-Fe, resulting in reduced charge transfer from metal to support and leading to an increase of C-H bond activation in CH4 combustion by more than 50 folds. This strategy is general and can be extended to other CMSI-existed metal-supported catalysts, providing a powerful tool to modulating the catalytic performance of SACs.
Comparison of barium peroxide, Ba(OH) 2 and Ba(NO 3 ) 2 as the precursor of BaO for the preparation of NO x -storage BaO/Al 2 O 3 material was carried out. The as prepared materials were calcined at 550 and 800°C and characterized by N 2 physisorption, XRD, Raman and FT-IR spectroscopy. Measurements of the NO x storage performances of these BaO/Al 2 O 3 materials by NO 2 adsorption and NO x -TPD experiments showed that the use of barium peroxide as the precursor of BaO inhibited the formation of BaAl 2 O 4 and led to remarkable improvements in the thermal stability as well as NO x storage capacity of the final BaO/Al 2 O 3 material calcined at 800°C.
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