5 research outputs found
WO3/CeO2/TiO2 Catalysts for Selective Catalytic Reduction of NOx by NH3: Effect of the Synthesis Method
WO3/CeO2/TiO2, CeO2/TiO2 and WO3/TiO2 catalysts were prepared by wet impregnation. CeO2/TiO2 and WO3/TiO2 showed activity towards the selective catalytic reduction (SCR) of NOx by NH3, which was significantly improved by subsequent impregnation of CeO2/TiO2 with WO3. Catalytic performance, NH3 oxidation and NH3 temperature programmed desorption of wet-impregnated WO3/CeO2/TiO2 were compared to those of a flame-made counterpart. The flame-made catalyst exhibits a peculiar arrangement of W-Ce-Ti-oxides that makes it very active for NH3-SCR. Catalysts prepared by wet impregnation with the aim to mimic the structure of the flame-made catalyst were not able to fully reproduce its activity. The differences in the catalytic performance between the investigated catalysts were related to their structural properties and the different interaction of the catalyst components
Flame-Made WO<sub>3</sub>/CeO<sub><i>x</i></sub>‑TiO<sub>2</sub> Catalysts for Selective Catalytic Reduction of NO<sub><i>x</i></sub> by NH<sub>3</sub>
Materials
based on a combination of cerium–tungsten−titanium
are potentially durable catalysts for selective catalytic NO<sub><i>x</i></sub> reduction using NH<sub>3</sub> (NH<sub>3</sub>–SCR).
Flame-spray synthesis is used here to produce WO<sub>3</sub>/CeO<sub><i>x</i></sub>-TiO<sub>2</sub> nanoparticles, which are
characterized with respect to their phase composition, morphology,
and acidic properties and are evaluated by NH<sub>3</sub>–SCR.
HR-TEM and XRD revealed that flame-made WO<sub>3</sub>/CeO<sub><i>x</i></sub>-TiO<sub>2</sub> consists of mainly rutile TiO<sub>2</sub>, brannerite CeTi<sub>2</sub>O<sub>6</sub>, cubic CeO<sub>2</sub>, and a minor fraction of anatase TiO<sub>2</sub>. These phases
coexist with a large portion of amorphous mixed Ce–Ti phase.
The lack of crystallinity and the presence of brannerite together
with the evident high fraction of Ce<sup>3+</sup> are taken as evidence
that cerium is also present as a dopant in TiO<sub>2</sub> and is
well dispersed on the surface of the nanoparticles. Clusters of amorphous
WO<sub>3</sub> homogeneously cover all particles as observed by STEM.
Such morphology and phase composition guarantee short-range Ce–O–Ti
and Ce–O–W interactions and thus the high surface concentration
of Ce<sup>3+</sup>. The presence of the WO<sub>3</sub> layer and the
close Ce–O–W interaction further increased the Ce<sup>3+</sup> content compared to binary Ce–Ti materials, as shown
by XPS and XANES. The acidity of the materials and the nature of the
acid sites were determined by NH<sub>3</sub> temperature-programmed
desorption (NH<sub>3</sub>-TPD) and DRIFT spectroscopy, respectively.
TiO<sub>2</sub> possesses mainly strong Lewis acidity; addition of
cerium, especially the presence of surface Ce<sup>3+</sup> in close
contact with titanium and tungsten, induces Brønsted acid sites
that are considerably increased by the amorphous WO<sub>3</sub> clusters.
As a result of this peculiar element arrangement and phase composition,
10 wt % WO<sub>3</sub>/10 mol % CeO<sub><i>x</i></sub>-90
mol % TiO<sub>2</sub> exhibits the highest NO<sub><i>x</i></sub> reduction efficiency, which matches that of a V<sub>2</sub>O<sub>5</sub>–WO<sub>3</sub>/TiO<sub>2</sub> catalyst. Preliminary
activity data indicate that the flame-made catalyst demonstrates much
higher performance after thermal and hydrothermal aging at 700 °C
than the V-based analogue despite the presence of the rutile phase.
Ce<sup>3+</sup> remains the dominating surface cerium species after
both aging treatments, thus confirming its crucial role in NH<sub>3</sub>–SCR by Ce–W–Ti-based catalysts