La0.6Ca0.2Fe0.8Cu0.2O3, undoped (LF)
and Ca, Cu-doped (LCFC), powders, obtained
by different industrial procedures, are compared to evaluate reproducibility
and scale-up in different industrial synthetic approaches: flame spray
pyrolysis (FSP) and coprecipitation (COP). Also the effects of varying
composition (doping) and FSP process variability are considered as
comparative studies on morphological, crystallographic, redox and
compositional properties, and functional activity. A model reaction
(CO + NO) and reactions with an automotive exhaust mixture were carried
out. Unexpected results on the effectiveness of doping for
catalytic activity emerged. Samples with the same compositions proved
to be significantly affected by the synthesis, with variability within
the same process. The activity of LCFC COP is comparable to the FSP
analogue, at stoichiometric conditions, notwithstanding differences
highlighted by characterization. In an oxygen-deficient mixture, LCFC-COP
yields higher NO reduction and CO oxidation activity than LCFC-FSP.
The absence of Ca in the lattice was unexpectedly beneficial. The
doping effectiveness must be carefully checked for large-scale production.
Mn-based perovskites
obtained by two different industrial procedures
[flame spray pyrolysis (FSP) and co-precipitation (COP)] have been
extensively compared in terms of chemical, structural, and morphological
properties with the aim of evaluating how the upscale of complex catalysts
can affect the functionality. The transition between laboratory and
production scale is, in fact, usually not straightforward. The catalytic
activity was tested focusing on reactions of relevance in the abatement
of pollutants. In particular, CO-assisted NO reduction (which could
be also considered as a model reaction) and reactions with a synthetic
automotive exhaust mixture, including 10% steam and oxygen, were carried
out. The development of three-way catalysts is still a relevant question:
noble metal-free, efficient catalysts are even more necessary in hybrid
vehicles. For this purpose, the catalytic activity of the samples
has been correlated with the characterization results and thus with
the peculiar aspects of the production method. Relevant differences
have been observed between COP and FSP catalysts, in terms of the
specific surface area, surface composition, and presence of surface-active
sites. Also, the different efficiencies of inserting dopants in the
perovskite unit cell and thus in reducibility and ion mobility are
relevant. Despite having the same composition and crystalline structure,
the catalytic activity and the effect of pre-treatments are observed
to depend on the production procedure.
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