By Umit S. Ozkan
This long-awaited reference resource is the 1st publication to target this crucial and scorching subject. As such, it presents examples from a wide range of fields the place catalyst layout has been in response to new insights and knowing, providing such sleek and critical issues as self-assembly, nature-inspired catalysis, nano-scale structure of surfaces and theoretical tools. With its inclusion of the entire helpful and robust instruments for the rational layout of catalysts, this can be a real "must have" booklet for each researcher within the box.
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Extra info for Design of heterogeneous catalysts : new approaches based on synthesis, characterization and modeling
Oxidative regeneration of the site is in competition with its deactivation by the combined action of hydrolysis and of mobile phosphate. Both are enhanced with growing performance – an argument for operating selective oxidation catalysts with comparatively low loads. The deactivation leads to growth of the active material into three-dimensional particles in much the same way as the pre-catalyst is grown from phosphoric acid, vanadium oxide and some reducing agent. It is anticipated that ﬁrst a clean surface of VOPO4 will result that may act as combustion catalyst (no site isolation) and thus enhance the energy supply to the system and augment the chemical potential of hydrolyzing water.
5(a) one observes, under kinetically relevant conditions of below 10% conversion, opposing trends for total and partial oxidation where not only the sign of the trend but also the shape of the curve indicate that different sites and different limiting factors operate in this reaction. The side product acetic acid is also not a direct precursor to total combustion. 5b). The MMO catalyst is a suitable system as it exhibits a high barrier towards direct combustion of the feed. 3. The difﬁcult step is the oxidation of the activated alkane for which acrolein stands only as proxy, as the structure of the real intermediate is unknown.
In the non-operating state the electron densities, as indicated by the XAS intensity changes, ﬁt more to a fully oxidized V¼O site and a more electron-rich V-O-V entity whose M–O bond distance (about 175 pm), as determined from the absolute energy position relative to that of V2O5, is much longer than expected  in the VPO structure. Based on our experimental information and the consistent opinion of the literature that VPO is a bulk pre-catalyst that undergoes transformations at least in the surface-near volume into an active phase that is not identical with the projections of the bulk VPO structure to its terminations, we attempt to construct a diagram highlighting the elements and its interrelations that control this vital process.