Alumina support, role

Alumina supported sodium metaperiodate, which can be prepared by soaking the inorganic support with a hot solution of sodium metaperiodate, was also found to be a very convenient reagent for the selective and clean oxidation of sulphides to sulphoxides79. The oxidation reaction may be simply carried out by vigorous stirring of this solid oxidant with the sulphide solution at room temperature. As may be expected for such a procedure, solvent plays an important role in this oxidation and ethanol (95%) was found to be... 

X-ray photoelectron spectra, V3f Alumina-supported metals, multitechnique characterization, 37V-83 Aluminosilicates, Intercalates of, role In heterogeneous catalysis, V72-83 Alumlmin... 

It is worth of note that the role of the alumina support, which showed a non-negligible NO adsorption capacity in the presence of N02 [28], was not considered in the scheme due to its almost complete coverage by the Ba component in the Pt—Ba/y-Al203 (1/20/100 w/w) reference sample. 

In this study butyl acetate (AcOBu) was hydrogenolysed to butanol over alumina supported Pt, Re, RePt and Re modified SnPt naphtha reforming catalysts both in a conventional autoclave and a high throughput (HT) slurry phase reactor system (AMTEC SPR 16). The oxide precursors of catalysts were characterized by Temperature-Programmed Reduction (TPR). The aim of this work was to study the role and efficiency of Sn and Re in the activation of the carbonyl group of esters. 

The sulfidation mechanisms of cobalt- or nickel-promoted molybdenum catalysts are not yet known in the same detail as that of M0O3, but are not expected to be much different, as TPS patterns of Co-Mo/A1203 and Mo/Al203 are rather similar [56J. However, interactions of the promoter elements with the alumina support play an important role in the ease with which Ni and Co convert to the sulfidic state. We come back to this after we have discussed the active phase for the hydrodesulfurization reaction in more detail. 

The presence of oxygen enhances the catalyst stability. Breen et al. [187] investigated SRE over a range of oxide-supported metal catalysts. They concluded that the support plays an important role in the reaction. In fact, they observed that alumina-supported catalysts are very active at low temperatures for dehydration of ethanol to ethylene, which at higher temperatures (550 °C) is converted into H2, CO and CO2 as major products and CH4 as a minor product. The activities of the metal decrease in the order of Rh > Pd > Ni PS Pt. Ceria/zirconia-supported catalysts are more active and exhibit 100% conversion of ethanol at high space velocity and high temperature (650 °C). 

The role of iron clusters in Fischer-Tropsch catalysis has been the focus of considerable studies. Cagnoli et al. have recently studied the role of Fe clusters on silica and alumina supports for methanation.22 Chemisorption, catalysis and Mossbauer spectroscopy experiments were used to study the effect of dispersion and the role of various supports. Although several oxidation states of iron were observed, the focus of this research was on Fe clusters which were found to be on the order of 12 A crystal size. The authors proposed that metal support interactions were greater for silica than alumina supports and that selectivity differences between these catalysts were due to differences in surface properties of silica vs. alumina. Differences in selectivity for Fe/SiC>2 catalysts at different H2/CO ratios were attributed to differences in coadsorption of H2 and CO. Selectivity differences are difficult to explain in such systems even when only one metal is present. 

For a "co-impregnated" catalyst all, or the dominant fraction of, both Pt and Sn are located on the surface alumina support. For the following discussion we consider the role of only the support surface area, the metal concentration and the Sn/Pt ratio. First consider the case of a series of catalysts with a constant Pt loading but with variable Sn/Pt ratios. 

To obtain homogeneously distributed platinum on alumina, it is necessary to add a competitor ion to the solution. The usual competitor is HC1 [34, 47, 112] whose role is to act on the equilibrium between the platinum precursor in the solution S and that fixed on the alumina support A1 according to the reaction... 

Furthermore, it was clearly shown that noble metals, rhodium in particular, play an active role in promoting the OSC of the support [1,3-6,31]. It was shown for example that only Rh can really promote OSC on alumina catalysts [32,33]. Nevertheless the situation changes when ceria is added to alumina. A comparative study of alumina and ceria-alumina supported bimetallic catalysts [32,33] demonstrated the differences between those systems. Ceria-alumina catalysts were shown to have higher OSC values which do not depend on the composition of the bimetallic (Fig. 7.3). 

Not only the preparation method but also the support materials play a major role in producing a highly active and stable CPO catalyst. Instead of conventional alumina support, Sun et al.33 studied 10 wt % Ni/SiC and detected tubular and amorphous carbon after time-on-stream. However, the deactivated catalyst was easily regenerated through burning carbon in air, and the activity completely recovered to the fresh condition. Another advantage is that the catalyst can be directly used in the reaction without prereduction. 

Obviously a controlled preparation of bimetallic catalysts is needed in order to imderstand its role upon activity, selectivity and deactivation resistance. On this way, the controlled formation of surface bimetallic particles has been reported in catalysts prepared by the redox method [1]. In the present work, in order to define the role of the redox method in the surface properties of the R-Au alumina supported catalysts, we report the preparation, characterization and catalytic properties of a set of bimetallic catalysts with different gold content. The catalysts were evaluated using methylcyclopentane (MCP) hydrogenolysis as the test reaction. 

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