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Heterogenous catalysis complete oxidation

It is true, however, that many catalytic reactions cannot be studied conveniently, under given conditions, with usual adsorption calorimeters of the isoperibol type, either because the catalyst is a poor heat-conducting material or because the reaction rate is too low. The use of heat-flow calorimeters, as has been shown in the previous sections of this article, does not present such limitations, and for this reason, these calorimeters are particularly suitable not only for the study of adsorption processes but also for more complete investigations of reaction mechanisms at the surface of oxides or oxide-supported metals. The aim of this section is therefore to present a comprehensive picture of the possibilities and limitations of heat-flow calorimetry in heterogeneous catalysis. The use of Calvet microcalorimeters in the study of a particular system (the oxidation of carbon monoxide at the surface of divided nickel oxides) has moreover been reviewed in a recent article of this series (19). [Pg.238]

A completely novel approach to technical electrolysis for anodic oxygen evolution from alkaline solution is the use of amorphous metals, i.e. chilled melts of nickel/cobalt mixtures whose crystallization is prevented by the addition of refractory metals like Ti, Zr, B, Mo, Hf, and P (46-51). For this type of material, enhanced catalytic activity in heterogeneous catalysis of gas-phase reactions has been observed (51). These amorphous metals are shown to be more corrosion resistant than the respective crystallized alloys, and the oxides being formed at their surfaces often exhibit a higher catalytic activity than those formed on ordered alloys, as shown by Kreysa (52-54). [Pg.105]

Alternative approaches have been proposed over the years. In none of these cases is there sufficient experimental evidence for truly heterogeneous catalysis. Frechet et al. (55) used a polyvinylpyridinium (PVP) material for supporting chlorochromate [Cr(IV)02Cl ] or dichromate [CrCVI Oy-]. Cr3+ can be immobilized by simple ion exchange on polymers such as Nation or on a Y zeolite (59, 60). However, it is doubtful whether these methods ensure complete Cr anchoring when the material is brought into contact with oxidants. Clark et al. (61) advocated the use of alumina-anchored dichromate. Particularly when a neutral alumina is used, surface-anchored species are formed ... [Pg.11]

It was previously stressed that apparent heterogeneous catalysis could be the result of the leaching of minute amount metal 7 10. By this work, we have demonstrated the existence of a new kind of "pseudo heterogeneous" catalysis a reaction in which the effective catalyst is dissolved to be active, but precipitates when the conversion is complete. These results constitute a new demonstration that recycling is not an appropriate proof of the heterogeneity of catalysis in liquid phase oxidation. [Pg.181]

In most cases, classical preparahon methods well known from heterogeneous catalysis have been applied for the preparation of the Pd parhcles/species supported on solids. However, the palladium parhcle size was inveshgated in detail in only a few reports in the literature. A strong influence of the preparation method, Pd particle size (dispersion) and of the chemical nature of the Pd nanoparticles (e.g. metal or oxide) has been reported in several papers. A rather complete overview of the literature on heterogeneous palladium systems applied to Heck catalysis including detailed discussion on mechanishc aspects is given in reviews by Biffis et al. [20] and Jones et al. [136] for the time before 2001 and 2006, respectively. [Pg.329]

Another related problem is associated with over-oxidation of the substrate, in the extreme case resulting in complete combustion. In the case of methane oxidation by FeO", for example, the activation of methane occurs with about 10% of the gas-kinetic collision rate, whereas those of the putative oxygenation products CH3OH, CH2O, and HCOOH occur on every collision [60]. With regard to applied catalysis this would imply that the oxidation products are oxidized faster by about one order of magnitude compared to methane as the initial substrate. In the particular context of heterogeneous oxidation... [Pg.16]

Zeolite catalysts may also be regarded as mixed oxides, but the crystallographic structures differ from the solids discussed above in that active sites for catalysis occur within the open lattice framework. In consequence, rate data are not directly comparable with similar observations for other heterogeneous reactions since the preexponential factors are calculated and reported on a different basis. For completeness, however, it is appropriate to mention here that instances of compensation behavior on zeolite catalysts are known. Taylor and Walker (282) described such an effect for the decomposition reactions of formic acid and of methyl forma te on cation-exchanged 13X molecular sieves, and comparable trends may be found in data reported for reactions of propene on similar catalysts (283). [Pg.303]


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See also in sourсe #XX -- [ Pg.95 , Pg.107 ]




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Catalysis heterogenized

Catalysis heterogenous

Catalysis, heterogenic

Heterogeneous catalysis

Oxidation catalysis

Oxidation heterogeneous

Oxides catalysis

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