Influence of the Specific Oxide Support Phase

SUPPORT PHASE DOES NOT AFFECT OXIDATION REACTIONS 

P-25 Anataeo Rutile Brookite B-Phase TI02 Phases 

P 25 Anatase Rutila Brookita B-Phasa Ti02 Phaaaa 

---

The influence of the specific oxide support phase upon the structure and reactivity of the surface vanadia species was also recently investigated.54 A series of titania-supported vanadia catalysts were synthesized over a series of Ti02 supports possessing different phases (anatase, rutile, brookite and B). Raman and solid state vanadium-51 characterization studies revealed that the same surface vanadia species were present in all the different V20/ri02 catalysts54. The reactivity of the surface vanadia species on the different oxide supports was probed by methanol oxidation and the TOFs are shown in Figure 6 (all the catalysts contained 1% V205)... 

Essentially the same methanol oxidation TOFs were obtained on the different oxide supports. The Degussa P-25 titania support (90% anatase 10% rutile) was also examined, as shown in Figure 6, because it possesses very low levels of surface impurities and represents a good reference sample. The invariance of the methanol oxidation TOF with the specific phase of the titania support reveals that the oxidation reaction is controlled by a local phenomenon, the bridging V-O-Support bond, rather than long range effects, the structure of the 2 support. Thus, the phase of the oxide support does not appear to influence the molecular structure or reactivity of the surface vanadia species. 

In this work, the activity and selectivity of catalysts based on niobium and vanadium oxides supported on high surface area anatase Ti02 in ethane ODH have been investigated. Specifically, the influence of the cooperation of vanadium and niobium oxides supported phases as components inducing respectively redox and acid properties, together with the effect of the preparation conditions on the catal3dic performances have been studied. 

The role of metal-support interaction on the catalytic activity of carbon-supported Pt nanoparticles toward oxygen reduction and methanol oxidation was analyzed. It was observed that both dispersion and specific activity are influenced by the interaction of the active phase with the support, determining well-defined relationships that may be used for interpreting the electrochemical behavior of new, more advanced catalytic systems. 

Porous metal membranes are commercially available in stainless steel and some other alloys (e.g.. Inconel, Hastelloy) and they are characterized by a macroporous structure. On the other hand, porous ceramic membranes can be found commercially in various oxides and combination of oxides (e.g., Al203,li02,Zr02, Si02) and pore size families in the mesopore and macropore ranges (e.g., from 1 nm to several microns). Most of the literature studies on three-phase catalytic membrane reactors have been carried out by developing catalytic ceramic membranes. The deposition techniques for the preparation of catalytic ceramic membranes involve methods widely used for the preparation of traditional supported catalysts (Pinna, 1998), and methods specifically developed for the preparation of structured catalysts (Cybulski and Moulijn, 2006). Other methods to introduce a catalytic species on a porous support include the chemical vapour deposition and physical vapour deposition (Daub et al, 2001). The catalyst deposition method has a strong influence on the catalytic membrane reactor performance. 

Surface Area, Porosity, and Permeability. Some very interesting and important phenomena involve small particles and their surfaces. For example, SO2 produced from mining and smelting operations that extract metals such as Cu and Ph from heavy metal sulfide ores can be oxidized to SO3 in the atmosphere, thus contrihutingto acid rain problems. The reaction rate depends not only on the concentration of the SO2 bnt also on the siuTace area of any catalyst available, such as airborne dnst particles. The efficiency of a catalyst depends on its specific surface area, defined as the ratio of siuTace area to mass (17). The specific snrface area depends on both the size and shape, and is distinctively high for colloidalsized species. This is important in the catalytic processes nsed in many indnstries for which the rates of reactions occurring at the catalyst siuTace depend not only on the concentrations of the feed stream reactants bnt also on the sinface area of catalyst available. Since practical catalysts freqnently are snpported catalysts, some of the sinface area is more important than the rest. Since the supporting phase is usnally porous the size and shapes of the pores may influence the reaction rates as well. The final rate expressions for a catalytic process may contain all of these factors sinface area, porosity, and permeability. 

---