Identification of the chemical composition of the outermost surface layer is essential in order to correlate catalytic activity and surface chemical structure. However, there is no one technique which enables to clearly define the exact chemical structure of the species responsible for a given catalytic activity. Combination of different XPS-UPS, ISS spectroscopic techniques could help in this respect.

X-ray photoelectron spectroscopy is a valuable technique which provides information about the different chemical species presented in the upper 10 monolayers. Changes in the oxidation state(s) following, in situ, different treatments such as reduction by hydrogen will be closely monitored. Characterization of the Mo(3d) spin-orbit binding energies, the valence band energy region and the presence of a density of state structure at the Fermi level in parallel with ion scattering spectra ISS will provide important information in relation to the catalytic activity of the material under investigation. In this respect, it was observed that MoO₃ is reduced by hydrogen to the MoO₂ structure in a stable state at temperatures up to 673 K. At higher reduction temperature, lower valency metallic Mo(0) state is produced [14]. In this work, we present the XPS-UPS, ISS data following in situ samples reductions by hydrogen at 673 K for 12 h. Reference XPS binding energies for the Mo(3d_5/2,3/2) are: 232.65 and 235.85 eV for MoO₃, 231.7 and 234.9 eV for Mo₂O₅, 229.1 and 232.3 eV for MoO₂ and 227.7 and 230.85 eV for Mo(0). On the other hand, Ti(2p_3/2,1/2) binding energy values are observed at 458.5 and 464.2 eV for TiO₂ [15]. XP spectra of the Mo(3d) energy region of the MoTi and NaMoTi samples following in situ hydrogen reduction at 673 K for 12 h in comparison with the unreduced MoTi are presented in Figure 1. In the case of untreated MoTi sample, two well-defined spectral lines at 232.65 and 235.85 eV characteristics of Mo(3d_5/2,3/2) spin-orbit components of MoO₃ [15]. Most of the Mo is reduced to the MoO₂ state following sample exposure to hydrogen at 673 K for 12 h (Figure 1 (b)). This assignment is based on the Mo3d binding energies at 232.3 and 229.1 eV. The sample MoO₃ conversion to MoO₂ under these experimental conditions seems to be incomplete since lower concentration of MoO₃ and the interphase Mo₂O₅ are still observed (Figure 1(b)). The efficiency of MoO₃ reduction to MoO₂ in NaMoTi at 673 K seems to be more pronounced as could be observed in Figure 1(c). Most probably, this is due to the fact that addition of sodium to the molybdenum oxide results in the formation of separated structural NaMoTi unit structure as compared to a polymeric type MoO₃ structure. On the other hand, the Na1s binding energy measured at 1072.1 eV corresponds to Mo-ONa bond formation. Titanium 2p spin-orbit components at 458.5 and 464.2 eV remain unchanged in the two MoTi and NaMoTi before and after hydrogen reduction. This is a demonstration that TiO₂ is not affected by the MoO₃ reduction process.

The XPS of the valence band (VB) energy region of calcined MoTi shows a broad band which consists

mainly of O2p spectral line. No DOS structure is observed at the Fermi level which reflects the insulating properties of MoO₃ structure (Figure 2(a)). Exposure of the sample to hydrogen at 673 K for 12 h produces beside the O2p band, a relatively high density structure at the Fermi level (Figure 2(b)), attributed to the metallic properties of MoO₂. Higher resolution UPS of this energy region enables to clearly define the presence of s and p bands characteristics of the deformed rutile structure of MoO₂ [5,6]. Similar structure is observed in the case of the Na promoted system after hydrogen reduction (Figure 2(c)).

Ion scattering spectroscopy ISS is the appropriate technique in order to determine the elemental composition of the outermost surface area. As could be observed in Figure 3(a), the ISS of MoTi before hydrogen reduction reveals the presence of the constituent Mo, Ti and O beside the pollution C. Despite the fact that the equivalent of 5 monolayers of MoO₃ deposited on titania pellets, yet Ti is still observed as part of the surface structure. This indicates that Mo deposition is in form of aggregates and not uniformly as expected. Most likely, Mo deposition on

TiO₂ surface takes place in form of “para-crystalline MoO₃” phase that resembles bulk MoO₃ and takes the form of needle-like crystallites growing away from the support surface as postulated by Bond et al. [16]. Similar behavior is observed in the case of NaMoTi (Figure 3(c)). The presence of Na on the sample surface is due to its bonding to the Mo via surface oxygen (Mo-ONa).

The catalytic activity of MoO_2−x(OH)_y/TiO₂ (MoTi) is studied for 2-propanol as a function of reaction temperature (Figure 4). A conversion of 13.8% producing 72% propene and 28% propane. At higher reaction temperatures, all the reactant alcohol molecules were converted to propene and propane. However, the relative concentration of propene increases to a maximum of 76.7% at 473 K and decreases as a function of reaction temperature. This is in parallel increase in propane concentration to reach 92.5% at 673K (Figure 4). At 673 k, all propene molecules were hydrogenated to propane by the metallic function of the MoTi system. These results demonstrate the action of the acid and metal functions in the MoTisystem. The dehydration process of 2-propanol to pen-

tene, performed by the acid function of MoTi is the first and easier catalytic step. Hydrogenation of the produced propene to propane is catalyzed by the metallic function of MoTi. The efficiency of this second step catalytic process depends on the reaction temperature.

Different catalytic behavior takes place in the case of the modified system by sodium NaMoTi. No catalytic activity to very low of 21% at reaction temperatures below 500 K. Moreover, propene yield does not exceed 24 % although all reactant 2-propanol molecules were converted at 673 K reaction temperature (Figure 5). This is a clear indication of the neutralization of most, if not all, of the Brønsted Mo-OH acid by sodium Mo-ONa atoms. As a result, only the metallic function in MoO_2−x(OH)_y/ TiO₂ remains active. Consequently, propane, acetone and polymeric compounds were produced. The effect of sodium addition on the metallic properties of MoTi could be observed in the case of the dehydrogenation of 2-propanol to acetone (Figure 5). This catalytic reaction did not take place in MoTi. Sodium bronze formation is most probably the reason for enhancing the metallic function in the modified system [10-12].

Hydroisomerization of n-hexane to monobranched 2, 3-methylpentanes and 2,2 DMB, 2,3 DMB of relatively high octane numbers in order to boost gasoline and improve motor engine efficiency is an important catalytic process in oil industry. These catalytic reactions were rationalized in terms of bifunctional mechanism [1]. The first catalytic step in this process is the dehydrogenation of n-hexane to the hexene olefin, performed by the metallic function, followed by the isomerization of the ole fin via carbenium ion mechanism performed by Brønsted acid function, then hydrogenation of the olefin isomer by the metallic function. Highly dispersed Pt particles deposited on chlorinated alumina or zeolites are the most commonly used catalysts to achieve such objective.

Very low conversion of 4.0% to only 2,3 MP takes place at 523 K. This is due to relatively difficult first step dehydrogenation process of n-hexane to hexene which requires relatively strong metallic function. The conversion increases as the reaction temperature increases to reach 88.6% at 673 K (Figure 6). On the other hand, the isomerization selectivity decreases from 100 % at 523 K to 30.4% at 673 K in favor of cracking products. It is interesting to note the isomerization products 2MP/3MP distribution remains almost constant at 1.4 regardless of the reaction temperature, which corresponds to the thermodynamic equilibrium ration.

No catalytic activity of n-hexane on the NaMoTi modified system at reaction temperatures up to 600 K. Very low conversion of 1.9% is observed at 623 K and reaches 7.8% at 673 K. The main products are cracking which reflects the metallic character of this modified system. In fact, it is expected that dehydrogenation of nhexane to hexene will take place even at low 523 K reaction temperature, but the reverse hydrogenation will take place in the absence of an acid function on the catalyst surface. This is a clear demonstration that indeed the isomerization of n-hexane to branched species takes place in a concerted dehydrogenation to olefin/isomerization of the olefin/hydrogenation of the olefin, using metal-acidmetal functions in what is known as the bifunctional mechanism.

The isomerization activity and efficiency of the MoO_2−x(OH)_y/TiO₂ bifunctional are comparable to those of the industrial Pt deposited on chlorinated alumina. In fact, some advantages could be attributed to the Mo based catalyst which could summarized as follows: No toxic and corrosive chlorine is used, no toxic benzene compound is formed as a by-product, no sintering problems take place, molybdenum is much cheaper than platinum and the Mo catalyst is easy to regenerate in case of poisoning.

Additional hydrogenation catalytic reaction is presented in 1-hexene as compared to n-hexane in relation to the hydroisomerization reactions to produce high octane number branched species. This will enable to obtain further information concerning the exact catalytic active site(s) in MoTi and NaMoYi. Complete conversion of 1-hexene takes place on MoTi at all reaction temperature up to 673 K (Figure 7). Hydrogenation reaction to n-hexane (95.5%) and 4% 2,3-dimethyl pentanes were obtained at 423 K. In fact, isomerization reactions to different branched iC6 species increase at higher reaction temperature to reach a maximum 60% at temperatures between 573 K - 623 K (Figure 7). Beyond this temperature, the relative concentrations of cracking products

increase. This increase is in relation to thermodynamic effects. The 1-hexene isomerization to branched saturated compounds is interpreted as follows: Hydrogenation of 1-hexene to n-hexane takes place first as the easier catalytic process in this case. Consequently, the produced n-hexane undergoes the isomerization reactions to different branched compounds via the bifunctional mechanism as discussed previously.

The only major catalytic reaction of 1-hexene on the modified NaMoTi is the hydrogenation to n-hexane. In fact, all reactant 1-hexene were converted at all reaction temperatures between 423 K and 673 K (Figure 8). n-hexane is the only product up to 600 K and decreases to 79% at 673 K in favor of cracking products as expected due to thermodynamic effect a clear demonstration of the neutralization of the BrØnsted Mo-OH acidic group(s) in the bifunctional MoO_2−x(OH)_y/TiO₂ by the addition of sodium and producing mono-functional metallic MoO_2−x(OH)_y/TiO₂ system. Also, a demonstration that the hydroisomerization of n-hexane to different branched iC6 species is performed by a concerted bifunctional mechanism.