Abstract
The catalytic activity, adsorption capacity, and pore structure of low-percentage nickel catalysts supported on γ-Al2O3or activated carbon and modified by tungsten heteropoly compounds are studied. The activity, selectivity, and thermal stability of the catalysts in the vapor-phase hydrogenation of olefins and aromatic hydrocarbons are higher than those for conventional nickel catalysts. The concentration of nickel in the catalysts is 10–15 times lower than that in commercial catalysts. However, the modified catalysts have higher specific surface areas of metal, higher dispersion, a uniform distribution of metal particles, and a pore-radius distribution other than in the support. The study of water adsorption and desorption showed that the heteropoly compound modifying the γ-Al2O3support covers the support surface completely, and supported nickel interacts with the active surface of the modifying agent rather than with Al2O3. A hydrogenation mechanism is proposed, which involves H2dissociation on Ni particles and the subsequent diffusion of hydrogen atoms via a spillover mechanism to the adsorbed organic compound with the participation of the OH groups of the modifying agent.
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