| Selective catalytic reduction(SCR) of NOx has been widely-used for the removal of NOx from Coal-fired power plant. V-based catalysts for above reaction are still problems, such as narrow reaction temperature range, oxidizing SO2 to SO3 easily, generating N2 O at a high temperature, toxicity of vanadia to the environment, etc. As a nontoxic and inexpensive material, ceria has excellent ability of oxygen storage and redox properties. However, regarding the effect of transitional metals on metal oxide catalysts, the SCR reaction was systematically investigated by using transitional metal oxides-CeO2/TiO2 catalysts in this dissertation.Firstly, several transitional metals were doped into CeO2/TiO2 catalysts. It was found that W doping could greatly improve the activity of the catalyst( NO conversion reached more than 90% at the temperature range of 275-500℃).Preparation parameters and operating parameters were studied based on the CeO2-WO3/TiO2 catalyst. When the calcinations temperature is 500℃, the activity of catalyst was highest. The appropriate mass ratio of CeO2, WO3 and TiO2 was 20, 10 and 100. High activity of catalyst was obtained within a wide range of gas hourly space velocity from 50,000 h-1 to 120,000 h-1. The presence of NH3 played an important role in SCR reaction. The optimal molar ratio of [NH3] and [NO] was 1. The activity of Ce O2-WO3/TiO2 catalyst was not affected when the volume fraction of oxygen was higher than 3%. Catalysts have good adaptability on NO concentration. It was also found that the resistance to SO2 and H2 O of catalysts was enhanced with the introduction of W.The excellent catalytic performance is associated with the highly dispersed Ce and Ti as well as the smaller particle diameter by the introduction of W. Meanwhile, the interaction between ceria and tungsten oxide could increase the amount of surface adsorbed oxygen and Ce3+, and promote oxygen storage capacity and redox ability.The reaction kinetics were studied on the selective catalytic reduction of NO with NH3 over the CeO2-WO3/TiO2 catalyst. The result showed that the reaction was a first-order reaction with NO, a zero-order reaction with NH3 and nearly quarter-order with O2. The reaction followed the Eley-Rideal mechanism model. The activation energy of CeO2-WO3/TiO2 catalysts was 32.1 kJ/mol. It was much lower than the values obtained on CeO2/TiO2 catalysts. |