文摘
The application of MnO<sub>xsub>-CeO<sub>2sub> as the low temperature selective catalytic reduction (SCR) catalyst to control NO<sub>xsub> emission from coal-fired power plants is extremely restricted due to the unrecoverable deactivation by SO<sub>2sub>. There is little SO<sub>2sub> in the flue gas from biomass-fired power plants, and the concentration of alkali metals in the flue gas after the electrostatic precipitator is very low, so the application of MnO<sub>xsub>-CeO<sub>2sub> may be possible to control NO<sub>xsub> emission from biomass-fired power plants. However, a very small amount of alkali metals showed a seriously negative effect on NO reduction over MnO<sub>xsub>-CeO<sub>2sub> such that both NO<sub>xsub> conversion and N<sub>2sub> selectivity obviously decreased. In this work, the mechanism of NO reduction over MnO<sub>xsub>-CeO<sub>2sub> and K-MnO<sub>xsub>-CeO<sub>2sub> was investigated by the transient reaction study and the kinetic parameters of NO reduction were obtained from the steady-state kinetic study. After comparison of the kinetic parameters, the mechanism of potassium deactivation on NO reduction over MnO<sub>xsub>-CeO<sub>2sub> was discovered. The decrease of the SCR activity of MnO<sub>xsub>-CeO<sub>2sub> after potassium deactivation was mainly attributed to the decrease of acid site and Mn<sup>4+sup> concentration on the surface, and the increase of N<sub>2sub>O selectivity was mainly related to the occurrence of N<sub>2sub>O formation over K-MnO<sub>xsub>-CeO<sub>2sub> through the Langmuir–Hinshelwood mechanism.