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A Comparative Study of the Effects of Water on Methane Oxidation over Pd@CeO2/Al2O3 and Pd@TiO2/Al2O3 Catalysts

机译:水对Pd @ CeO2 / Al2O3和Pd @ TiO2 / Al2O3催化剂对甲烷氧化作用的对比研究

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The development of a highly active catalyst for methane oxidation would have a significant impact on a number of energy-based technologies. In this work a comparative investigation of the catalytic performers of supported Pd@TiO2 and Pd@CeO2 for the application of methane oxidation have been presented. Catalytical activity of Pd@CeO2/Al2O3 was different than that of Pd@TiO2/Al2O3 catalyst. Under dry conditions Pd@CeO2/Al2O3 was more active than Pd@TiO2/Al2O3 where 100 % conversion of methane was achieved at 450°C, whereas for Pd@TiO2/Al2O3 complete oxidation of methane occurred at 570°C. in both cases addition of water into the feed resulted in a shift of methane conversions to higher temperatures, these effects were more detrimental over Pd@TiO2/Al2O3 catalyst where there was an exceptional decrease in methane conversions. In both cases increase in partial pressure of water resulted in increased deactivation of the catalysts.
机译:高活性催化剂的甲烷氧化催化剂对许多能源技术产生显着影响。在这项工作中,已经介绍了支持Pd @ TiO2和Pd @ CeO2的催化性表演者用于施用甲烷氧化的比较研究。 PD @ CeO2 / Al2O3的催化活性与Pd @ TiO 2 / Al2O3催化剂的催化活性不同。在干燥条件下,Pd @ CeO 2 / Al 2O3比Pd @ TiO 2 / Al 2 O 3更活跃,其中在450℃下达到甲烷的100%转化率,而Pd @ TiO 2 / Al2O3完全氧化甲烷在570℃下发生甲烷。在这两种情况下,将水加入到进料中导致甲烷转化的偏移到更高的温度,这些效果在Pd @ TiO 2 / Al2O3催化剂上更有害,其中甲烷转化的出色下降。在两种情况下,水的分压增加导致催化剂的失活增加。

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