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A Kinetic Study of SCR of NOx by NH_3 over γ Fe_2O_3 Nano-catalyst

机译:纳米Fe_2O_3在NH_3上NH_3催化还原NOx的动力学研究。

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In this study, we focus on the SCR reaction mechanism over γ Fe_2O_3 nano-catalyst. The kinetic parameters of the SCR reaction on γ Fe_2O_3 nano-catalyst were investigated in a differential reactor. Through kinetic research, it can be found that the reaction orders are 0.78-0.93, 0 and 0.9-0.11, respectively, for NO, NH_3 and O_2. The observed activation energy is 57.3kJ/mol. Combined with DRIFTS study, it can be concluded that increasing NH_3 concentration could not increase the rate of NO conversion because NH_3 could be strong adsorbed on the catalyst surface and the adsorption sites could be saturated by NH3 easily at low temperature, adsorbed NO_2 and nitrite species could be generated on the catalyst surface. The SCR reactbn is mainly followed L-H mechanism at the temperature below 270°C, and E-R mechanism at the temperature above 270 °C.
机译:在这项研究中,我们集中在γFe_2O_3纳米催化剂上的SCR反应机理。在差分反应器中研究了SCR反应在γFe_2O_3纳米催化剂上的动力学参数。通过动力学研究,发现NO,NH_3和O_2的反应阶数分别为0.78-0.93、0和0.9-0.11。观察到的活化能为57.3kJ / mol。结合DRIFTS研究,可以得出结论,增加NH_3的浓度并不能提高NO的转化率,因为NH_3在低温下很容易吸附在催化剂表面,并且吸附位点容易被NH3,吸附的NO_2和亚硝酸盐类物质饱和可能在催化剂表面产生。 SCR反应主要在温度低于270°C时遵循L-H机理,在温度高于270°C时遵循E-R机理。

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