Mn-based oxides are promising for the selective catalytic reduction (SCR) of NOx with NH at temperatures below 200 °C. There is a general agreement that combining Mn with another metal oxide, such as CeOx improves catalytic activity. However, to date, there is an unsettling debate on the effect of Ce.
View Article and Find Full Text PDFNi and NiSn supported on zirconia (ZrO) and on indium (In)-incorporated zirconia (InZrO) catalysts were prepared by a wet chemical reduction route and tested for hydrogenation of CO to methanol in a fixed-bed isothermal flow reactor at 250 °C. The mono-metallic Ni (5%Ni/ZrO) catalysts showed a very high selectivity for methane (99%) during CO hydrogenation. Introduction of Sn to this material with the following formulation 5Ni5Sn/ZrO (5% Ni-5% Sn/ZrO) showed the rate of methanol formation to be 0.
View Article and Find Full Text PDFThe presence of a Fe-FeAl2 O4 structure over an Fe-Al2 O3 catalysts is demonstrated to be vital for the catalytic methane decomposition (CMD) activity. After H2 reduction at 750 °C, Fe-Al2 O3 prepared by means of a fusion method, containing 86.5 wt % FeAl2 O4 and 13.
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