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A series of Co1-xMgxO/Al2O3/FeCrAl catalysts (x=0-1) were prepared. The structures of the catalysts were characterized using XRD, SEM, and TPR analyses. The catalytic activity of the catalysts for methane combustion was evaluated in a continuous flow microreactor. The results indicated that the active washcoats adhered well on the FeCrAl foils. The phases in the catalysts were Co1-xMgxO solid solutions,α-Al2O3, andγ-Al2O3. The surface particle size of the catalysts varied with variations in the molar ratios of Co to Mg. The Co component of the Co1-xMgxO/Al2O3/FeCrAl catalysts played an important role in the catalytic activity for methane combustion. In the Co1-xMgxO/Al2O3/FeCrAl series catalyst (x=0.2-0.8), the catalytic activity in terms of x was in the order of 0.5>0.2>0.8 under the experimental conditions. The presence of Mg in these catalysts could promote the thermal stability to a large extent. There were strong interactions between the Co1-xMgxO oxides and the supports.
The series of Co1-xMgxO / Al2O3 / FeCrAl catalysts (x = 0-1) were prepared. The structures of the catalysts were characterized using XRD, SEM, and TPR analyzes. The catalytic activity of the catalysts for methane combustion was evaluated in a The results indicated that the active washcoats adhered well on the FeCrAl foils. The phases in the catalysts were Co1-xMgxO solid solutions, α-Al2O3, and γ-Al2O3. The surface particle size of the catalysts varied with variations in the The Co component of the Co1-xMgxO / Al2O3 / FeCrAl bass plays an important role in the catalytic activity for methane combustion. In the Co1-xMgxO / Al2O3 / FeCrAl series catalyst (x = 0.2-0.8) , the catalytic activity in terms of x was in the order of 0.5> 0.2> 0.8 under the experimental conditions. The presence of Mg in these resins could promote the thermal stability to a large extent. There were strong interactions between the Co1-xMgxO oxides and the supports