Article ID Journal Published Year Pages File Type
63930 Journal of Energy Chemistry 2014 6 Pages PDF
Abstract

MgO-modified Ni/Al2O3 catalysts with different Ni loadings were prepared and employed in dry reforming of methane (DRM). The effect of Ni loadings on the activity and coke formation of Ni/MgO-Al2O3 catalysts were investigated. The synthesized catalysts were characterized by XRD, N2 adsorption-desorption, SEM, TPO and TPR techniques. The obtained results showed that increasing nickel loading decreased the BET surface area and increased the catalytic activity and amount of deposited carbon. In addition, the effect of gas hourly space velocity (GHSV) and feed ratio were studied.

Graphical AbstractMg-modified Ni/Al2O3 catalysts were studied in dry reforming of methane. Effect of Ni loadings on the catalytic activity and coke formation of Ni/MgO-Al2O3 catalyst was studied. The catalytic activity and coke formation increased as the nickel content increased.Figure optionsDownload full-size imageDownload as PowerPoint slide

Related Topics
Physical Sciences and Engineering Chemical Engineering Catalysis
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