کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
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63930 | 48260 | 2014 | 6 صفحه PDF | دانلود رایگان |

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 as PowerPoint slide
Journal: Journal of Energy Chemistry - Volume 23, Issue 5, September 2014, Pages 633–638