Evaluating the performance of non-precious metal based catalysts for sulfur-tolerance during the dry reforming of biogas

详细信息    查看全文

• 作者：Bappy Saha ; Ataullah Khan ; Hussameldin Ibrahim ; Raphael Idem
• 关键词：Biogas ; Dry reforming ; Non-precious catalysts ; Sulfur resistance ; Parametric study
• 刊名：Fuel
• 出版年：15 March, 2014
• 年：2014
• 卷：120
• 期：Complete
• 页码：202-217
• 全文大小：3312 K

文摘

A portfolio of catalysts with a nominal composition 15 wt.%Ni + (0/5 wt.%)Co/M_aO_x-N_aO_x-Al₂O₃ (where M = Mg, Ca, La, Y, Gd; N = Al, Zr) were synthesized and evaluated for biogas reforming application. Structure activity relations (SARs) were designed to help explain the significant difference in activity observed among the catalysts containing monometallic (Ni) and bimetallic species (Ni-Co) and among the bimetallic catalysts impregnated by altering the sequence of impregnation. The order of activity observed among the various catalyst formulations was: bi-metallic (reverse stepwise Co 鈫?#xA0;Ni) > bi-metallic (simultaneous Ni + Co) > mono-metallic > bi-metallic (stepwise Ni 鈫?#xA0;Co). From SARs it is established that high pore volume to surface area ratio, high metal dispersion, high reducibility and high support basicity are the essential traits of an active and stable catalyst. Analysis of variability (ANOVA) was performed to identify the main and interaction effects of various factors on both catalyst activity and catalyst textural properties. Impregnation sequence and promoter composition are found to have significant effects on both catalysts activity and its textural properties. Also, an empirical model equation that establishes a statistical relationship between the factors and the response variable was developed. In addition, a sensitivity analysis was performed to study the effect of surfactant to metal ratio, CH₄-to-CO₂ ratio, operating temperature, H₂S concentration, cobalt amount, and support basicity on catalyst performance.