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Optimizing CO_2 hydrogenation to methane over CoFe bimetallic catalyst: Experimental and density functional theory studies

机译:优化CoFe Bimetallic催化剂对甲烷的CO_2氢化:实验和密度泛函理论研究

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Alumina supported cobalt (Co) and cobalt-iron (CoFe) catalysts are active for CO2 hydrogenation. Different amounts of CO and CH4 are produced depending on the Co and Fe content. The composition of alumina supported CoFe that maximizes the methane yield for the CO2 methanation reaction was determined using statistically defined experiments and response surface methodology. The catalyst that maximized the methane yield contained 21.47 wt% Co and 2.53 wt% Fe on this alumina support. X-ray diffraction and temperature programme reduction studies showed that Fe enhances the reducibility of cobalt oxides to metallic cobalt. Furthermore, transmission electron microscopy with elemental analysis showed uniform distribution of Co and Fe as an evidence of CoFe bimetallic alloy formation. DFT calculations were used to study the adsorption of CO2 and its dissociation into CO and O on Co and CoFe catalysts. A comparison of reaction energy profiles reveals that CO2 dissociation becomes difficult on the CoFe catalyst containing the optimized composition. The experimentally observed increase in methane formation over CoFe catalyst is probably due to this inhibition of CO formation via CO2 dissociation.
机译:氧化铝支持的钴(CO)和钴 - 铁(COFE)催化剂用于CO 2氢化。根据CO和Fe含量产生不同量的CO和CH 4。使用统计定义的实验和响应表面方法测定最大化CO 2甲烷化反应的甲烷产率的氧化铝负载的COFE的组成。最大化甲烷产率的催化剂含有21.47wt%的CO和2.53wt%Fe,对该氧化铝载体。 X射线衍射和温度减少研究表明,Fe增强了钴氧化物对金属钴的再减产。此外,具有元素分析的透射电子显微镜显示CO和Fe的均匀分布作为CoFe双金属合金形成的证据。使用DFT计算研究CO 2的吸附及其解离CO和COFE催化剂的CO和O.反应能谱的比较揭示CO 2离解在含有优化组合物的COFE催化剂上难以。通过CO 2离解的这种抑制,实验观察到CoFe催化剂上的甲烷形成的增加可能是由于CO 2的抑制作用。

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