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The effect of temperature and initial methane concentration on carbon dioxide methanation on Ni based catalysts

机译:温度和初始甲烷浓度对镍基催化剂上二氧化碳甲烷化的影响

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摘要

A series of Ni based catalysts prepared by incipient wetness method were characterized by chemisorption and studied for CO2 methanation. Ru had apparently a positive effect on the active metal surface area, and thus the catalytic activity. The CO2 conversion was greatly affected by temperature where the conversion ranged from 12%-85% at temperatures of 300 to 400 oC on the 12% Ni/Al2O3 catalyst. At 350 oC, higher Ni loading resulted in increased activity. The incorporation of 0.5% Ru lead to a drastic increase in catalytic activity, which can be explained by increased reducibility and a synergetic effect between Ni and Ru, and was further enhanced by increased Ni loading. Addition of CH4 at twice the initial concentration of CO2 to the feed gas mixture was found to decrease the conversion from 52% to 48% at 350 oC on the 20% Ni/Al2O3 catalyst, whereas only a slight reduction in selectivity was observed. The results preliminary demonstrate that high methane purity can be achieved from a biogas feed stream over Ni based catalysts. 
机译:通过化学吸附对初湿法制备的一系列镍基催化剂进行了表征,并对CO2甲烷化进行了研究。 Ru显然对活性金属表面积具有积极作用,因此对催化活性也具有积极作用。 CO2转化率受温度的影响很大,在12%Ni / Al2O3催化剂上,在300至400 oC的温度下,转化率的变化范围为12%-85%。在350 oC,较高的Ni含量导致活性增加。掺入0.5%的Ru导致催化活性的急剧增加,这可以通过增加的还原性和Ni与Ru之间的协同作用来解释,并且可以通过增加Ni的负载而进一步增强。发现向原料气混合物中添加初始浓度为CO2两倍的CH4会使20%Ni / Al2O3催化剂在350 oC下的转化率从52%降低至48%,而观察到选择性仅略有降低。结果初步证明,在基于镍的催化剂上,沼气进料流可实现高甲烷纯度。

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