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Steam CO_2 Reforming of Methane over La_(1-x)Ce_xNiO_3 Perovskite Catalysts

机译:La_(1-x)Ce_xNiO_3钙钛矿催化剂上甲烷的蒸汽CO_2重整

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La_(1-x)Ce_xNiO_3 catalysts were prepared by modified EDTA-cellulose method. The prepared catalysts were characterized by various techniques such as N_2 physisorption, TPR, XRD, TPH, TEM-EDS and TG analysis. It was observed that the substitution of Ce resulted in easier reduction of the catalyst. The performance and stability of the catalysts for the steam CO_2 reforming of CH_4 were investigated under the reaction conditions of 600 ~ 900 °C, 1 bar and feed molar ratio of CH_4 : H_2O : CO_2 = 1 : 1 : 1. It was considered that the substitution of small amount of Ce in the catalyst could activate CH_4 and CO_2 and it led to higher conversions and CeO_2 suppressed carbon formation. However the substitution of large amount of Ce species led to the methanation of CO_2 as well as water gas shift reaction. It was found that the conversions of CH_4 and CO_2 decreased in the following order : La_(0.9)Ce_(0.1)NiO_3 > LaNiO_3 > La_(0.5)Ce_(0.5)NiO_3.
机译:采用改进的EDTA-纤维素法制备了La_(1-x)Ce_xNiO_3催化剂。制备的催化剂通过N_2物理吸附,TPR,XRD,TPH,TEM-EDS和TG分析等多种技术表征。观察到Ce的取代导致催化剂的还原更容易。在600〜900°C,1 bar和CH_4:H_2O:CO_2 = 1:1:1的进料摩尔比的反应条件下,研究了CH_4的蒸汽CO_2重整催化剂的性能和稳定性。催化剂中少量Ce的取代可以活化CH_4和CO_2,导致较高的转化率,而CeO_2抑制了碳的形成。然而,大量Ce的取代导致CO_2的甲烷化以及水煤气变换反应。发现CH_4和CO_2的转化率按以下顺序降低:La_(0.9)Ce_(0.1)NiO_3> LaNiO_3> La_(0.5)Ce_(0.5)NiO_3。

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