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Promotion Effect of Cobalt-based Catalyst with Rare Earth for the Ethanol Steam Reforming

机译:基于钴的稀土催化剂促进促进效应乙醇蒸汽重整

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Catalytic performance of ethanol steam reforming (ESR) was investigated on praseodymium (Pr) modified ceriasupported cobalt oxide catalyst. The ceria-supported cobalt oxide (Ce-Co) catalyst was prepared by co-precipitation-oxidation (CPO) method, and the doped Pr (5 and 10 wt% loading) catalysts (Pr_5-Ce-Co and Pr_(10)-Ce-Co) were prepared by incipient wetness impregnation method. The reduction pretreatment under 250 and 400 C (H250 and H400) was also studied. All samples were characterized by XRD, TPR and TEM. Catalytic performance of ESR was tested from 250 to 500 C in a fixedbed reactor. The doping of Pr into the ceria lattice has significantly promoted the activity and reduced the coke formation. The products distribution also can be influenced by the different reduction pretreatment. The Pr_(10)-Ce-Co-H400 sample is a preferential ESR catalyst, where the hydrogen distribution approaches 73% at 475 C with less amounts (< 2%) of CO and CH_4.
机译:研究了乙醇蒸汽重整(ESR)的催化性能对镨(PR)改性Ceriasupported钴氧化物催化剂进行了研究。通过共沉淀 - 氧化(CPO)方法制备二氧化铈载钴(CE-CO)催化剂,以及掺杂的PR(5和10wt%负载)催化剂(PR_5-CE-CO和PR_(10) - CE-CO)通过初期湿润浸渍方法制备。还研究了250和400℃下的减少预处理(H250和H400)。所有样品的特征在于XRD,TPR和TEM。 ESR的催化性能在固定用物反应器中从250-500℃测试。 PR进入Ceria格子的掺杂显着促进了活性并降低了焦炭形成。产品分布也可能受到不同减少预处理的影响。 PR_(10)-CE-CO-H400样品是优先ESR催化剂,其中氢气分布在475℃下以较少量(<2%)的CO和CH_4接近73%。

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