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Methane steam reforming and ethanol steam reforming using a Ni(II)-Al(III) catalyst prepared from lamellar double hydroxides

机译:使用由层状双氢氧化物制备的Ni(II)-Al(III)催化剂进行甲烷蒸汽重整和乙醇蒸汽重整

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In this work the methane steam reforming (MSR) and the ethanol steam reforming (ESR) on Ni(II)-Al(III) catalyst prepared from lamellar double hydroxides (LDHs) as precursor are studied.A comprehensive analysis of the kinetics results obtained at different water/methane and water/ethanol feed ratio and its correlation with the structural characteristic and redox behavior of the catalyst is carried out.The results show evidence that the catalyst behavior is related with the presence of only one type of active site in the Ni/Al_2O_3 catalyst.The competition for the active sites between reactants is verified for MSR.This behavior is also observed in ethanol steam reforming since methane steam reforming determines the products distribution in the exit stream.There would be an optimum inlet water concentration that gives a maximum performance in terms of H_2 and CO_2 selectivity and,simultaneously,a minimum CO selectivity.This is a promissory result taking into account that the hydrogen flow entering a PEM fuel-cell requires a CO concentration lower than 20 ppm.
机译:本文研究了以层状双氢氧化物(LDHs)为前驱体的Ni(II)-Al(III)催化剂上的甲烷蒸汽重整(MSR)和乙醇蒸汽重整(ESR),对动力学结果进行了综合分析。在不同的水/甲烷和水/乙醇进料比下,进行了与催化剂的结构特征和氧化还原行为的相关性研究。结果表明,催化剂的行为与催化剂中仅存在一种类型的活性位有关。 Ni / Al_2O_3催化剂。通过MSR验证了反应物之间的活性位竞争。在乙醇蒸汽重整中也观察到了此行为,因为甲烷蒸汽重整决定了出口物流中的产物分布。 H_2和CO_2选择性方面的最高性能,同时CO选择性最低。这是考虑到氢气流量的必然结果进入PEM燃料电池需要的CO浓度低于20 ppm。

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