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H-2 production from aqueous-phase reforming of glycerol over Cu-Ni bimetallic catalysts supported on carbon nanotubes

机译:在碳纳米管上负载的Cu-Ni双金属催化剂上甘油的水相重整制H-2

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Aqueous-phase reforming of glycerol was investigated over a series of Ni and Cu-Ni bimetallic catalysts supported on multiwalled carbon nanotubes (MWNT). The reaction was carried out in a continuous flow fixed bed reactor (240 degrees C, 40 atm) with a solution of 1 wt% glycerol in DI water at a flow rate of 0.05 mL/min. Amongst the catalysts tested, bimetallic 1Cu-12Ni/MWNT catalyst gave the higher H-2 selectivity (86%) and glycerol conversion (84%) than the benchmark 12Ni/MWNT catalyst. Irrespective of Cu and Ni ratio, bimetallic Cu-Ni catalysts showed higher selectivity and glycerol conversion towards H-2 production than the Ni catalyst. The presence of Cu in bimetallic catalysts resulted in suppression of undesirable methanation reaction. Catalysts characterized by XRD and XPS showed a significant peak shift of Ni in bimetallic Cu-Ni catalysts than the Ni catalyst, suggesting a strong interaction between Cu and Ni. Also H-2-TPR analysis showed that introducing Cu increased Ni reducibility. The bimetallic interaction is thought to be responsible for the lowered methane yield and ultimately, higher hydrogen yield observed. Copyright (C) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
机译:在多壁碳纳米管(MWNT)上负载的一系列Ni和Cu-Ni双金属催化剂上研究了甘油的水相重整。该反应在连续流固定床反应器(240℃,40atm)中,以1重量%甘油在DI水中的溶液以0.05mL / min的流速进行。在测试的催化剂中,双金属1Cu-12Ni / MWNT催化剂比基准12Ni / MWNT催化剂具有更高的H-2选择性(86%)和甘油转化率(84%)。不论Cu和Ni的比例如何,双金属Cu-Ni催化剂都比Ni催化剂具有更高的选择性和向H-2生产的甘油转化率。双金属催化剂中Cu的存在导致不希望的甲烷化反应的抑制。 XRD和XPS表征的催化剂显示双金属Cu-Ni催化剂中Ni的峰位移比Ni催化剂大,表明Cu和Ni之间有很强的相互作用。 H-2-TPR分析还表明,引入Cu提高了Ni的还原性。据认为,双金属相互作用是导致甲烷产率降低并最终导致氢产率提高的原因。 Hydrogen Energy Publications,LLC版权所有(C)2015。由Elsevier Ltd.出版。保留所有权利。

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