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Hydrogen production from ethanol steam reforming over Ni-Cu/ZnO catalyst

机译:乙醇蒸汽重整的氢气生产在Ni-Cu / ZnO催化剂上

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Hydrogen production by ethanol steam reforming over Ni-Cu/ZnO catalyst in the temperatures range of 250-550 °C was studied on a fixed bed reactor. The effects of reaction temperature and water/ethanol molar ratio on hydrogen production were investigated. The structure and surface characteristics of the catalyst were measured by scanning electron microscopy (SEM), X-ray diffraction (XRD) and differential thermal analyzer (TG-DSC). The results show that the Ni-Cu/ZnO catalyst has good catalytic performance with higher hydrogen yield of 4.87molH2/molEtOH reacted. A comparison of hydrogen production from ethanol steam reforming over Ni-Cu/ZnO catalyst with over a commercial catalyst was made in this paper.
机译:在固定床反应器上研究了在250-550℃的温度范围内通过乙醇蒸汽重整乙醇蒸汽重整的氢气产生。研究了反应温度和水/乙醇摩尔比对氢生产的影响。通过扫描电子显微镜(SEM),X射线衍射(XRD)和差分热分析仪(TG-DSC)测量催化剂的结构和表面特性。结果表明,Ni-Cu / ZnO催化剂具有良好的催化性能,氢产率为4.87molH 2 / MoletOH反应。本文制备了在Ni-Cu / ZnO催化剂上用乙醇蒸汽重整的氢气产生与商业催化剂的比较。

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