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A novel rotary reactor configuration for simultaneous production of hydrogen and carbon nanofibers

机译:同时生产氢气和碳纳米纤维的新型旋转反应器配置

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摘要

A novel reactor configuration, a rotary bed reactor (RBR), was used to study at large scale production the Catalytic Decomposition of Methane (CDM) into hydrogen and carbon nanofibers using a nickel-copper catalyst. The results were compared to those obtained in a fluidized bed reactor (FBR) under the same operating conditions. Tests carried out in the RBR provided higher hydrogen yields and more sustainable catalyst performance in comparison to the FBR. Additionally, the effect of the rotation speed and reaction temperature on the performance in the RBR of the nickel-copper catalyst was studied. The textural and structural properties of the carbon nanofibers produced were also studied by means of N_2 adsorption, SEM and XRD, and compared to those obtained in the FBR set-up under the same operating conditions.
机译:一种新颖的反应器配置,即旋转床反应器(RBR),用于研究大规模生产使用镍铜催化剂将甲烷催化分解(CDM)分解为氢和碳纳米纤维。将结果与在相同操作条件下在流化床反应器(FBR)中获得的结果进行比较。与FBR相比,在RBR中进行的测试提供了更高的氢气产率和更可持续的催化剂性能。此外,研究了转速和反应温度对镍-铜催化剂的RBR性能的影响。还通过N_2吸附,SEM和XRD研究了生产的碳纳米纤维的结构和结构性能,并将其与在相同操作条件下通过FBR装置获得的结构进行了比较。

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