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Experimental study of methane dry reforming in an electrically heated reactor

机译:电加热反应器中甲烷干重整的实验研究

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Dry reforming of methane (DRM) is an interesting process as it allows for CO2 utilization and production of CO-richer syngas compared to methane steam reforming (SMR). Due to the endothermic reaction, reformer concepts suitable for high heat fluxes have to be developed. In this work, we therefore experimentally investigate a novel electrically heated reformer. Heating elements consisting of a FeCrAl alloy are coated with a LaNi0.95Ru0.05O3 catalyst at different washcoat thicknesses. The effects of different operating parameters on the performance of the DRM reaction and the reverse water gas shift (RWGS) reaction are evaluated. A combined operation of dry and steam reforming is also investigated. The results show a maximal CH4 conversion of 29.4% using one heating element at 900 degrees C. The H-2/CO ratio in the gas can be varied between 0.4 and 12.3 by combining steam and dry reforming. However, CH4 conversion decreased when steam is added. Copyright (C) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
机译:甲烷干重整(DRM)是一个有趣的过程,因为与甲烷蒸汽重整(SMR)相比,它可以利用CO2和生产富含CO的合成气。由于吸热反应,必须开发适用于高热通量的重整器概念。因此,在这项工作中,我们通过实验研究了一种新型的电加热重整器。由FeCrAl合金组成的加热元件以不同的修补基面涂层厚度涂覆LaNi0.95Ru0.05O3催化剂。评估了不同操作参数对DRM反应和逆水煤气变换(RWGS)反应性能的影响。还研究了干重整和蒸汽重整的组合操作。结果显示,使用一个加热元件在900摄氏度下,最大CH4转化率为29.4%。通过结合蒸汽和干重整,气体中的H-2 / CO比可以在0.4和12.3之间变化。但是,添加蒸汽后,CH4转化率降低。 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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