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Four different configurations of a 5 kW class shell-and-tube methane steam reformer with a low-temperature heat source

机译:带有低温热源的5 kW级壳管式甲烷蒸汽重整器的四种不同配置

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The methane steam reforming reaction is an extremely high endothermic reaction that. needs a high temperature heat source. Various fuel cell hybrid systems have been developed to improve the thermal efficiency of the entire system. This paper presents a low temperature steam reformer for those hybrid systems to maximize the utilization of energy from a low temperature waste heat source. In this study, the steam reformer has a shell and tube configuration that is divided into the following zones: the inlet heat exchanging zone, the reforming zone and the exit heat exchanging zone. Four different configurations for methane steam reformers are developed to examine the effect of heat transfer on the methane conversion performance of the low temperature steam reformer. The experimental results show diet the overall heat transfer area is a critical parameter in a high methane conversion rate. When the heat transfer area increases about 30%, the results showed elevated dry mole fractions of hydrogen about 3% with about 30 degrees C rise of reformer outlet temperature. (C) 2018 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:甲烷蒸汽重整反应是极高的吸热反应。需要高温热源。已经开发了各种燃料电池混合系统以提高整个系统的热效率。本文提出了一种用于这些混合系统的低温蒸汽重整器,以最大程度地利用低温废热源的能量。在这项研究中,蒸汽重整器具有壳管式结构,该结构分为以下区域:入口热交换区,重整区和出口热交换区。开发了用于甲烷蒸汽重整器的四种不同配置,以检查传热对低温蒸汽重整器的甲烷转化性能的影响。实验结果表明,饮食中的总传热面积是甲烷转化率高的关键参数。当传热面积增加约30%时,结果表明,随着重整器出口温度升高约30摄氏度,氢气的干摩尔分数提高了约3%。 (C)2018氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

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