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    Performance Evaluation of Dynamic Model of Compact Heat Exchange Reformer for High Temperature Fuel Cell Systems

    Source: Journal of Fuel Cell Science and Technology:;2014:;volume( 011 ):;issue: 001::page 11006
    Author:
    Ki, Jeongpill
    ,
    Kim, Daejong
    DOI: 10.1115/1.4025524
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Solid oxide fuel cell (SOFC) systems are the most advanced power generation system with the highest thermal efficiency. The current trend of research on the SOFC systems is focused on multikilowatt scale systems, which require either internal reforming within the stack or a compact external reformer. Even if the internal reforming within the SOFC stack allows compact system configuration, it causes significant and complicated temperature gradients within the stack, due to endothermic reforming reactions and exothermic electrochemical reactions. As an alternative solution to the internal reforming, an external compact heat exchange reformer (CHER) is investigated in this work. The CHER is based on a typical platefin counterflow or coflow heat exchanger platform, and it can save space without causing large thermal stress and degradation to the SOFC stack (i.e., eventually reducing the overall system cost). In this work, a previously developed transient dynamic model of the CHER is validated by experiments. An experimental apparatus, which comprises the CHER, air heater, gas heater, steam generator, several mass flow controllers, and controller cabinet, was designed to investigate steady state reforming performance of the CHER for various hot air inlet temperatures (thermal energy source) and steam to carbon ratios (SCRs). The transient thermal dynamics of the CHER was also measured and compared with simulations when the CHER is used as a heat exchanger with inert gas. The measured transient dynamics of CHER matches very well with simulations, validating the heat transfer model within the CHER. The measured molar fractions of reformate gases at steady state also agree well with the simulations validating the used reaction kinetics. The transient CHER model can be easily integrated into a total integrated SOFC system, and the model can be also used for optimal design of similar CHERs and provides a guideline to select optimal operating conditions of the CHERs and the integrated SOFC system.
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      Performance Evaluation of Dynamic Model of Compact Heat Exchange Reformer for High Temperature Fuel Cell Systems

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    contributor authorKi, Jeongpill
    contributor authorKim, Daejong
    date accessioned2017-05-09T01:08:58Z
    date available2017-05-09T01:08:58Z
    date issued2014
    identifier issn2381-6872
    identifier otherfc_011_01_011006.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/155104
    description abstractSolid oxide fuel cell (SOFC) systems are the most advanced power generation system with the highest thermal efficiency. The current trend of research on the SOFC systems is focused on multikilowatt scale systems, which require either internal reforming within the stack or a compact external reformer. Even if the internal reforming within the SOFC stack allows compact system configuration, it causes significant and complicated temperature gradients within the stack, due to endothermic reforming reactions and exothermic electrochemical reactions. As an alternative solution to the internal reforming, an external compact heat exchange reformer (CHER) is investigated in this work. The CHER is based on a typical platefin counterflow or coflow heat exchanger platform, and it can save space without causing large thermal stress and degradation to the SOFC stack (i.e., eventually reducing the overall system cost). In this work, a previously developed transient dynamic model of the CHER is validated by experiments. An experimental apparatus, which comprises the CHER, air heater, gas heater, steam generator, several mass flow controllers, and controller cabinet, was designed to investigate steady state reforming performance of the CHER for various hot air inlet temperatures (thermal energy source) and steam to carbon ratios (SCRs). The transient thermal dynamics of the CHER was also measured and compared with simulations when the CHER is used as a heat exchanger with inert gas. The measured transient dynamics of CHER matches very well with simulations, validating the heat transfer model within the CHER. The measured molar fractions of reformate gases at steady state also agree well with the simulations validating the used reaction kinetics. The transient CHER model can be easily integrated into a total integrated SOFC system, and the model can be also used for optimal design of similar CHERs and provides a guideline to select optimal operating conditions of the CHERs and the integrated SOFC system.
    publisherThe American Society of Mechanical Engineers (ASME)
    titlePerformance Evaluation of Dynamic Model of Compact Heat Exchange Reformer for High Temperature Fuel Cell Systems
    typeJournal Paper
    journal volume11
    journal issue1
    journal titleJournal of Fuel Cell Science and Technology
    identifier doi10.1115/1.4025524
    journal fristpage11006
    journal lastpage11006
    identifier eissn2381-6910
    treeJournal of Fuel Cell Science and Technology:;2014:;volume( 011 ):;issue: 001
    contenttypeFulltext
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    DSpace software copyright © 2002-2015  DuraSpace
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