Numerical analysis of a cell-based indirect internal reforming tubular SOFC operating with biogas

A numerical study is performed on the thermal and electrochemical characteristics of a tubular solid oxide fuel cell (SOFC) employing the steam reforming of biogas in each individual cell unit but indirectly from the anode. The numerical model used in this study takes account of momentum, heat, and...

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Main Authors: Nishino, T, Szmyd, J
Format: Journal article
Language:English
Published: 2010
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author Nishino, T
Szmyd, J
author_facet Nishino, T
Szmyd, J
author_sort Nishino, T
collection OXFORD
description A numerical study is performed on the thermal and electrochemical characteristics of a tubular solid oxide fuel cell (SOFC) employing the steam reforming of biogas in each individual cell unit but indirectly from the anode. The numerical model used in this study takes account of momentum, heat, and mass transfer in and around the cell, including the effects of radiation, internal reforming, and electrochemical reactions. The biogas, which is fed into the reformer with steam, is assumed to be composed of methane (CH4) and carbon dioxide (CO2). The results show that, under the conditions of a constant average current density of 400 mA/cm2 and a constant fuel utilization of 80%, the terminal voltage of the cell decreases but only moderately as the proportion of CH4 in the fuel supplied to the reformer is reduced. It is also shown that temperature gradients within the cell decrease as the proportion of CH4 in the supplied fuel is reduced. These results are promising for the future use of biogas for this type of indirect internal reforming SOFC system. Copyright © 2010 by ASME.
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spelling oxford-uuid:a8d461db-23db-43c3-b344-7c83de5d03bc2022-03-27T03:04:10ZNumerical analysis of a cell-based indirect internal reforming tubular SOFC operating with biogasJournal articlehttp://purl.org/coar/resource_type/c_dcae04bcuuid:a8d461db-23db-43c3-b344-7c83de5d03bcEnglishSymplectic Elements at Oxford2010Nishino, TSzmyd, JA numerical study is performed on the thermal and electrochemical characteristics of a tubular solid oxide fuel cell (SOFC) employing the steam reforming of biogas in each individual cell unit but indirectly from the anode. The numerical model used in this study takes account of momentum, heat, and mass transfer in and around the cell, including the effects of radiation, internal reforming, and electrochemical reactions. The biogas, which is fed into the reformer with steam, is assumed to be composed of methane (CH4) and carbon dioxide (CO2). The results show that, under the conditions of a constant average current density of 400 mA/cm2 and a constant fuel utilization of 80%, the terminal voltage of the cell decreases but only moderately as the proportion of CH4 in the fuel supplied to the reformer is reduced. It is also shown that temperature gradients within the cell decrease as the proportion of CH4 in the supplied fuel is reduced. These results are promising for the future use of biogas for this type of indirect internal reforming SOFC system. Copyright © 2010 by ASME.
spellingShingle Nishino, T
Szmyd, J
Numerical analysis of a cell-based indirect internal reforming tubular SOFC operating with biogas
title Numerical analysis of a cell-based indirect internal reforming tubular SOFC operating with biogas
title_full Numerical analysis of a cell-based indirect internal reforming tubular SOFC operating with biogas
title_fullStr Numerical analysis of a cell-based indirect internal reforming tubular SOFC operating with biogas
title_full_unstemmed Numerical analysis of a cell-based indirect internal reforming tubular SOFC operating with biogas
title_short Numerical analysis of a cell-based indirect internal reforming tubular SOFC operating with biogas
title_sort numerical analysis of a cell based indirect internal reforming tubular sofc operating with biogas
work_keys_str_mv AT nishinot numericalanalysisofacellbasedindirectinternalreformingtubularsofcoperatingwithbiogas
AT szmydj numericalanalysisofacellbasedindirectinternalreformingtubularsofcoperatingwithbiogas