Performance Evaluation of Dynamic Model of Compact Heat Exchange Reformer for High Temperature Fuel Cell SystemsSource: Journal of Fuel Cell Science and Technology:;2014:;volume( 011 ):;issue: 001::page 11006DOI: 10.1115/1.4025524Publisher: 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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contributor author | Ki, Jeongpill | |
contributor author | Kim, Daejong | |
date accessioned | 2017-05-09T01:08:58Z | |
date available | 2017-05-09T01:08:58Z | |
date issued | 2014 | |
identifier issn | 2381-6872 | |
identifier other | fc_011_01_011006.pdf | |
identifier uri | http://yetl.yabesh.ir/yetl/handle/yetl/155104 | |
description 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. | |
publisher | The American Society of Mechanical Engineers (ASME) | |
title | Performance Evaluation of Dynamic Model of Compact Heat Exchange Reformer for High Temperature Fuel Cell Systems | |
type | Journal Paper | |
journal volume | 11 | |
journal issue | 1 | |
journal title | Journal of Fuel Cell Science and Technology | |
identifier doi | 10.1115/1.4025524 | |
journal fristpage | 11006 | |
journal lastpage | 11006 | |
identifier eissn | 2381-6910 | |
tree | Journal of Fuel Cell Science and Technology:;2014:;volume( 011 ):;issue: 001 | |
contenttype | Fulltext |