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    Numerical Analysis of Thermal Behavior of Small Solid Oxide Fuel Cell Systems

    Source: Journal of Fuel Cell Science and Technology:;2007:;volume( 004 ):;issue: 003::page 299
    Author:
    Takanobu Shimada
    ,
    Tohru Kato
    ,
    Yohei Tanaka
    DOI: 10.1115/1.2744049
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Recently, small solid oxide fuel cell (SOFC) systems have been developed for various applications because of their high performance. In such small generation systems, quick and frequent start-stops are often required. However, it is generally considered that these start-stops with SOFC systems are not preferable because SOFC systems are operated at high temperature. Also, quantitative studies on the thermal behavior of small SOFC systems are limited. The purpose of this paper is to obtain insight into the possibility of using small SOFC systems with quick and frequent start-stops. A simple two-dimensional numerical model for 1kW-class SOFC systems was fabricated to study this problem. The model consists of a cylindrical SOFC stack, a prereformer on the stack, a heat exchanger for exhaust gas, and a thermal insulator that covers the stack and the prereformer. Using this model, first, the characteristics of the power generation efficiency were estimated under various operating conditions. In addition, the validity of the modeling was verified. Next, the start-up dependence on their structure and operating conditions was investigated. Finally, for the cyclic daily start-up and shutdown (DSS) procedure, the total efficiency during a day was calculated when the energy loss during start-stops is considered. As a result of the analysis, the following points were found. First, the validity and accuracy of the modeling was established, and their efficiency under the rated condition becomes 60% (DC/HHV) at a steam-carbon ratio=2.5 and an oxygen utilization=50%. Next, the thickness of the thermal insulator (0.03W∕m∕K) is required to be more than 6cm to reduce the heat loss from the outer surface of the thermal insulator to <5% of the provided fuel energy (2kW) under the rated condition. In this case, it takes ca. 150min to start, if the fuel (methane) flow rate is 3.02NL∕min, which is equivalent to 2kW of heat flow. Finally, for the DSS operation, consisting of repetition of a 16h operation and an 8h stop in a day, the total efficiency decreases by ca. 1.5% from the rated power generation efficiency. Therefore, it is clarified that 1kW-class SOFC systems can be quite suitable even in the case where quick and frequent start-stops are required.
    keyword(s): Temperature , Solid oxide fuel cells , Fuels , Flow (Dynamics) , Heat AND Heat losses ,
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      Numerical Analysis of Thermal Behavior of Small Solid Oxide Fuel Cell Systems

    URI
    https://yetl.yabesh.ir/yetl1/handle/yetl/136113
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    • Journal of Fuel Cell Science and Technology

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    contributor authorTakanobu Shimada
    contributor authorTohru Kato
    contributor authorYohei Tanaka
    date accessioned2017-05-09T00:24:24Z
    date available2017-05-09T00:24:24Z
    date copyrightAugust, 2007
    date issued2007
    identifier issn2381-6872
    identifier otherJFCSAU-28930#299_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/136113
    description abstractRecently, small solid oxide fuel cell (SOFC) systems have been developed for various applications because of their high performance. In such small generation systems, quick and frequent start-stops are often required. However, it is generally considered that these start-stops with SOFC systems are not preferable because SOFC systems are operated at high temperature. Also, quantitative studies on the thermal behavior of small SOFC systems are limited. The purpose of this paper is to obtain insight into the possibility of using small SOFC systems with quick and frequent start-stops. A simple two-dimensional numerical model for 1kW-class SOFC systems was fabricated to study this problem. The model consists of a cylindrical SOFC stack, a prereformer on the stack, a heat exchanger for exhaust gas, and a thermal insulator that covers the stack and the prereformer. Using this model, first, the characteristics of the power generation efficiency were estimated under various operating conditions. In addition, the validity of the modeling was verified. Next, the start-up dependence on their structure and operating conditions was investigated. Finally, for the cyclic daily start-up and shutdown (DSS) procedure, the total efficiency during a day was calculated when the energy loss during start-stops is considered. As a result of the analysis, the following points were found. First, the validity and accuracy of the modeling was established, and their efficiency under the rated condition becomes 60% (DC/HHV) at a steam-carbon ratio=2.5 and an oxygen utilization=50%. Next, the thickness of the thermal insulator (0.03W∕m∕K) is required to be more than 6cm to reduce the heat loss from the outer surface of the thermal insulator to <5% of the provided fuel energy (2kW) under the rated condition. In this case, it takes ca. 150min to start, if the fuel (methane) flow rate is 3.02NL∕min, which is equivalent to 2kW of heat flow. Finally, for the DSS operation, consisting of repetition of a 16h operation and an 8h stop in a day, the total efficiency decreases by ca. 1.5% from the rated power generation efficiency. Therefore, it is clarified that 1kW-class SOFC systems can be quite suitable even in the case where quick and frequent start-stops are required.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleNumerical Analysis of Thermal Behavior of Small Solid Oxide Fuel Cell Systems
    typeJournal Paper
    journal volume4
    journal issue3
    journal titleJournal of Fuel Cell Science and Technology
    identifier doi10.1115/1.2744049
    journal fristpage299
    journal lastpage307
    identifier eissn2381-6910
    keywordsTemperature
    keywordsSolid oxide fuel cells
    keywordsFuels
    keywordsFlow (Dynamics)
    keywordsHeat AND Heat losses
    treeJournal of Fuel Cell Science and Technology:;2007:;volume( 004 ):;issue: 003
    contenttypeFulltext
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