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    Solar Steam Reforming of Methane in a Volumetric Receiver–Reactor With Different Types of Catalysts

    Source: Journal of Solar Energy Engineering:;2012:;volume( 134 ):;issue: 004::page 41013
    Author:
    Han Bin Do
    ,
    Jong Tak Jang
    ,
    Gui Young Han
    DOI: 10.1115/1.4007355
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: The steam reforming of methane is considered as one of the hydrogen production methods with solar thermal energy. In this study, lab-scale solar steam reforming of methane was examined under direct solar radiation from a solar simulator. A volumetric receiver–reactor with quartz window was used and three different catalysts were prepared, ICI 46-6, Ru/Al2 O3 , and Pd/Al2 O3 . An SiC foam absorber was employed as the catalyst supporter, and Al2 O3 was applied by wash-coating onto the SiC foam support. The characteristics of the steam reforming of methane in a solar receiver were investigated with respect to reaction temperature, space velocity, and steam/methane ratio. The composition of the product gas was analyzed by gas chromatography. From the experiment, it was observed that methane conversion was increased with temperature and above the temperature of 700 °C, methane conversion increased significantly and approached equilibrium conversion. The catalytic activities of the three catalysts were estimated in the same reaction conditions, and the Ru/Al2 O3 showed the highest activity followed by the Pd/Al2 O3 . The commercial ICI catalyst showed the lowest activity.
    keyword(s): Solar energy , Catalysts , Methane , Steam reforming AND Temperature ,
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      Solar Steam Reforming of Methane in a Volumetric Receiver–Reactor With Different Types of Catalysts

    URI
    http://yetl.yabesh.ir/yetl1/handle/yetl/150197
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    contributor authorHan Bin Do
    contributor authorJong Tak Jang
    contributor authorGui Young Han
    date accessioned2017-05-09T00:54:18Z
    date available2017-05-09T00:54:18Z
    date copyrightNovember, 2012
    date issued2012
    identifier issn0199-6231
    identifier otherJSEEDO-926222#041013_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/150197
    description abstractThe steam reforming of methane is considered as one of the hydrogen production methods with solar thermal energy. In this study, lab-scale solar steam reforming of methane was examined under direct solar radiation from a solar simulator. A volumetric receiver–reactor with quartz window was used and three different catalysts were prepared, ICI 46-6, Ru/Al2 O3 , and Pd/Al2 O3 . An SiC foam absorber was employed as the catalyst supporter, and Al2 O3 was applied by wash-coating onto the SiC foam support. The characteristics of the steam reforming of methane in a solar receiver were investigated with respect to reaction temperature, space velocity, and steam/methane ratio. The composition of the product gas was analyzed by gas chromatography. From the experiment, it was observed that methane conversion was increased with temperature and above the temperature of 700 °C, methane conversion increased significantly and approached equilibrium conversion. The catalytic activities of the three catalysts were estimated in the same reaction conditions, and the Ru/Al2 O3 showed the highest activity followed by the Pd/Al2 O3 . The commercial ICI catalyst showed the lowest activity.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleSolar Steam Reforming of Methane in a Volumetric Receiver–Reactor With Different Types of Catalysts
    typeJournal Paper
    journal volume134
    journal issue4
    journal titleJournal of Solar Energy Engineering
    identifier doi10.1115/1.4007355
    journal fristpage41013
    identifier eissn1528-8986
    keywordsSolar energy
    keywordsCatalysts
    keywordsMethane
    keywordsSteam reforming AND Temperature
    treeJournal of Solar Energy Engineering:;2012:;volume( 134 ):;issue: 004
    contenttypeFulltext
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