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    Development of Methanol Steam Reformer for Chemical Recuperation

    Source: Journal of Engineering for Gas Turbines and Power:;2001:;volume( 123 ):;issue: 004::page 727
    Author:
    T. Nakagaki
    ,
    T. Ogawa
    ,
    K. Murata
    ,
    Y. Nakata
    DOI: 10.1115/1.1359238
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: The purpose of the present work is to establish the design method of methanol steam-reformer for application to chemical recuperation in a gas turbine system. The reaction rate of the methanol steam-reforming was measured with a small amount of catalyst using the gaseous mixture of methanol, water, hydrogen, and carbon dioxide as a simulated product gas. The reaction rate equation could be expressed by power law of methanol mole fraction and total pressure. The reaction and heat transfer in the catalyst-packed bed was analyzed numerically using the reaction rate equation. The analytical results of temperature distribution and conversion were compared with the experimental results using a reforming tube. These results agreed well except for the region of high methanol conversion.
    keyword(s): Catalysts , Steam , Methanol , Temperature , Pressure , Water , Hydrogen , Mixtures , Carbon dioxide AND Equations ,
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      Development of Methanol Steam Reformer for Chemical Recuperation

    URI
    http://yetl.yabesh.ir/yetl1/handle/yetl/125127
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    • Journal of Engineering for Gas Turbines and Power

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    contributor authorT. Nakagaki
    contributor authorT. Ogawa
    contributor authorK. Murata
    contributor authorY. Nakata
    date accessioned2017-05-09T00:04:42Z
    date available2017-05-09T00:04:42Z
    date copyrightOctober, 2001
    date issued2001
    identifier issn1528-8919
    identifier otherJETPEZ-26807#727_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/125127
    description abstractThe purpose of the present work is to establish the design method of methanol steam-reformer for application to chemical recuperation in a gas turbine system. The reaction rate of the methanol steam-reforming was measured with a small amount of catalyst using the gaseous mixture of methanol, water, hydrogen, and carbon dioxide as a simulated product gas. The reaction rate equation could be expressed by power law of methanol mole fraction and total pressure. The reaction and heat transfer in the catalyst-packed bed was analyzed numerically using the reaction rate equation. The analytical results of temperature distribution and conversion were compared with the experimental results using a reforming tube. These results agreed well except for the region of high methanol conversion.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleDevelopment of Methanol Steam Reformer for Chemical Recuperation
    typeJournal Paper
    journal volume123
    journal issue4
    journal titleJournal of Engineering for Gas Turbines and Power
    identifier doi10.1115/1.1359238
    journal fristpage727
    journal lastpage733
    identifier eissn0742-4795
    keywordsCatalysts
    keywordsSteam
    keywordsMethanol
    keywordsTemperature
    keywordsPressure
    keywordsWater
    keywordsHydrogen
    keywordsMixtures
    keywordsCarbon dioxide AND Equations
    treeJournal of Engineering for Gas Turbines and Power:;2001:;volume( 123 ):;issue: 004
    contenttypeFulltext
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    DSpace software copyright © 2002-2015  DuraSpace
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