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    Exergy Destruction Mechanism of Coal Gasification by Combining the Kinetic Method and the Energy Utilization Diagram

    Source: Journal of Energy Resources Technology:;2017:;volume( 139 ):;issue: 006::page 62201
    Author:
    Wu, Handong
    ,
    Li, Sheng
    ,
    Gao, Lin
    DOI: 10.1115/1.4036957
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Gasification is the core unit of coal-based production systems and is also the site where one of the largest exergy destruction occurs. This paper reveals the exergy destruction mechanism of carbon gasification through a combined analysis of the kinetic method and the energy utilization diagram (EUD). Instead of a lumped exergy destruction using the traditional “black-box” and other models, the role of each reaction in carbon gasification is revealed. The results show that the exergy destruction caused by chemical reactions accounts for 86.3% of the entire carbon gasification process. Furthermore, approximately 90.3% of exergy destruction of chemical reactions is caused by the exothermal carbon partial oxidation reaction (reaction 1), 6.0% is caused by the carbon dioxide gasification reaction (reaction 2), 2.4% is caused by the steam gasification reaction (reaction 3), and 1.3% is caused by other reactions under the base condition. With increasing O2 content α and decreasing steam content β, the proportion of exergy destruction from reaction 1 decreases due to the higher gasification temperature (a higher energy level of energy acceptor in EUD), while the proportions of other reactions increase. This shows that the chemical efficiency is optimal when the extent of reactions 1 and 3 is equal and the shift reaction extent approaches zero at the same time.
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      Exergy Destruction Mechanism of Coal Gasification by Combining the Kinetic Method and the Energy Utilization Diagram

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    http://yetl.yabesh.ir/yetl1/handle/yetl/4236998
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    contributor authorWu, Handong
    contributor authorLi, Sheng
    contributor authorGao, Lin
    date accessioned2017-11-25T07:21:16Z
    date available2017-11-25T07:21:16Z
    date copyright2017/15/6
    date issued2017
    identifier issn0195-0738
    identifier otherjert_139_06_062201.pdf
    identifier urihttp://138.201.223.254:8080/yetl1/handle/yetl/4236998
    description abstractGasification is the core unit of coal-based production systems and is also the site where one of the largest exergy destruction occurs. This paper reveals the exergy destruction mechanism of carbon gasification through a combined analysis of the kinetic method and the energy utilization diagram (EUD). Instead of a lumped exergy destruction using the traditional “black-box” and other models, the role of each reaction in carbon gasification is revealed. The results show that the exergy destruction caused by chemical reactions accounts for 86.3% of the entire carbon gasification process. Furthermore, approximately 90.3% of exergy destruction of chemical reactions is caused by the exothermal carbon partial oxidation reaction (reaction 1), 6.0% is caused by the carbon dioxide gasification reaction (reaction 2), 2.4% is caused by the steam gasification reaction (reaction 3), and 1.3% is caused by other reactions under the base condition. With increasing O2 content α and decreasing steam content β, the proportion of exergy destruction from reaction 1 decreases due to the higher gasification temperature (a higher energy level of energy acceptor in EUD), while the proportions of other reactions increase. This shows that the chemical efficiency is optimal when the extent of reactions 1 and 3 is equal and the shift reaction extent approaches zero at the same time.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleExergy Destruction Mechanism of Coal Gasification by Combining the Kinetic Method and the Energy Utilization Diagram
    typeJournal Paper
    journal volume139
    journal issue6
    journal titleJournal of Energy Resources Technology
    identifier doi10.1115/1.4036957
    journal fristpage62201
    journal lastpage062201-9
    treeJournal of Energy Resources Technology:;2017:;volume( 139 ):;issue: 006
    contenttypeFulltext
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