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    The New Mathematical Models for Plain Fin and Tube Heat Exchangers With Dehumidification

    Source: Journal of Heat Transfer:;2015:;volume( 137 ):;issue: 003::page 31801
    Author:
    Pirompugd, Worachest
    ,
    Wang, Chi
    ,
    Wongwises, Somchai
    DOI: 10.1115/1.4029037
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: For evaluating performance of finandtube heat exchangers under dehumidifying conditions, the recent lumped approach models are based on the enthalpy potential or equivalent dry bulb temperature. This study proposes a new lumped approach model based on the dry bulb temperature difference. The concept of dry bulb temperature was first presented by McQuiston for derivation of fin efficiency under dehumidifying conditions in 1975. This concept is simpler than the concepts of enthalpy potential and equivalent dry bulb temperature. Nevertheless, it cannot be found that this concept is applied to the finandtube heat exchangers. Moreover, this study also presents the finite circular fin method (FCFM) based on the dry bulb temperature and equivalent dry bulb temperature. The FCFM was first presented in our published literature but it was based on the enthalpy potential. The FCFM is done by dividing the finandtube heat exchanger into many small segments. Then, the segments are divided into three cases: fully dry condition, fully wet condition, and partially wet condition. From the results, the new lumped approach model based on dry bulb temperature gives a good result. It is the simplest method for evaluating heat transfer performance of finandtube heat exchangers under fully wet conditions. For the FCFM, the heat and mass transfer characteristics obtained by dry bulb temperature and equivalent dry bulb temperature are nearly the same as those obtained by the enthalpy potential. However, the heat and mass transfer characteristics by the FCFM based on equivalent dry bulb temperature are higher than those obtained by the FCFM based on dry bulb temperature. This is because of the effect of the nonconstant term in the two methods. The correlations applicable for both fully wet and partially wet conditions for the FCFMs based on equivalent dry bulb temperature and dry bulb temperature are proposed to describe the heat and mass transfer characteristics for the present plain fin configuration.
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      The New Mathematical Models for Plain Fin and Tube Heat Exchangers With Dehumidification

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    https://yetl.yabesh.ir/yetl1/handle/yetl/158441
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    contributor authorPirompugd, Worachest
    contributor authorWang, Chi
    contributor authorWongwises, Somchai
    date accessioned2017-05-09T01:19:35Z
    date available2017-05-09T01:19:35Z
    date issued2015
    identifier issn0022-1481
    identifier otherht_137_03_031801.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/158441
    description abstractFor evaluating performance of finandtube heat exchangers under dehumidifying conditions, the recent lumped approach models are based on the enthalpy potential or equivalent dry bulb temperature. This study proposes a new lumped approach model based on the dry bulb temperature difference. The concept of dry bulb temperature was first presented by McQuiston for derivation of fin efficiency under dehumidifying conditions in 1975. This concept is simpler than the concepts of enthalpy potential and equivalent dry bulb temperature. Nevertheless, it cannot be found that this concept is applied to the finandtube heat exchangers. Moreover, this study also presents the finite circular fin method (FCFM) based on the dry bulb temperature and equivalent dry bulb temperature. The FCFM was first presented in our published literature but it was based on the enthalpy potential. The FCFM is done by dividing the finandtube heat exchanger into many small segments. Then, the segments are divided into three cases: fully dry condition, fully wet condition, and partially wet condition. From the results, the new lumped approach model based on dry bulb temperature gives a good result. It is the simplest method for evaluating heat transfer performance of finandtube heat exchangers under fully wet conditions. For the FCFM, the heat and mass transfer characteristics obtained by dry bulb temperature and equivalent dry bulb temperature are nearly the same as those obtained by the enthalpy potential. However, the heat and mass transfer characteristics by the FCFM based on equivalent dry bulb temperature are higher than those obtained by the FCFM based on dry bulb temperature. This is because of the effect of the nonconstant term in the two methods. The correlations applicable for both fully wet and partially wet conditions for the FCFMs based on equivalent dry bulb temperature and dry bulb temperature are proposed to describe the heat and mass transfer characteristics for the present plain fin configuration.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleThe New Mathematical Models for Plain Fin and Tube Heat Exchangers With Dehumidification
    typeJournal Paper
    journal volume137
    journal issue3
    journal titleJournal of Heat Transfer
    identifier doi10.1115/1.4029037
    journal fristpage31801
    journal lastpage31801
    identifier eissn1528-8943
    treeJournal of Heat Transfer:;2015:;volume( 137 ):;issue: 003
    contenttypeFulltext
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    DSpace software copyright © 2002-2015  DuraSpace
    نرم افزار کتابخانه دیجیتال "دی اسپیس" فارسی شده توسط یابش برای کتابخانه های ایرانی | تماس با یابش
    yabeshDSpacePersian