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    Effect of Tube Geometry and Curvature on Film Condensation in the Presence of a Noncondensable Gas

    Source: Journal of Thermal Science and Engineering Applications:;2015:;volume( 007 ):;issue: 001::page 11001
    Author:
    Li, Huijun
    ,
    Peng, Wenping
    ,
    Liu, Yingguang
    ,
    Ma, Chao
    DOI: 10.1115/1.4028345
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Based on the double boundary layer theory, a generalized mathematical model was developed to study the distributions of gas film, liquid film, and heat transfer coefficient along the tube surface with different geometries and curvatures for film condensation in the presence of a noncondensable gas. The results show that: (i) for tubes with the same geometry, gas film thickness, and liquid film thickness near the top of the tube decrease with the increasing of curvature and the heat transfer rate increases with it. (ii) For tubes with different geometries, one need to take into account all factors to compare their overall heat transfer rate including gas film thickness, liquid film thickness and the separating area. Besides, the mechanism of the drainage and separation of gas film and liquid film was analyzed in detail. One can make a conclusion that for free convection, gas film never separate since parameter A is always positive, whereas liquid film can separate if parameter B becomes negative. The separating angle of liquid film decreases with the increasing of curvature.
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      Effect of Tube Geometry and Curvature on Film Condensation in the Presence of a Noncondensable Gas

    URI
    http://yetl.yabesh.ir/yetl1/handle/yetl/159675
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    • Journal of Thermal Science and Engineering Applications

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    contributor authorLi, Huijun
    contributor authorPeng, Wenping
    contributor authorLiu, Yingguang
    contributor authorMa, Chao
    date accessioned2017-05-09T01:23:41Z
    date available2017-05-09T01:23:41Z
    date issued2015
    identifier issn1948-5085
    identifier othertsea_007_01_011001.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/159675
    description abstractBased on the double boundary layer theory, a generalized mathematical model was developed to study the distributions of gas film, liquid film, and heat transfer coefficient along the tube surface with different geometries and curvatures for film condensation in the presence of a noncondensable gas. The results show that: (i) for tubes with the same geometry, gas film thickness, and liquid film thickness near the top of the tube decrease with the increasing of curvature and the heat transfer rate increases with it. (ii) For tubes with different geometries, one need to take into account all factors to compare their overall heat transfer rate including gas film thickness, liquid film thickness and the separating area. Besides, the mechanism of the drainage and separation of gas film and liquid film was analyzed in detail. One can make a conclusion that for free convection, gas film never separate since parameter A is always positive, whereas liquid film can separate if parameter B becomes negative. The separating angle of liquid film decreases with the increasing of curvature.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleEffect of Tube Geometry and Curvature on Film Condensation in the Presence of a Noncondensable Gas
    typeJournal Paper
    journal volume7
    journal issue1
    journal titleJournal of Thermal Science and Engineering Applications
    identifier doi10.1115/1.4028345
    journal fristpage11001
    journal lastpage11001
    identifier eissn1948-5093
    treeJournal of Thermal Science and Engineering Applications:;2015:;volume( 007 ):;issue: 001
    contenttypeFulltext
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    DSpace software copyright © 2002-2015  DuraSpace
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