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    An Effectiveness–Number of Transfer Units Relationship for Evaporators With Non negligible Boiling Point Elevation Increases

    Source: Journal of Heat Transfer:;2016:;volume( 138 ):;issue: 012::page 121801
    Author:
    Thiel, Gregory P.
    ,
    Lienhard, V ,John H.
    DOI: 10.1115/1.4034055
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: An effectiveness number of transfer units (خµâ€“NTU) model is developed for use in evaporators where the evaporating stream: (1) comprises a volatile solvent and nonvolatile solute(s) and (2) undergoes a significant, but linear change in boiling point elevation (BPE) with increasing solute molality. The model is applicable to evaporators driven by an isothermal stream (e.g., steamdriven or refrigerantdriven) in parallel flow, counterflow, and crossflow configurations where the evaporating stream is mixed. The model is of use in a variety of process engineering applications as well as the sizing and rating of evaporators in highsalinity desalination systems.
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      An Effectiveness–Number of Transfer Units Relationship for Evaporators With Non negligible Boiling Point Elevation Increases

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    http://yetl.yabesh.ir/yetl1/handle/yetl/161710
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    contributor authorThiel, Gregory P.
    contributor authorLienhard, V ,John H.
    date accessioned2017-05-09T01:30:42Z
    date available2017-05-09T01:30:42Z
    date issued2016
    identifier issn0022-1481
    identifier otherht_138_12_121801.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/161710
    description abstractAn effectiveness number of transfer units (خµâ€“NTU) model is developed for use in evaporators where the evaporating stream: (1) comprises a volatile solvent and nonvolatile solute(s) and (2) undergoes a significant, but linear change in boiling point elevation (BPE) with increasing solute molality. The model is applicable to evaporators driven by an isothermal stream (e.g., steamdriven or refrigerantdriven) in parallel flow, counterflow, and crossflow configurations where the evaporating stream is mixed. The model is of use in a variety of process engineering applications as well as the sizing and rating of evaporators in highsalinity desalination systems.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleAn Effectiveness–Number of Transfer Units Relationship for Evaporators With Non negligible Boiling Point Elevation Increases
    typeJournal Paper
    journal volume138
    journal issue12
    journal titleJournal of Heat Transfer
    identifier doi10.1115/1.4034055
    journal fristpage121801
    journal lastpage121801
    identifier eissn1528-8943
    treeJournal of Heat Transfer:;2016:;volume( 138 ):;issue: 012
    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