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    Predicting Mixing Volumes in Serial Transport in Pipelines

    Source: Journal of Fluids Engineering:;2002:;volume( 124 ):;issue: 002::page 528
    Author:
    F. B. Freitas Rachid
    ,
    Department of Mechanical Engineering
    ,
    R. M. Baptista
    ,
    Senior Petroleum Engineer
    ,
    J. H. Carneiro de Araujo
    ,
    Computer Science
    DOI: 10.1115/1.1459078
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: This paper presents a model for predicting the contaminated mixing volume arising in pipeline batch transfers without physical separators. The proposed technique represents an improvement over the existing methods since it takes into account time-dependent flow rates and accurate concentration-varying axial dispersion coefficients. The governing equation of the model forms a nonlinear boundary-value problem that is solved by a finite element method coupled to the Newton’s method. A comparison among the theoretical predictions of this method, a field test, and other classical procedures show that the proposed method exhibits the best estimate over the whole range of admissible concentrations investigated.
    keyword(s): Flow (Dynamics) , Pipelines , Mixtures , Viscosity , Equations , Fluids , Pumps , Reynolds number AND Boundary-value problems ,
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      Predicting Mixing Volumes in Serial Transport in Pipelines

    URI
    http://yetl.yabesh.ir/yetl1/handle/yetl/126983
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    • Journal of Fluids Engineering

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    contributor authorF. B. Freitas Rachid
    contributor authorDepartment of Mechanical Engineering
    contributor authorR. M. Baptista
    contributor authorSenior Petroleum Engineer
    contributor authorJ. H. Carneiro de Araujo
    contributor authorComputer Science
    date accessioned2017-05-09T00:07:52Z
    date available2017-05-09T00:07:52Z
    date copyrightJune, 2002
    date issued2002
    identifier issn0098-2202
    identifier otherJFEGA4-27173#528_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/126983
    description abstractThis paper presents a model for predicting the contaminated mixing volume arising in pipeline batch transfers without physical separators. The proposed technique represents an improvement over the existing methods since it takes into account time-dependent flow rates and accurate concentration-varying axial dispersion coefficients. The governing equation of the model forms a nonlinear boundary-value problem that is solved by a finite element method coupled to the Newton’s method. A comparison among the theoretical predictions of this method, a field test, and other classical procedures show that the proposed method exhibits the best estimate over the whole range of admissible concentrations investigated.
    publisherThe American Society of Mechanical Engineers (ASME)
    titlePredicting Mixing Volumes in Serial Transport in Pipelines
    typeJournal Paper
    journal volume124
    journal issue2
    journal titleJournal of Fluids Engineering
    identifier doi10.1115/1.1459078
    journal fristpage528
    journal lastpage534
    identifier eissn1528-901X
    keywordsFlow (Dynamics)
    keywordsPipelines
    keywordsMixtures
    keywordsViscosity
    keywordsEquations
    keywordsFluids
    keywordsPumps
    keywordsReynolds number AND Boundary-value problems
    treeJournal of Fluids Engineering:;2002:;volume( 124 ):;issue: 002
    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