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    Mass Transfer in a Rigid Tube With Pulsatile Flow and Constant Wall Concentration

    Source: Journal of Fluids Engineering:;2010:;volume( 132 ):;issue: 008::page 81202
    Author:
    T. E. Moschandreou
    ,
    C. G. Ellis
    ,
    D. Goldman
    DOI: 10.1115/1.4002213
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: An approximate-analytical solution method is presented for the problem of mass transfer in a rigid tube with pulsatile flow. For the case of constant wall concentration, it is shown that the generalized integral transform (GIT) method can be used to obtain a solution in terms of a perturbation expansion, where the coefficients of each term are given by a system of coupled ordinary differential equations. Truncating the system at some large value of the parameter N, an approximate solution for the system is obtained for the first term in the perturbation expansion, and the GIT-based solution is verified by comparison to a numerical solution. The GIT approximate-analytical solution indicates that for small to moderate nondimensional frequencies for any distance from the inlet of the tube, there is a positive peak in the bulk concentration C1b due to pulsation, thereby, producing a higher mass transfer mixing efficiency in the tube. As we further increase the frequency, the positive peak is followed by a negative peak in the time-averaged bulk concentration and then the bulk concentration C1b oscillates and dampens to zero. Initially, for small frequencies the relative Sherwood number is negative indicating that the effect of pulsation tends to reduce mass transfer. There is a band of frequencies, where the relative Sherwood number is positive indicating that the effect of pulsation tends to increase mass transfer. The positive peak in bulk concentration corresponds to a matching of the phase of the pulsatile velocity and the concentration, respectively, where the unique maximum of both occur for certain time in the cycle. The oscillatory component of concentration is also determined radially in the tube where the concentration develops first near the wall of the tube, and the lobes of the concentration curves increase with increasing distance downstream until the concentration becomes fully developed. The GIT method proves to be a working approach to solve the first two perturbation terms in the governing equations involved.
    keyword(s): Flow (Dynamics) , Mass transfer , Equations , Frequency , Pulsatile flow , Fluctuations (Physics) , Diffusion (Physics) , Cycles AND Differential equations ,
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      Mass Transfer in a Rigid Tube With Pulsatile Flow and Constant Wall Concentration

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    https://yetl.yabesh.ir/yetl1/handle/yetl/143438
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    contributor authorT. E. Moschandreou
    contributor authorC. G. Ellis
    contributor authorD. Goldman
    date accessioned2017-05-09T00:38:10Z
    date available2017-05-09T00:38:10Z
    date copyrightAugust, 2010
    date issued2010
    identifier issn0098-2202
    identifier otherJFEGA4-27426#081202_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/143438
    description abstractAn approximate-analytical solution method is presented for the problem of mass transfer in a rigid tube with pulsatile flow. For the case of constant wall concentration, it is shown that the generalized integral transform (GIT) method can be used to obtain a solution in terms of a perturbation expansion, where the coefficients of each term are given by a system of coupled ordinary differential equations. Truncating the system at some large value of the parameter N, an approximate solution for the system is obtained for the first term in the perturbation expansion, and the GIT-based solution is verified by comparison to a numerical solution. The GIT approximate-analytical solution indicates that for small to moderate nondimensional frequencies for any distance from the inlet of the tube, there is a positive peak in the bulk concentration C1b due to pulsation, thereby, producing a higher mass transfer mixing efficiency in the tube. As we further increase the frequency, the positive peak is followed by a negative peak in the time-averaged bulk concentration and then the bulk concentration C1b oscillates and dampens to zero. Initially, for small frequencies the relative Sherwood number is negative indicating that the effect of pulsation tends to reduce mass transfer. There is a band of frequencies, where the relative Sherwood number is positive indicating that the effect of pulsation tends to increase mass transfer. The positive peak in bulk concentration corresponds to a matching of the phase of the pulsatile velocity and the concentration, respectively, where the unique maximum of both occur for certain time in the cycle. The oscillatory component of concentration is also determined radially in the tube where the concentration develops first near the wall of the tube, and the lobes of the concentration curves increase with increasing distance downstream until the concentration becomes fully developed. The GIT method proves to be a working approach to solve the first two perturbation terms in the governing equations involved.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleMass Transfer in a Rigid Tube With Pulsatile Flow and Constant Wall Concentration
    typeJournal Paper
    journal volume132
    journal issue8
    journal titleJournal of Fluids Engineering
    identifier doi10.1115/1.4002213
    journal fristpage81202
    identifier eissn1528-901X
    keywordsFlow (Dynamics)
    keywordsMass transfer
    keywordsEquations
    keywordsFrequency
    keywordsPulsatile flow
    keywordsFluctuations (Physics)
    keywordsDiffusion (Physics)
    keywordsCycles AND Differential equations
    treeJournal of Fluids Engineering:;2010:;volume( 132 ):;issue: 008
    contenttypeFulltext
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