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    Capillary rise in porous fibrous media during liquid immersion

    189060_189060.pdf (748.3Kb)
    Access Status
    Open access
    Authors
    Mullins, Benjamin
    Braddock, R.
    Date
    2012
    Type
    Journal Article
    
    Metadata
    Show full item record
    Citation
    Mullins, Benjamin J. and Braddock, Roger D. 2012. Capillary rise in porous fibrous media during liquid immersion. International Journal of Heat and Mass Transfer. 55 (21-22): pp. 6222-6230.
    Source Title
    International Journal of Heat and Mass Transfer
    DOI
    10.1016/j.ijheatmasstransfer.2012.06.046
    ISSN
    00179310
    Remarks

    NOTICE: this is the author’s version of a work that was accepted for publication in International Journal of Heat and Mass Transfer. Changes resulting from the publishing process, such as peer review, editing, corrections, structural formatting, and other quality control mechanisms may not be reflected in this document. Changes may have been made to this work since it was submitted for publication. A definitive version was subsequently published in International Journal of Heat and Mass Transfer, Volume 55, Issues 21-22, October 2012, Pages 6222-6230, http://dx.doi.org/10.1016/j.ijheatmasstransfer.2012.06.046

    URI
    http://hdl.handle.net/20.500.11937/40324
    Collection
    • Curtin Research Publications
    Abstract

    The modified Washburn equation has been further developed in this work, to examine capillary rise in porous media which are being immersed in liquid at a continuous rate. The capillary rise rate and/or properties of the media can be determined by a series of differential equations which govern the processes. The model was applied to oleophillic and oleophobic porous, fibrous media with generally good results, however it was found that the model needed to be fitted separately to the initial rise phase and to the longer-term (near-constant slope) phase. It was also found that a good agreement between the theory and experiment could be found if the porous media was contained inside a glass tube so that inflow could only occur from below and not from the sides of the filter. In order to model the insertion of media without this tube, a combination of a horizontal and a vertical capillary model was needed. The model could not be easily fitted to very thin, oleophillic media, and reasons for this are discussed; one likely reason being the inflow of liquid from the sides of the media. However, good agreement between the model and experiment could be found for equivalent media with an oleophobic coating and the same oil.

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