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Influence of the Flow Direction on the Mass Transport of Vapors through Membranes Consisting of Several Layers

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    SYSNO ASEP0445186
    Document TypeJ - Journal Article
    R&D Document TypeJournal Article
    Subsidiary JČlánek ve WOS
    TitleInfluence of the Flow Direction on the Mass Transport of Vapors through Membranes Consisting of Several Layers
    Author(s) Loimer, T. (AT)
    Uchytil, Petr (UCHP-M) RID, SAI
    Source TitleExperimental Thermal and Fluid Science. - : Elsevier - ISSN 0894-1777
    Roč. 67, OCT 2015 (2015), s. 2-5
    Number of pages4 s.
    ActionInternational conference on Heat Transfer and Fluid Flow in Microscale (HTFFM-V) /5./
    Event date22.04.2014 - 25.04.2014
    VEvent locationMarseilles
    CountryFR - France
    Event typeEUR
    Languageeng - English
    CountryUS - United States
    Keywordsporous media ; phase change ; vapor flow
    Subject RIVCI - Industrial Chemistry, Chemical Engineering
    R&D Projects7AMB12AT010 GA MŠMT - Ministry of Education, Youth and Sports (MEYS)
    7AMB14AT011 GA MŠMT - Ministry of Education, Youth and Sports (MEYS)
    Institutional supportUCHP-M - RVO:67985858
    UT WOS000357223800002
    EID SCOPUS84922184538
    DOI10.1016/j.expthermflusci.2014.12.012
    AnnotationThe flow of vapors with possible condensation is described, taking into account the energy balance, the Joule-Thomson effect and possible capillary condensation. For vapors close to saturation, the mass flux may be several times larger in one flow direction than in the opposite flow direction through an asymmetric membrane. As an example, the flow of isobutane through a porous ceramic membrane consisting of three different layers is theoretically investigated. The individual layers have different thicknesses with pore sizes of 10 nm for the separation layer, 100 nm for the middle layer and 6 μ m for the support layer. For a small ratio of the upstream pressure to the saturation pressure, the fluid does not condense within the porous membrane, and the mass flux is a few percent larger for the flow direction from the support to the separation layer than for the other flow direction. For larger upstream pressures, the fluid may condense and the mass flow can become about 7 times larger for one flow direction than for the opposite flow direction.
    WorkplaceInstitute of Chemical Process Fundamentals
    ContactEva Jirsová, jirsova@icpf.cas.cz, Tel.: 220 390 227
    Year of Publishing2016
Number of the records: 1  

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