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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 ASEP 0445186 Document Type J - Journal Article R&D Document Type Journal Article Subsidiary J Článek ve WOS Title Influence 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, SAISource Title Experimental Thermal and Fluid Science. - : Elsevier - ISSN 0894-1777
Roč. 67, OCT 2015 (2015), s. 2-5Number of pages 4 s. Action International conference on Heat Transfer and Fluid Flow in Microscale (HTFFM-V) /5./ Event date 22.04.2014 - 25.04.2014 VEvent location Marseilles Country FR - France Event type EUR Language eng - English Country US - United States Keywords porous media ; phase change ; vapor flow Subject RIV CI - Industrial Chemistry, Chemical Engineering R&D Projects 7AMB12AT010 GA MŠMT - Ministry of Education, Youth and Sports (MEYS) 7AMB14AT011 GA MŠMT - Ministry of Education, Youth and Sports (MEYS) Institutional support UCHP-M - RVO:67985858 UT WOS 000357223800002 EID SCOPUS 84922184538 DOI 10.1016/j.expthermflusci.2014.12.012 Annotation The 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. Workplace Institute of Chemical Process Fundamentals Contact Eva Jirsová, jirsova@icpf.cas.cz, Tel.: 220 390 227 Year of Publishing 2016
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