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Description of the Gas Transport through Dynamic Liquid Membrane.

  1. 1.
    SYSNO ASEP0474616
    Document TypeJ - Journal Article
    R&D Document TypeJournal Article
    Subsidiary JČlánek ve WOS
    TitleDescription of the Gas Transport through Dynamic Liquid Membrane.
    Author(s) Uchytil, Petr (UCHP-M) RID, SAI
    Setničková, Kateřina (UCHP-M) RID, ORCID, SAI
    Tseng, H.-H. (TW)
    Šíma, Vladimír (UCHP-M)
    Petričkovič, Roman (UCHP-M) RID, SAI
    Source TitleSeparation and Purification Technology. - : Elsevier - ISSN 1383-5866
    Roč. 184, AUG 31 (2017), s. 152-157
    Number of pages6 s.
    Languageeng - English
    CountryGB - United Kingdom
    Keywordsgas separation ; liquid membrane ; solurion-diffusion model
    Subject RIVCI - Industrial Chemistry, Chemical Engineering
    OECD categoryChemical process engineering
    Institutional supportUCHP-M - RVO:67985858
    UT WOS000403730500016
    EID SCOPUS85019008150
    DOI10.1016/j.seppur.2017.04.014
    AnnotationRecently we published a short communication about the gas separation by new type of membranes so called dynamic liquid membranes (DLM). The gas transport through water film was described by solution diffusion model commonly used for evaluation of the gas permeation through nonporous polymeric membranes, therefore this type of membranes is suitable for the separation of such systems where one of the components has high solubility in water. The separation ability of DLM based on thin water film for the binary mixtures of carbon dioxide and methane was investigated. Since direct measurement of permeate flux and its composition was not possible, we suggested three models for gas transport evaluation based on the use of simplifying assumptions. The obtained values of carbon dioxide permeate flux (permeance) from all models are very close, the highest difference is 6.3 mol % for feed composition 92 mol % CO2. Carbon dioxide flux is between 0.048 and 0.729 m3 m-2 h-1. The results of carbon dioxide permeation flux determined as difference between experimental values of the feed and retentate fluxes with permeate flux calculated using the Model 3 were in very good agreement.
    WorkplaceInstitute of Chemical Process Fundamentals
    ContactEva Jirsová, jirsova@icpf.cas.cz, Tel.: 220 390 227
    Year of Publishing2018
Number of the records: 1  

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