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Residence Time Distribution in a Narrow Bed of Solid Particles – Comparison of Modelling and Experiments

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    SYSNO ASEP0444603
    Document TypeC - Proceedings Paper (int. conf.)
    R&D Document TypeThe record was not marked in the RIV
    TitleResidence Time Distribution in a Narrow Bed of Solid Particles – Comparison of Modelling and Experiments
    Author(s) Hejda, Stanislav (UCHP-M) RID, ORCID, SAI
    Trávníčková, Tereza (UCHP-M) RID, ORCID, SAI
    Havlica, Jaromír (UCHP-M) RID, ORCID, SAI
    Stavárek, Petr (UCHP-M) RID, ORCID, SAI
    Křišťál, Jiří (UCHP-M) RID
    Source TitleProceedings of the 42nd International Conference of SSCHE. - Bratislava : Slovak Society of Chemical Engineering, 2015 / Markoš J. - ISBN 978-80-89475-14-8
    Pagess. 266
    Number of pages1 s.
    Publication formPrint - P
    ActionInternational Conference of Slovak Society of Chemical Engineering /42./
    Event date25.05.2015-29.05.2015
    VEvent locationTatranské Matliare
    CountrySK - Slovakia
    Event typeEUR
    Languageeng - English
    CountrySK - Slovakia
    Keywordsmicroreactor ; RTD ; CFD
    Subject RIVCI - Industrial Chemistry, Chemical Engineering
    R&D ProjectsGAP105/12/0664 GA ČR - Czech Science Foundation (CSF)
    Institutional supportUCHP-M - RVO:67985858
    AnnotationWe designed and constructed a laboratory device for the residence time distribution (RTD) experiments with packed bed microreactors. The device was design in a flexible way allowing an easy modification of the microchannel length and the size of packing particles. In this work, we dealt with hydrodynamics interactions between solid phase and liquid in static unstructured systems. In experiments, we used packed bed reactor with channel length between 25 and 150 mm and variable channel-to-particle ratio. The size of spherical glass particles was 2.4 mm and channel diameter 3.0 mm in this case. For determination of the residence time distribution (RTD) we used the dye tracer method. To improve the RTD acquisition system the two-tracer monitoring was used during measurements. In parallel, CFD simulations of corresponding device geometry were performed. For the verification of the output signal depending on the arrangement of the particles in the reactor, simulations were performed for two different particles geometrical configurations. Obtained results were compared with experiments and conclusions about effects of microreactor set up were discussed.
    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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