- Local turbulent energy dissipation rate in an agitated vessel: experi…
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Local turbulent energy dissipation rate in an agitated vessel: experimental and turbulence scaling

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    SYSNO ASEP0484246
    Document TypeJ - Journal Article
    R&D Document TypeJournal Article
    Subsidiary JČlánek ve WOS
    TitleLocal turbulent energy dissipation rate in an agitated vessel: experimental and turbulence scaling
    Author(s) Ditl, P. (CZ)
    Šulc, R. (CZ)
    Pešava, V. (CZ)
    Jašíková, D. (CZ)
    Kotek, M. (CZ)
    Kopecký, V. (CZ)
    Kysela, Bohuš (UH-J) SAI, ORCID, RID
    Source TitleTheoretical Foundations of Chemical Engineering. - : Pleiades Publishing - ISSN 0040-5795
    Roč. 52, č. 1 (2018), s. 122-134
    Number of pages13 s.
    Publication formPrint - P
    Languageeng - English
    CountryRU - Russian Federation
    Keywordsturbulence ; mixing ; particle image velocimetry ; turbulent energy dissipation rate ; energy spectrum function ; Rushton turbine
    Subject RIVJP - Industrial Processing
    OECD categoryFluids and plasma physics (including surface physics)
    R&D ProjectsGA16-20175S GA ČR - Czech Science Foundation (CSF)
    Institutional supportUH-J - RVO:67985874
    UT WOS000426897400016
    EID SCOPUS85042854670
    DOI https://doi.org/10.1134/S0040579518010037
    AnnotationThe hydrodynamics and the flow field in an agitated vessel were measured using 2-D time resolved particle image velocimetry (2-D TR PIV). The experiments were carried out in fully baffled cylindrical flat bottom vessels 300 and 400 mm in inner diameter. The 300 mm inner diameter tank was agitated by a Rushton turbine 100 mm in diameter, and the 400 mm inner diameter tank was agitated by a Rushton turbine 133 mm in diameter. Three liquids of different viscosities were used as the agitated liquid: (i) distilled water (nu = 9.35 x 10(-7) m(2)/s), (ii) a 28 vol % aqueous solution of glycol (nu = 2 x 10(-6) m(2)/s), and (iii) a 43 vol % aqueous solution of glycol (nu = 3 x 10(-6) m(2)/s). The velocity fields were measured at an impeller rotation speed in the range from 300 to 850 rpm, which covers the Reynolds number range from 50000 to 189000. This means that fullydeveloped turbulent flow was reached. The experiments were performed to investigate the applicability of the following relations: epsilon* = epsilon/(u (4)/nu) = const, vK/u = const, I >/eta K = const, tau(I >)/tau(K) = const, epsilon* = epsilon/((Nd)4/nu) = const, I >/d ae Re-1, eta K/d ae Re-1, vK/(Nd) = const, N tau(I >) ae R-1, N tau(K) ae Re-1, and epsilon/(Nq) ae Re. These formulas were theoretically derived in our previous work, using turbulence theory, in particular, using turbulence spectrum analysis. The correctness of the proposed relations is investigated by statistical hypothesis testing.
    WorkplaceInstitute of Hydrodynamics
    ContactSoňa Hnilicová, hnilicova@ih.cas.cz, Tel.: 233 109 003
    Year of Publishing2019
Number of the records: 1  

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