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Local Turbulent Energy Dissipation Rate in an Agitated Vessel: Experimental and Turbulence Scaling

The result's identifiers

  • Result code in IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F46747885%3A24620%2F18%3A00005856" target="_blank" >RIV/46747885:24620/18:00005856 - isvavai.cz</a>

  • Alternative codes found

    RIV/67985874:_____/18:00484246 RIV/68407700:21220/18:00321434

  • Result on the web

    <a href="https://link.springer.com/content/pdf/10.1134/S0040579518010037.pdf" target="_blank" >https://link.springer.com/content/pdf/10.1134/S0040579518010037.pdf</a>

  • DOI - Digital Object Identifier

    <a href="http://dx.doi.org/10.1134/S0040579518010037" target="_blank" >10.1134/S0040579518010037</a>

Alternative languages

  • Result language

    angličtina

  • Original language name

    Local Turbulent Energy Dissipation Rate in an Agitated Vessel: Experimental and Turbulence Scaling

  • Original language description

    The 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 × 10–7 m2/s), (ii) a 28 vol % aqueous solution of glycol (&nu; = 2 × 10–6 m2/s), and (iii) a 43 vol % aqueous solution of glycol (&nu; = 3 × 10–6 m2/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: ε* = ε/(u4/&nu;) = const, vK/u = const, &Lambda;/&eta;K = const, &tau;&Lambda;/&tau;K = const, ε* = ε/((Nd)4/&nu;) = const, &Lambda;/d ∝ Re–1, &eta;K/d ∝ Re–1, vK/(Nd) = const, N&tau;&Lambda; ∝ R–1, N&tau;K ∝ Re–1, and ε/(Nq) ∝ 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.

  • Czech name

  • Czech description

Classification

  • Type

    J<sub>imp</sub> - Article in a specialist periodical, which is included in the Web of Science database

  • CEP classification

  • OECD FORD branch

    20501 - Materials engineering

Result continuities

  • Project

    Result was created during the realization of more than one project. More information in the Projects tab.

  • Continuities

    P - Projekt vyzkumu a vyvoje financovany z verejnych zdroju (s odkazem do CEP)

Others

  • Publication year

    2018

  • Confidentiality

    S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Data specific for result type

  • Name of the periodical

    Theoretical Foundations of Chemical Engineering

  • ISSN

    0040-5795

  • e-ISSN

  • Volume of the periodical

    52

  • Issue of the periodical within the volume

    1

  • Country of publishing house

    US - UNITED STATES

  • Number of pages

    13

  • Pages from-to

    122-134

  • UT code for WoS article

    000426897400016

  • EID of the result in the Scopus database

    2-s2.0-85042854670