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Simulation of Flow and Design of Agitated Large-Volume Biorectors

The result's identifiers

  • Result code in IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F68407700%3A21220%2F17%3A00314815" target="_blank" >RIV/68407700:21220/17:00314815 - isvavai.cz</a>

  • Result on the web

    <a href="http://www.etaflorence.it/proceedings/?detail=14607&mode=topic&categories=0&items=%2D%2D&searchstring=jirout&limit=0" target="_blank" >http://www.etaflorence.it/proceedings/?detail=14607&mode=topic&categories=0&items=%2D%2D&searchstring=jirout&limit=0</a>

  • DOI - Digital Object Identifier

    <a href="http://dx.doi.org/10.5071/25thEUBCE2017-3CV.1.52" target="_blank" >10.5071/25thEUBCE2017-3CV.1.52</a>

Alternative languages

  • Result language

    angličtina

  • Original language name

    Simulation of Flow and Design of Agitated Large-Volume Biorectors

  • Original language description

    Industrial fermenters are designed as large-volume equipment with a volume of several tens of m3 with side-entry impellers. For this reason, experimental modeling of mixing in those batches is very difficult and subsequent scale-up of the obtained results. In the literature, we very often encounter modeling of these processes that the geometric similarity is not entirely keep and particularly the ratio of impeller diameter to vessel diameter. Another manner is the replacement of the modeling impeller, which during maintaining geometric similarity has a very small and during production unattainable diameter, by same directed jet generating same flow as the impeller. Comparison of the adequacy of this replacement on the base of CFD simulations has been done within this study. The results of the CFD simulations have been experimentally verified in the vessel with diameter 1.6 m. The results confirmed that it is not possible for correct modeling of the flow in the agitated batch of the large-volume fermenters utilize replacement of the side-entry impeller by jet with same diameter and flow. However, a large amount of high quality information about mixing in reactors with centrally placed impellers can be found in the literature. Consideration, based on CFD simulations and experiments, which data for centrally placed impellers may be used for designing the side-entry impellers has been another aim of this study.

  • Czech name

  • Czech description

Classification

  • Type

    D - Article in proceedings

  • CEP classification

  • OECD FORD branch

    20704 - Energy and fuels

Result continuities

  • Project

  • Continuities

    S - Specificky vyzkum na vysokych skolach

Others

  • Publication year

    2017

  • Confidentiality

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

Data specific for result type

  • Article name in the collection

    Proceedings of the 25th EUBCE - Stockholm 2017

  • ISBN

    978-88-89407-17-2

  • ISSN

  • e-ISSN

    2282-5819

  • Number of pages

    7

  • Pages from-to

    1374-1380

  • Publisher name

    ETA - Florence

  • Place of publication

    Florencie

  • Event location

    Stockholm

  • Event date

    Jun 12, 2017

  • Type of event by nationality

    WRD - Celosvětová akce

  • UT code for WoS article