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Simulation of Flow and Design of Agitated Large-Volume Biorectors

Identifikátory výsledku

  • Kód výsledku v 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>

  • Výsledek na webu

    <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>

Alternativní jazyky

  • Jazyk výsledku

    angličtina

  • Název v původním jazyce

    Simulation of Flow and Design of Agitated Large-Volume Biorectors

  • Popis výsledku v původním jazyce

    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.

  • Název v anglickém jazyce

    Simulation of Flow and Design of Agitated Large-Volume Biorectors

  • Popis výsledku anglicky

    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.

Klasifikace

  • Druh

    D - Stať ve sborníku

  • CEP obor

  • OECD FORD obor

    20704 - Energy and fuels

Návaznosti výsledku

  • Projekt

  • Návaznosti

    S - Specificky vyzkum na vysokych skolach

Ostatní

  • Rok uplatnění

    2017

  • Kód důvěrnosti údajů

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

Údaje specifické pro druh výsledku

  • Název statě ve sborníku

    Proceedings of the 25th EUBCE - Stockholm 2017

  • ISBN

    978-88-89407-17-2

  • ISSN

  • e-ISSN

    2282-5819

  • Počet stran výsledku

    7

  • Strana od-do

    1374-1380

  • Název nakladatele

    ETA - Florence

  • Místo vydání

    Florencie

  • Místo konání akce

    Stockholm

  • Datum konání akce

    12. 6. 2017

  • Typ akce podle státní příslušnosti

    WRD - Celosvětová akce

  • Kód UT WoS článku