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Experimental Investigation of Radial Gas Dispersion Coefficients in a Fluidized Bed

The result's identifiers

  • Result code in IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F68407700%3A21220%2F12%3A00194041" target="_blank" >RIV/68407700:21220/12:00194041 - isvavai.cz</a>

  • Result on the web

  • DOI - Digital Object Identifier

Alternative languages

  • Result language

    angličtina

  • Original language name

    Experimental Investigation of Radial Gas Dispersion Coefficients in a Fluidized Bed

  • Original language description

    Considering a fluidized bed boiler the combustion efficiency, NOX formation rate, flue gas desulphurization and fluidized bed heat transfer are all ruled by the gas distribution. In this work the tracer gas method was used for radial gas dispersion coefficient evaluation. CO2 was used as a tracer gas and the experiment was carried out in the bubbling fluidized bed cold model. As the bed material ceramic balls were used. The effect of gas velocity, radial position and bed height was investigated

  • Czech name

  • Czech description

Classification

  • Type

    J<sub>x</sub> - Unclassified - Peer-reviewed scientific article (Jimp, Jsc and Jost)

  • CEP classification

    JE - Non-nuclear power engineering, energy consumption and utilization

  • OECD FORD branch

Result continuities

  • Project

  • Continuities

    Z - Vyzkumny zamer (s odkazem do CEZ)

Others

  • Publication year

    2012

  • Confidentiality

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

Data specific for result type

  • Name of the periodical

    Acta Polytechnica

  • ISSN

    1210-2709

  • e-ISSN

  • Volume of the periodical

    52

  • Issue of the periodical within the volume

    3

  • Country of publishing house

    CZ - CZECH REPUBLIC

  • Number of pages

    4

  • Pages from-to

    97-100

  • UT code for WoS article

  • EID of the result in the Scopus database