Experimental Investigation of Radial Gas Dispersion Coefficients in a Fluidized Bed

Kód výsledku v 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>
Výsledek na webu
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DOI - Digital Object Identifier
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Jazyk výsledku
angličtina
Název v původním jazyce
Experimental Investigation of Radial Gas Dispersion Coefficients in a Fluidized Bed
Popis výsledku v původním jazyce
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
Název v anglickém jazyce
Experimental Investigation of Radial Gas Dispersion Coefficients in a Fluidized Bed
Popis výsledku anglicky
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

Druh
J<sub>x</sub> - Nezařazeno - Článek v odborném periodiku (Jimp, Jsc a Jost)
CEP obor
JE - Nejaderná energetika, spotřeba a užití energie
OECD FORD obor
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Rok uplatnění
2012
Kód důvěrnosti údajů
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

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