Gas solid contacting measurements in a turbulent fluidized bed by oxidation of carbon monoxide

The conversion rate of the mass transfer controlled oxidation of CO over a Pt/?-alumina catalyst (d = 65 ?m) has been studied in a fluidized bed (internal diameter = 0.05 m) p operated close to and in the turbulent fluid bed regime. The objectives were to investigate the gas-solids contacting effici...

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Veröffentlicht in:	Thermal science 2019, Vol.23 (Suppl. 5), p.1413-1423
Hauptverfasser:	Venderbosch, Robbie, Prins, Wolter, van, Swaaij
Format:	Artikel
Sprache:	eng
Schlagworte:	Agglomerates Aluminum oxide Computational fluid dynamics Conversion Fluid flow Fluidized beds Mass transfer Oxidation Transitional aluminas Turbulent flow
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