Air-based coal gasification in a two-chamber gas reactor with circulating fluidized bed

During the bed gasification of solid fuels, the process temperature in the reaction zone is not high enough for reaching the maximum rate of the chemical efficiency factor of the gasification process. In order to increase the chemical efficiency factor, it is necessary to supply extra heat to the re...

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Veröffentlicht in:	Thermal engineering 2017, Vol.64 (1), p.46-52
Hauptverfasser:	Dubinin, A. M., Tuponogov, V. G., Kagramanov, Y. A.
Format:	Artikel
Sprache:	eng
Schlagworte:	Auxiliary Equipment of Boilers Beds (process engineering) Bubbling Burner Arrangements Carbon monoxide Chemical reduction Circulation Coal gasification Combustion chambers Cone crushers Engineering Engineering Thermodynamics Fluidized beds Fuel combustion Fuel mixtures Gas composition Heat and Mass Transfer Heat transfer Kinetic equations Power Plant Fuel Simulation models Solid fuels Steam Boilers Thermal simulation
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