Combustion of coal char particles under fluidized bed oxyfiring conditions (Contributo in atti di convegno)

Type
Label
  • Combustion of coal char particles under fluidized bed oxyfiring conditions (Contributo in atti di convegno) (literal)
Anno
  • 2009-01-01T00:00:00+01:00 (literal)
Alternative label
  • Scala F., Chirone R (2009)
    Combustion of coal char particles under fluidized bed oxyfiring conditions
    in Proc. of 20th Int. Conf. on Fluidized Bed Combustion, Xi'an, China
    (literal)
Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#autori
  • Scala F., Chirone R (literal)
Pagina inizio
  • 624 (literal)
Pagina fine
  • 629 (literal)
Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#affiliazioni
  • Istituto di ricerche sulla combustione - CNR (literal)
Titolo
  • Combustion of coal char particles under fluidized bed oxyfiring conditions (literal)
Abstract
  • In this work combustion of single coal char particles was studied at 850°C in a lab-scale fluidized bed under simulated oxyfiring conditions. The burning rate of the particles was followed as a function of time by continuously measuring the outlet CO and O2 concentrations. Some preliminary evaluations on the significance of homogeneous CO oxidation in the reactor and of carbon gasification by CO2 in the char were also carried out. Results showed that the carbon burning rate increases with oxygen concentration and char particle size. The particle temperature is approximately equal to the bed one up to an oxygen concentration of 2%, but it is considerably higher for larger oxygen concentrations. Both CO2 gasification of char and homogeneous CO oxidation are not negligible. The gasification reaction rate is slow and it is likely to be controlled by intrinsic kinetics. During purely gasification conditions the extent of carbon loss due to particle attrition by abrasion (estimated from the carbon mass balance) appears to be more important than under combustion conditions. (literal)
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