Fluidized bed combustion of single coal char particles at high CO2 concentration (Articolo in rivista)

Type

• Articolo in rivista (Classe)
• Prodotto della ricerca (Classe)

Label

• Fluidized bed combustion of single coal char particles at high CO2 concentration (Articolo in rivista) (literal)

Anno

• 2010-01-01T00:00:00+01:00 (literal)

Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#doi

• 10.1016/j.cej.2010.09.059 (literal)

Alternative label

• Scala, F; Chirone, R (2010)
  Fluidized bed combustion of single coal char particles at high CO2 concentration
  in Chemical engineering journal ( Print)
  (literal)

Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#autori

• Scala, F; Chirone, R (literal)

Pagina inizio

• 902 (literal)

Pagina fine

• 906 (literal)

Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#numeroVolume

• 165 (literal)

Rivista

• Chemical engineering journal (Rivista)

Note

• ISI Web of Science (WOS) (literal)

Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#affiliazioni

• Istituto di Ricerca sulla Combustione, IRC-CNR (literal)

Titolo

• Fluidized bed combustion of single coal char particles at high CO2 concentration (literal)

Abstract

• Combustion of single coal char particles was studied at 850 degrees C in a lab-scale fluidized bed at high CO(2) concentration, typical of oxyfiring conditions. The burning rate of the particles was followed as a function of time by continuously measuring the outlet CO and O(2) concentrations. Some preliminary evaluations on the significance of homogeneous CO oxidation in the reactor and of carbon gasification by CO(2) 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 that of the bed up to an oxygen concentration of 2%, but it is considerably higher for larger oxygen concentrations. Both CO(2) 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 much more important than under combustion conditions. (literal)

Prodotto di

• Istituto di ricerche sulla combustione (IRC) (Istituto)
• Sviluppo di tecnologie di gasificazione con riguardo anche ai problemi di sicurezza e impatto ambientale (ET.P01.003.002) (Modulo)
• Studio dei processi e tecnologie di combustione a basso impatto ambientale (ET.P01.003.001) (Modulo)

Autore CNR

• FABRIZIO SCALA (Persona)
• RICCARDO CHIRONE (Unità di personale interno)

Insieme di parole chiave

• Keywords of "Fluidized bed combustion of single coal char particles at high CO2 concentration" (Insieme di parole chiave)

Incoming links:

Autore CNR di

• FABRIZIO SCALA (Persona)
• RICCARDO CHIRONE (Unità di personale interno)

Prodotto

• Istituto di ricerche sulla combustione (IRC) (Istituto)
• Studio dei processi e tecnologie di combustione a basso impatto ambientale (ET.P01.003.001) (Modulo)
• Sviluppo di tecnologie di gasificazione con riguardo anche ai problemi di sicurezza e impatto ambientale (ET.P01.003.002) (Modulo)

Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#rivistaDi

• Chemical engineering journal (Rivista)

Insieme di parole chiave di

• Keywords of "Fluidized bed combustion of single coal char particles at high CO2 concentration" (Insieme di parole chiave)