http://www.cnr.it/ontology/cnr/individuo/prodotto/ID42599
On the relevance of axial and transversal fuel segregation during the FB combustion of a biomass (Articolo in rivista)
- Type
- Label
- On the relevance of axial and transversal fuel segregation during the FB combustion of a biomass (Articolo in rivista) (literal)
- Anno
- 2004-01-01T00:00:00+01:00 (literal)
- Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#doi
- 10.1021/ef034084j (literal)
- Alternative label
Chirone, Riccardo; Miccio, Francesco; Scala, Fabrizio (2004)
On the relevance of axial and transversal fuel segregation during the FB combustion of a biomass
in Energy & fuels (Print)
(literal)
- Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#autori
- Chirone, Riccardo; Miccio, Francesco; Scala, Fabrizio (literal)
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- Pagina fine
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- Rivista
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- Note
- ISI Web of Science (WOS) (literal)
- Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#affiliazioni
- ISTITUTO DI RICERCHE SULLA COMBUSTIONE (literal)
- Titolo
- On the relevance of axial and transversal fuel segregation during the FB combustion of a biomass (literal)
- Abstract
- The fluidized bed combustion of a typical Mediterranean biomass (pine-seed shells) was
investigated in a pilot-scale bubbling FB combustor (200 kWth) at different operating conditions.
Both over- and under-bed fuel feeding options were considered. The focus of the experiments
was to study the extent of volatile matter mixing/segregation in the bed and the subsequent
postcombustion in the splashing zone and freeboard. To this end, temperature profiles along the
combustor axis as well as transversal gas concentration profiles above the bed surface were
measured. Experiments highlighted that complete conversion of the fuel within the combustor
was obtained, even if a significant volatiles postcombustion above the bed occurred. This results
in an appreciable overheating of the freeboard. Both the fuel feeding option and the excess air
affect the extent of volatiles postcombustion. Gas concentration profiles were not uniform along
the combustor diameter because of the single-point fuel feeding and the incomplete fuel mixing
in the bed. The measured carbon-containing gaseous species profiles along the bed diameter were
used to estimate the fuel lateral dispersion coefficient in the fluidized bed, by means of a simplified
dispersion/pyrolysis model. Comparison of experimental profiles with model results at over- and
under-bed feeding conditions allowed us to evaluate both the fuel lateral dispersion coefficient
inside the bed and on the bed surface, which were determined to be of the order of 0.01 m2/s and
0.1 m2/s, respectively. (literal)
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