2010
DOI: 10.1021/ef900806z
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Fragmentation Effect on Batches of Pine Wood Char Burning in a Fluidized Bed

Abstract: Batches of Pinus pinea char particles with average diameters of 2.2, 2.8, and 3.6 mm were burned in a bubbling fluidized bed at temperatures of 600, 700, and 750 °C, with a velocities ratio U/U mf = 9. The results show that only primary fragmentation occurs with an average fragmentation ratio of 1.5. No effect of the secondary fragmentation phenomena is observed. The increase in the number of particles in the bed because of fragmentation is accounted over the burning time, and its effect is evaluated on the de… Show more

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Cited by 10 publications
(11 citation statements)
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“…For the sake of simplicity, results for only two of the tested sizes, 1.8 and 3.6 mm, are shown, but for all tested sizes the trends are equal. The shape of the CO 2 concentration curves also shows that there is primary fragmentation and absence of secondary fragmentation, phenomena which are discussed elsewhere (Rangel and Pinho, 2010).…”
Section: Evolution Of Volumic Co2 Concentration In the Combustion Gasesmentioning
confidence: 63%
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“…For the sake of simplicity, results for only two of the tested sizes, 1.8 and 3.6 mm, are shown, but for all tested sizes the trends are equal. The shape of the CO 2 concentration curves also shows that there is primary fragmentation and absence of secondary fragmentation, phenomena which are discussed elsewhere (Rangel and Pinho, 2010).…”
Section: Evolution Of Volumic Co2 Concentration In the Combustion Gasesmentioning
confidence: 63%
“…Elutriation is out of the question as an explanation for the low carbon recovery rate, as the fragmentation phenomenon occurring with this type of char does not lead to elutriable particle sizes (Rangel and Pinho, 2010). Table 1 also shows densities and proximate analysis for the studied particles.…”
Section: Carbon Recovery Ratio and Properties Of The Fuel Particlesmentioning
confidence: 99%
“…The real explanation is not a lower combustion resistance but an increase of the overall surface area of reactant particles. Because this increase was not taken into account, its influence was translated into a decrease of the overall combustion resistance. , Therefore, the next step is to take into account the influence of the fragmentation process on the overall surface area of particles available for the reaction and re-evaluate the experimental data, in the case of fragile particles, by comparing the corresponding Sh and k c to those obtained with the stronger particles.…”
Section: Resultsmentioning
confidence: 99%
“…The secondary fragmentation is the result of the internal structure of the particles. Thus, this type of fragmentation is mainly caused by the physical shocks that occur between coal particles during combustion. , …”
Section: Introductionmentioning
confidence: 99%
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