2015
DOI: 10.1016/j.cherd.2015.05.042
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Influence of contactor geometry and draft tube configuration on the cycle time distribution in sawdust conical spouted beds

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Cited by 26 publications
(21 citation statements)
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“…18,19,25,26 A change in ΔP b is also observed with the variation of particle size. 23 Use of porous DT (with peripheral holes) further adds to the insight, accounting for the probable losses of energy through the various porous channels. 20,23,27 Computational fluid dynamics (CFD) simulation findings are seen to effectively describe the solid circulation and particle velocity profiles along with the distribution of gas phase through various regions of DT-SB, highlighting the solid−fluid interactions at various flow conditions.…”
Section: Introductionmentioning
confidence: 99%
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“…18,19,25,26 A change in ΔP b is also observed with the variation of particle size. 23 Use of porous DT (with peripheral holes) further adds to the insight, accounting for the probable losses of energy through the various porous channels. 20,23,27 Computational fluid dynamics (CFD) simulation findings are seen to effectively describe the solid circulation and particle velocity profiles along with the distribution of gas phase through various regions of DT-SB, highlighting the solid−fluid interactions at various flow conditions.…”
Section: Introductionmentioning
confidence: 99%
“…23 Use of porous DT (with peripheral holes) further adds to the insight, accounting for the probable losses of energy through the various porous channels. 20,23,27 Computational fluid dynamics (CFD) simulation findings are seen to effectively describe the solid circulation and particle velocity profiles along with the distribution of gas phase through various regions of DT-SB, highlighting the solid−fluid interactions at various flow conditions. 22−24,28−34 H e is reported to be the key influencing design parameter on ΔP b for a nonporous DT-assisted SB followed by the height of static bed (H 0 ) and cone angle (γ c ).…”
Section: Introductionmentioning
confidence: 99%
“…It is well reported in the previous literature that the porous or open-sided DT ease the higher fraction of gas flow into the annular region. As a matter of fact, the gas pressure drop increases across the DT with the increase in porosity or the open area of the DT. At the same time, U ms is expected to increase when the DT is switched from nonporous to the porous and open-sided one.…”
Section: Introductionmentioning
confidence: 84%
“…Measurement of gas phase residence time (τ g ) has also been reported in the literature for the case of DTSB. τ g is seen to have a higher value for higher H e , and it is reduced obviously with an increase in U . Average normalized pressure ( P A /Δ P b ) in the annular and the spout has been experimentally found in the case of a DTSB and compared with suitable simulation results. P A /Δ P b is seen to vary nearly linearly with H 0 both in the case of the spout and the annular region .…”
Section: Introductionmentioning
confidence: 99%
“…The mass flow rate in the spout, together with the average particle cycle time, have been adopted as standard parameters for assessing the circulation of solids in spouted beds 13, 14. The particle circulation in the spouted beds is directly related to heat and mass transfer rates 15, 16, so it is a key factor to consider in their modeling and design 17. Moreover, to make effective use of conical spouted beds in industrial facilities, an improved fundamental understanding of their hydrodynamics is required 18.…”
Section: Introductionmentioning
confidence: 99%