2017
DOI: 10.1016/j.ijheatmasstransfer.2016.10.117
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Three dimensional modeling of heat transfer and bed flow in a conical fluidized bed reactor

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Cited by 15 publications
(2 citation statements)
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“…Figure 8 shows the average heat transfer coe cients (h avg ) for the various fuel options and the range of excess air (EA), with only EA showing signi cant effects on the h avg . The h avg increases with increasing EA or increasing gas inlet velocity, indicating good agreement with the modeling study of Abdelmotalib and Im [34].…”
Section: Average Heat Transfer Coe Cient For Each Operating Condition...supporting
confidence: 82%
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“…Figure 8 shows the average heat transfer coe cients (h avg ) for the various fuel options and the range of excess air (EA), with only EA showing signi cant effects on the h avg . The h avg increases with increasing EA or increasing gas inlet velocity, indicating good agreement with the modeling study of Abdelmotalib and Im [34].…”
Section: Average Heat Transfer Coe Cient For Each Operating Condition...supporting
confidence: 82%
“…This increased the turbulence of the ow and the surface renewal frequency rate leading to a slightly higher level of heat transfer. The same behavioral trend was found in the conical FBC studied for gas-solid radial heat transfer by using twodimensional (2D) modeling of the air sand bed [34].…”
Section: Local Heat Transfer Coe Cient (H Local )supporting
confidence: 67%