Title of article :
CFD modeling of gas–solid flow in an internally circulating fluidized bed
Author/Authors :
Feng، نويسنده , , Yuqing and Swenser-Smith، نويسنده , , Tim and Witt، نويسنده , , Peter J. and Doblin، نويسنده , , Christian and Lim، نويسنده , , Seng and Schwarz، نويسنده , , M. Phil، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2012
Abstract :
This paper presents a numerical study of gas and solid flow in an internally circulating fluidized bed (ICFB). The gas and solid dynamics has been calculated using the commercial computational fluid dynamics (CFD) software package ANSYS/Fluent and an Eulerian–Eulerian model (EEM) with kinetic theory of granular flow used to calculate solid stresses. A two dimensional geometry was used to represent key parts of a laboratory ICFB. Simulations were conducted to assess the effect of changes to four designs or operating parameters: gas distributor plate angles, presence of a heat exchange tube bundle, superficial fluidizing velocities and initial solid packing heights. The mechanism governing the solid recirculation in an ICFB has been explained based on gas and solid dynamics obtained from the simulations and the effect of the four designs or operating parameters is quantified in terms of solid recirculation rate (SRR). Both of the investigated operating parameters, superficial fluidizing velocities and initial solid packing height, strongly affect solid circulation rate. For the two investigated design parameters, the presence of a tube bundle reduced the solid recirculation rate by 20%, while an inclination angle of 1.5° does not affect the solid recirculation rate significantly.
Keywords :
Gas solid flow , Solid recirculation rate , computational fluid dynamics (CFD) , Eulerian–Eulerian model , Internally circulating fluidized bed (ICFB)
Journal title :
Powder Technology
Journal title :
Powder Technology