2008
DOI: 10.1016/j.ces.2008.04.038
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DEM–LES study of 3-D bubbling fluidized bed with immersed tubes

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Cited by 74 publications
(34 citation statements)
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“…As a particle may cross the boundaries of several computational grids, the segmentation of a particle is usually utilized to obtain the accurate volume fraction of a specific computational grid in numerical simulations (Gui et al, 2008;Yang et al, 2014aYang et al, , 2014b. Every particle is divided into 48 elements and the computational cell that a specific particle element locates in is detected based on its position.…”
Section: Governing Equations For Gas Motionmentioning
confidence: 99%
“…As a particle may cross the boundaries of several computational grids, the segmentation of a particle is usually utilized to obtain the accurate volume fraction of a specific computational grid in numerical simulations (Gui et al, 2008;Yang et al, 2014aYang et al, , 2014b. Every particle is divided into 48 elements and the computational cell that a specific particle element locates in is detected based on its position.…”
Section: Governing Equations For Gas Motionmentioning
confidence: 99%
“…The DEM-LES coupled approach has been validated in our previous study (Gui et al, 2008) and applied successfully for simulation of fluidized beds ).…”
Section: 29mentioning
confidence: 99%
“…the results obtained from a real three-dimensional particle system would be more informative and useful. However, it is so hard to carry out a simulation of a 3-D fluidized bed that any attempt on this issue is always intensively limited to reduced scales (Gui et al, 2008;Tsuji et al, 2008). …”
Section: The Effect Of the Particle Concentrations On The Interfacementioning
confidence: 99%
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“…Different approaches have been used to treat the stationary boundary of the tube in CFD calculation either using staircase approximation on a Cartesian grid [20,21] or accurately representing the boundary shape using body-fitted unstructured mesh [22,23]. Considerable efforts have been devoted to various aspects of the fluidized bed, including heat transfer [21,24,25], bubble hydrodynamics [20,26] and erosion of the tube surface [27]. However, the capability of CFD-DEM methods to tackle FSI problems in particle-fluid flow is lacking, especially when the fluid field is described by a continuous mesh-based method, such as Finite Volume Method (FVM) or Finite Difference Method (FDM).…”
Section: Introductionmentioning
confidence: 99%