|Title||Sub-grid drag models for horizontal cylinder arrays immersed in gas-particle multiphase flows|
|Publication Type||Journal Article|
|Year of Publication||2013|
|Authors||Sarkar A, Sun X, Sundaresan S|
|Journal||Chemical Engineering Science|
|Type of Article||Journal Article dcm|
|Keywords||Computational fluid dynamics (CFD), Cylinders, Filtered models, Fluidization, Multiphase flow, Multiscale|
Immersed cylindrical tube arrays often are used as heat exchangers in gas-particle fluidized beds. In multiphase computational fluid dynamics (CFD) simulations of large fluidized beds, explicit resolution of small cylinders is computationally infeasible. Instead, the cylinder array may be viewed as an effective porous medium in coarse-grid simulations. The cylinders’ influence on the suspension as a whole, manifested as an effective drag force, and on the relative motion between gas and particles, manifested as a correction to the gas-particle drag, must be modeled via suitable sub-grid constitutive relationships. In this work, highly-resolved unit-cell simulations of flow around an array of horizontal cylinders, arranged in a staggered configuration, are filtered to construct sub-grid, or ‘filtered’, drag models, which can be implemented in coarse-grid simulations. The force on the suspension exerted by the cylinders is composed of, as expected, a buoyancy contribution, and a kinetic component analogous to fluid drag on a single cylinder. Furthermore, the introduction of tubes also is found to enhance segregation at the scale of the cylinder size, which, in turn, leads to a reduction in the filtered gas-particle drag.