کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
172924 | 458569 | 2012 | 9 صفحه PDF | دانلود رایگان |

Gas and particles hydrodynamic behaviors were investigated in a pilot-scale cold-mode riser and a bubbling fluidized bed gasifier by means of experiment and computational fluid dynamics (CFD).Six different experimental sets were conducted in the cold-rig dual fluidized bed (DFB) at different gas velocities in both the riser and the recycle chamber aeration. A two-dimensional (2D) multi-fluid Eulerian model incorporating the kinetic theory of granular flows was applied to identify unsteady-state behaviors of the fluidized bed.The CFD model predicts well the solid circulation rate in the cold-rig DFB for all the six experimental runs. A discrepancy between experiment and simulation is observed in the axial solid holdup along the riser. The simulation results demonstrate that the cold-bed simulation can be used to predict the solid circulation rate for the hot-bed operation of the DFB gasifier.
► Hydrodynamics of cold-rig dual CFB were investigated by means of experiment and CFD.
► Solid circulation rate was predicted by CFD and compared to the experimental one.
► CFD simulation results show reasonable agreement with experimental data.
► Cold-bed hydrodynamics are comparable to hydrodynamics in hot-bed mode.
Journal: Computers & Chemical Engineering - Volume 36, 10 January 2012, Pages 48–56