CFD simulation of fluidization quality in the three-dimensional fluidized bed  被引量:5

CFD simulation of fluidization quality in the three-dimensional fluidized bed

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作  者:Kai Zhang Stefano Brandani Jicheng. Bi Jianchun Jiang 

机构地区:[1]State Key Lab of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China [2]IMP-SEE, University of Edinburgh, The King's Buildings, Edinburgh EH9 3JL, UK [3]State Key Lab of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan 030001, China [4]Institute of Chemical Industry of Forest Products, Chinese Academy of Forestry, Nanjing 210042, China

出  处:《Progress in Natural Science:Materials International》2008年第6期729-733,共5页自然科学进展·国际材料(英文版)

基  金:National Key Technology R&D Program of China (2006BAD07A0301);National Natural Science Foundation of China (20476057 and 20490200);Key Laboratory of Coal Conversion (04-202)is gratefully acknowledged.

摘  要:Multiphase computational fluid dynamics (CFD) has become an alternative method to experimental investigation for predicting the fluid dynamics in gas-solid fluidized beds. The model of Brandani and Zhang, which contains additional terms in both the gas- and solidphase momentum equations, is employed to explore homogeneous fluidization of Geldart type A particles and bubbling fluidization of Geldart type B particles in three-dimensional gas-fluidized beds. In this model, only a correlation for drag force is necessary to close the governing equations. Two kinds of solids, i.e., fine alumina powder (dp= 60 μm and pp = 1500 kg/m^3) and sand (dp = 610 μm and pp = 2500 kg/m^3), are numerically simulated in a rectangular duct of 0.2 m (long) × 0.2 m (wide)× 0.5 m (high) size. The results show good agreement with the classic theory of Geldart.Multiphase computational fluid dynamics(CFD)has become an alternative method to experimental investigation for predicting the fluid dynamics in gas-solid fluidized beds.The model of Brandani and Zhang,which contains additional terms in both the gas-and solid-phase momentum equations,is employed to explore homogeneous fluidization of Geldart type A particles and bubbling fluidization of Geldart type B particles in three-dimensional gas-fluidized beds.In this model,only a correlation for drag force is necessary to close the governing equations.Two kinds of solids,i.e.,fine alumina powder(dp=60 lm and qp=1500 kg/m3)and sand(dp=610 lm and qp=2500 kg/m3),are numerically simulated in a rectangular duct of 0.2 m(long)0.2 m(wide)0.5 m(high)size.The results show good agreement with the classic theory of Geldart.

关 键 词:Three-dimensional gas-solid fluidized bed Fluidization quality CFD simulation 

分 类 号:O645[理学—物理化学]

 

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