流态化
机械
压力降
传热
捆绑
敲击
联轴节(管道)
湍流
材料科学
离散元法
大涡模拟
流化床
流量(数学)
流化床燃烧
热力学
物理
复合材料
作者
Shuai Wang,Kun Luo,Chenshu Hu,Jianren Fan
出处
期刊:Springer proceedings in physics
日期:2016-12-02
卷期号:: 1023-1035
标识
DOI:10.1007/978-981-10-1926-5_107
摘要
Bubbling and turbulent fluidization are two typical fluidization regimes in fluidized bedsFluidized bed . Under the Eulerian-Lagrangian framework, the heat transferHeat transfer properties in a bubbling fluidized bedFluidized bed (BFB) and gas-solid behaviors in a three-dimensional (3-D) circulating fluidized bedFluidized bed (CFB) are investigated respectively by using Discrete Element Method-Large-eddy Simulation (DEM-LESDiscrete element method-large-eddy simulation ) coupling approach. The gas behavior is resolved at computational grid level and the solid behavior is handled at particle-scale level, moreover, inter-particle and inter-phase heat transferHeat transfer are involved. Results show that the tube bundles make the solid distribution more uniform. Staggered tube bundle BFB achieves higher heat transferHeat transfer performance. In the CFB, solid internal circulations are observed in the riser. Moreover, the inventories in six standpipes differ even though the geometry of the apparatus is symmetric. The solid back-mixing occurs mainly in the four corners of the riser. In each external circulating system, pressure drop forming between the inlet of riser and the surface of packed beds in standpipes becomes the driven force for solid circulations in the closed loop. In summary, all these crucial mechanisms shed light on the design, operation and scale-up of fluidized bedsfluidized bed in practical engineering fields.
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