流态化
压力降
流化床
机械
流量(数学)
材料科学
CFD-DEM公司
粒子(生态学)
计算流体力学
粒径
热力学
地质学
工程类
物理
化学工程
海洋学
作者
Li Ning Han,Lu Min Wang
出处
期刊:Advanced Materials Research
日期:2014-01-01
卷期号:881-883: 1809-1813
标识
DOI:10.4028/www.scientific.net/amr.881-883.1809
摘要
The Euler-Euler two-fluid model incorporating the kinetic theory of granular flow was applied to simulate the gas-solid flow in fluidized beds. The pressure drop, particle distribution and motion characteristics were studied in this paper. In order to investigate the effect of structure of the fluidized bed on flow characteristics, fluidized beds with different diameters and structures were applied. User defined functions (UDF) were applied to study the flow characteristics when the particle size and mass changed over time. The results showed that with the increase of particle size, higher minimum fluidization velocity was required, but lower pressure drop was obtained. For a certain fluidizing medium, the bed critical fluidization velocity depended only on the size and nature of the particles. The structure of a fluidized bed had an influence on the particle distribution and motion characteristics.
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