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流体床内细长颗粒的浓度分布(英文) 被引量:1

Number Concentration of Cylindrical Particles in a Fluidized Bed
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摘要 In this study, a three-dimensional model based on RANS, slender-body theory and Newton-Euler dynamics is established to study the number concentration, one of the most important fluidization characteristics of cylindrical particles. Also, the effects of interaction between cylindrical particles are taken into account by introducing the rigid collision dynamics. To validate the model, the fluidization experiments of cylindrical particles in a cold-state fluidized bed are carried out. The number concentration characteristics of cylindrical particles are obtained from computational fluid dynamics (CFD) simulation. It is found that cylindrical particles arriving at the exit of the riser the earliest come from the near-wall regions, the horizontal transfer of so many cylindrical particles from the radial centre regions to the near-wall regions is evident. Meanwhile, there is no distinct relationship between the number concentration and inlet wind velocity. In this study, a three-dimensional model based on RANS, slender-body theory and Newton-Euler dy- namics is established to study the number concentration, one of the most important fluidization characteristics of cylindrical particles. Also, the effects of interaction between cylindrical particles are taken into account by intro- ducing the rigid collision dynamics. To validate the model, the fluidization experiments of cylindrical particles in a cold-state fluidized bed are carried out. The number concentration characteristics of cylindrical particles are ob- tained from computational fluid dynamics (CFD) simulation. It is found that cylindrical particles arriving at the exit of the riser the earliest come from the near-wall regions, the horizontal transfer of so many cylindrical particles from the radial centre regions to the near-wall regions is evident. Meanwhile, there is no distinct relationship be- tween the number concentration and inlet wind velocity.
出处 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2013年第1期94-103,共10页 中国化学工程学报(英文版)
基金 Supported by the Natural Science Fund for Colleges and Universities in Jiangsu Province(2011112TSJ0149) Jiangsu Key Laboratory of Process Enhancement & New Energy Equipment Technology at Nanjing University of Technology,China
关键词 柱形颗粒 数浓度 圆柱状 流化床 计算流体动力学 碰撞动力学 三维模型 细长体理论 number concentration, cylindrical particles, a three-dimensional model, interaction between cylindrical particles, numerical simulation
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