首页> 外文会议>ASME international mechanical engineering congress and exposition;IMECE2011 >DETERMINATION OF MINIMUM FLUIDIZATION VELOCITY FOR GAS-SOLID BEDS BY EXPERIMENTAL DATA AND NUMERICAL SIMULATIONS
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DETERMINATION OF MINIMUM FLUIDIZATION VELOCITY FOR GAS-SOLID BEDS BY EXPERIMENTAL DATA AND NUMERICAL SIMULATIONS

机译:用实验数据和数值模拟确定气固床的最小流化速度

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The purpose of this work is to predict the minimum flu-idization velocity U_mf in a gas-solid fluidized bed. The study was carried out with an experimental apparatus for sand particles with diameters between 310μm and 590pm, and density of 2,590kg/m~3. The experimental results were compared with numerical simulations developed in MFIX (Multiphase Flow with Interphase eXchange) open source code [1], for three different sizes of particles: 310mum, 450μm and 590μm. A homogeneous mixture with the three kinds of particles was also studied. The influence of the particle diameter was presented and discussed. The Ergun equation was also used to describe the minimum fluidization velocity. The experimental data presented a good agreement with Ergun equation and numerical simulations.
机译:本作作品的目的是预测气固流化床中的最小流感型速度U_mf。该研究是用直径在310μm和590分的砂颗粒的实验装置进行,密度为2,590kg / m〜3。将实验结果与MFIX中开发的数值模拟进行比较(具有相互交换的多相流)开源代码[1],用于三种不同尺寸的粒子:310mum,450μm和590μm。还研究了具有三种颗粒的均匀混合物。提出和讨论了粒径的影响。 Ergun方程还用于描述最小的流化速度。实验数据与Ergun方程和数值模拟吻合了一致。

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