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3D CFD Modeling and Experimental Validation for Slurry Flow Through Pipe Bend

机译:用管弯对浆料流动的CFD建模与实验验证

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Bends are integral part of any slurry pipeline system and are prone to excessive wear. Therefore, a detailed knowledge of the flow characteristics in the bends will enable us to identify the causes of excessive wear which in turn may help in developing remedial steps to control the excessive wear. In the present study, experimental data are collected in a 90 degree horizontal pipe bend having bend radius of 148 mm situated in a pilot plant test loop with pipe diameter of 53 mm. The experiments are performed at volumetric concentration of 16.28% of silica sand having mean particle diameter of 448.5 micron. The flow velocity was varied from 1.78 to 3.56 m/s. Separation chambers are provided at each pressure tap for interface separation of slurry and manometric fluid, water being the intermediate fluid. For better accuracy, pressure drop along the pipeline is measured by an inclined manometer. Electromagnetic flow meter is used for the measurement of slurry discharge. It is observed that pressure drop along the pipe bend increases with flow velocity. The experimental data collected in the present study have been compared with the three-dimensional computational fluid dynamics (CFD) modeling, using Eulerian two-phase model and commercial CFD package FLUENT 6.2. Eulerian model expands the definition of continuum assumption to the dispersed phase and treats both continuous and dispersed phases separately as two phases. Both phases are linked using the drag force in the momentum equation. The standard k-epsilon model is used to treat turbulence phenomena in both the phases. The granular theory for the liquid-solid flow of the Eulerian model is introduced. Gambit software is used for the development of mesh. It is observed that CFD modeling gives fairly accurate results for almost all the pressure drop data considered in the present study. CFD modeling results for concentration and velocity profiles for collected experimental data have also been presented.
机译:弯曲是任何浆料管道系统的组成部分,易于过度磨损。因此,详细了解弯曲中的流动特性的知识将使我们能够识别过量磨损的原因,这反过来可能有助于开发控制过度磨损的补救措施。在本研究中,在90度水平管弯曲中收集实验数据,其弯曲半径为148mm,位于导频工厂测试回路,管直径为53mm。实验以16.28%的二氧化硅砂体积浓度进行,平均粒径为448.5微米。流速从1.78变化到3.56米/秒。在每个压力挖掘机处提供分离室,用于界面分离浆料和压液,水是中间体流体。为了更好的准确性,沿着管道的压降是通过倾斜的压力计测量的。电磁流量计用于测量浆料放电。观察到沿管弯的压降随着流速而增加。使用欧拉两相模型和商业CFD包流程6.2将本研究中收集的实验数据与三维计算流体动力学(CFD)建模进行了比较。 Eulerian模型扩展了连续局对分散相的定义,并将连续和分散相单独处理为两相。两个阶段都是使用动量方程中的拖曳力连接的。标准K-EPSILON模型用于治疗两个阶段的湍流现象。介绍了欧拉模型液体固体流动的粒状理论。 Gambit软件用于网格的开发。观察到,CFD建模对于本研究中考虑的几乎所有压力下降数据给出了相当准确的结果。还提出了用于收集的实验数据的浓度和速度谱的CFD建模结果。

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