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CFD Simulations of Complex Fluid Flow in Gas-Solid Fluidized Bed Using Modified k-ε Turbulence Models

机译:使用改性K-ε湍流模型CFD模拟气体固体流化床中的复杂流体流动

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This work studies the effect of kinetic Prandtl value in the k-ε turbulence model transport equation on the characteristics of fluidized bed fluid flow. The research was conducted using CFD simulation method. Three kinetic Prandtl values were chosen, namely 0.8; 0.9 and 1.1; plus 1 from the default value of the turbulent model. The parameters observed were the difference in pressure in the bed, and several turbulence parameters, i.e. the rate of dissipation, the effective viscosity of the gas and the particles. The turbulent model with k-Prandtl of 0.9 gives the most accurate results at the superficial velocity range of 0.40 m/s - 0.70 m/s, while k-Prandtl of 1.1 gives most accurate results at the superficial velocity range of 0.80 m/s - 0.90 m/s. It is found that the decrease in the k-Prandtl value causes the decrease in the dissipation rate; same phenomena with effective viscosity of gas. Meanwhile, there is no significant change in the particle's effective viscosity with the change of k-Prandtl value.
机译:这项工作研究了动力学PRANDTL值在k-ε湍流模型传输方程中的影响流化床流体流动特性。使用CFD仿真方法进行了研究。选择三个动力学普朗特值,即0.8; 0.9和1.1;加1来自湍流模型的默认值。观察到的参数是床中的压力差异,以及几个湍流参数,即耗散速率,气体的有效粘度和颗粒。具有0.9的k-prandtl的湍流模型在0.40 m / s-0.70 m / s的静态速度范围内给出最精确的结果,而K-prandtl为1.1给出最精确的结果,在浅刻速度范围为0.80 m / s - 0.90 m / s。发现k-prandtl值的减少导致耗散率降低;相同的现象,具有有效粘度的气体。同时,随着k-prandtl值的变化,颗粒的有效粘度没有显着变化。

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