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Thermo-mechanical modeling of turbulent heat transfer in gas-solid flows including particle collisions

机译:气固两相中湍流传热的热力学模型,包括粒子碰撞

摘要

A thermo-mechanical turbulence model is developed and used for predicting heat transfer in a gas-solid flow through a vertical pipe with constant wall heat flux. The new four-way interaction model makes use of the thermal kθ-τθ equations, in addition to the hydrodynamic k-τ transport, and accounts for the particle-particle and particle-wall collisions through a Eulerian/Lagrangian formulation. The simulation results indicate that the level of thermal turbulence intensity and the heat transfer are strongly affected by the particle collisions. Inter-particle collisions attenuate the thermal turbulence intensity near the wall but somewhat amplify the temperature fluctuations in the pipe core region. The hydrodynamic-to-thermal times-scale ratio and the turbulent Prandtl number in the region near the wall increase due to the inter-particle collisions. The results also show that the use of a constant or the single-phase gas turbulent Prandtl number produces error in the thermal eddy diffusivity and thermal turbulent intensity fields. Simulation results also indicate that the inter-particle contact heat conduction during collision has no significant effect in the range of Reynolds number and particle diameter studied. © 2002 Elsevier Science Inc. All rights reserved.
机译:建立了热力机械湍流模型,并将其用于预测具有恒定壁热通量的垂直管道中气固流中的热传递。新的四向相互作用模型除了利用流体动力学k-τ传输之外,还利用了热kθ-τθ方程,并通过欧拉/拉格朗日公式解释了粒子与粒子和粒子与壁的碰撞。仿真结果表明,粒子碰撞对热湍流强度和传热的影响很大。粒子间碰撞会减弱壁附近的热湍流强度,但会在一定程度上放大管芯区域的温度波动。由于粒子间的碰撞,壁附近区域的水动力-热时间标度比和湍流的普朗特数增加。结果还表明,使用恒定或单相气体湍流Prandtl数会在热涡流扩散率和热湍流强度场中产生误差。模拟结果还表明,碰撞过程中的颗粒间接触热传导在研究的雷诺数和粒径范围内没有显着影响。 ©2002 Elsevier Science Inc.保留所有权利。

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