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首页> 外文期刊>International Journal for Numerical Methods in Fluids >Comparative study of Euler/Euler and Euler/Lagrange approaches simulating evaporation in a turbulent gas-liquid flow
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Comparative study of Euler/Euler and Euler/Lagrange approaches simulating evaporation in a turbulent gas-liquid flow

机译:欧拉/欧拉和欧拉/拉格朗日方法模拟湍流气液流中蒸发的比较研究

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摘要

This study deals with the Reynolds-averaged Navier-Stokes simulation of evaporation in a turbulent gas- liquid flow in a three-dimensional duct, focussing on the results obtained by a four-equation turbulence model within the framework of the Euler/Euler approach for multiphase flow calculations: in addition to the two-equation k-ε model describing the turbulence of the continuous (C) phase, the computational model employs transport equations for the turbulence kinetic energy of the disperse (D) phase and for the velocity covariance q =〈{(u{sub}i){sup}D }{sup}D{(u{sub}I){sup}C }{sup}C〉{sup}D. In the present study, the evaporation model according to Abramzon and Sirignano (Int. J. Heat Mass Transfer 1989; 32:1605-1618) has been extended by introducing an additional transport equation for a newly defined quantity a{top}-, defined as the phase-interface surface fraction. This allows the change in the drop diameter to be quantified in terms of a probability density function. The source term in the equation describing the dynamics of the volumetric fraction of the dispersed phase α{sup}D is related to the evaporation time scale τ{sub}Γ. The performance of the new model is evaluated by performing a comparative analysis of the results obtained by simulating a polydispersed spray in a three-dimensional duct configuration with the results of the Euler/Lagrange calculations performed in parallel. Prior to these calculations, some selected (solid) particle-laden flow configurations were computationally examined with respect to the validation of the background, four-equation, eddy-viscosity-based turbulence model.
机译:这项研究涉及三维管道中湍流气液流中蒸发的雷诺兹平均Navier-Stokes模拟,重点是在Euler / Euler方法框架内通过四方程湍流模型获得的结果多相流计算:除了描述连续(C)相湍流的两方程式k-ε模型外,该计算模型还采用了运移方程来求解分散(D)相的湍流动能和速度协方差q = 〈{{(u {sub} i){sup} D} {sup} D {{u {sub} I} {sup} C} {sup} C〉 {sup} D。在本研究中,根据Abramzon和Sirignano(Int。J. Heat Mass Transfer 1989; 32:1605-1618)的蒸发模型已经通过引入新定义的量a {top}-的附加输运方程进行了扩展作为相界面表面分数。这使得可以根据概率密度函数来量化液滴直径的变化。方程中描述分散相α{sup} D的体积分数动态的方程中的源项与蒸发时间标度τ{sub}Γ有关。通过对在三维风管配置中模拟多分散喷雾与并行执行的Euler / Lagrange计算结果的结果进行比较分析,可以评估新模型的性能。在进行这些计算之前,相对于本底,四方程,基于涡流粘度的湍流模型的验证,对一些选定的(固体)载有颗粒的流动构型进行了计算检查。

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