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A Lattice Boltzmann model for multi-component vapor-liquid two phase flow

机译:多组分气液两相流的格子Boltzmann模型

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摘要

In traditional multi-phase multi-component Lattice Boltzmann (LB) models, the phase properties especially the vapor-liquid equilibrium calculations failed to model the actual flow realistically. A new multi-component vapor-liquid two phase LB model that involves a four-parameter (critical temperature, critical pressure, acentric factor and volume shift factor) equation of state (EOS) is proposed. The new model employs a four-parameter EOS to calculate the force on each lattice and then to determine the force between different fluid phases accurately. An accurate difference method is proposed to integrate the interaction force into the evolution functions of each component. Moreover, the Lorentz-Bray-Clark viscosity model is implemented to calculate the viscosity of lattice fluid according to the component density. The new model is validated and applied to forecast the phase behavior of methane, ethane, and propane mixture at multiple temperatures and pressures. The simulation results show a good agreement with experimental data and theoretical predictions.
机译:在传统的多相多组分格子Boltzmann(LB)模型中,相特性(尤其是气液平衡计算)无法真实地模拟实际流量。提出了一种新的多组分气液两相LB模型,该模型涉及一个四参数(临界温度,临界压力,偏心因数和体积偏移因数)状态方程(EOS)。新模型采用四参数EOS计算每个晶格上的力,然后精确确定不同流体相之间的力。提出了一种精确的差分方法,将相互作用力整合到每个组件的演化函数中。此外,采用Lorentz-Bray-Clark粘度模型来根据组分密度计算晶格流体的粘度。新模型经过验证,可用于预测多种温度和压力下甲烷,乙烷和丙烷混合物的相态。仿真结果与实验数据和理论预测吻合良好。

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