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Direct numerical simulations of film boiling heat transfer by a phase-change lattice Boltzmann method

机译:相变晶格玻尔兹曼法的薄膜沸腾传热的直接数值模拟

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Numerical simulations of film boiling heat transfer on a horizontal surface are conducted in this paper using a modified pseudo-potential liquid-vapor phase change lattice Boltzmann model. A conjugate heat transfer problem, including heat conduction in the heater and its thermal responses during the film boiling process, is investigated. Unlike previous numerical studies which needed to initialize the shape of the liquid-vapor interface wave at the beginning of the computation, the computation domain for fluid region is occupied initially by saturated liquid in this paper. Taylor instability at the liquid-vapor interface is triggered by small temperature perturbations imposed at the bottom of the heater during a short initial period. Consequently, this paper represents a more direct and complete numerical simulation for film boiling heat transfer on a horizontal heater. The simulated time- and space-averaged Nusselt number is found in good agreement with a previous correlation equation. Temporal and spatial variations of the vapor film thickness are also investigated numerically and compared with existing correlation equations. It is demonstrated that the temperature at the top surface of the heart changes with position and time during the film boiling process. Although the transient film boiling patterns may depend on temperature perturbations imposed on he bottom of the heater during an initial period, the time- and space-averaged film boiling heat flux is independent of initial temperature perturbations.
机译:本文利用改进的伪势液相-汽相变格子Boltzmann模型对膜在水平面上的沸腾传热进行了数值模拟。研究了共轭传热问题,包括加热器在膜沸腾过程中的热传导及其热响应。不同于先前的数值研究需要在计算开始时初始化液-汽界面波的形状,本文中流体区域的计算域最初被饱和液体占据。在较短的初始期间,在加热器底部施加的较小的温度扰动会触发液-气界面的泰勒不稳定性。因此,本文代表了在水平加热器上进行薄膜沸腾传热的更直接和完整的数值模拟。发现模拟的时间和空间平均努塞尔数与先前的相关方程非常吻合。还对气相膜厚度的时空变化进行了数值研究,并与现有的相关方程进行了比较。已经证明,在膜沸腾过程中,心脏顶表面的温度随位置和时间而变化。尽管瞬态膜沸腾模式可能取决于在初始阶段施加在加热器底部的温度扰动,但时间和空间平均的膜沸腾热通量与初始温度扰动无关。

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