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Numerical investigation of film boiling on a horizontal wavy wall Nikhil

机译:水平波浪壁Nikhil上薄膜沸腾的数值研究

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Liquid-vapour interface dynamics and instability characteristics together with heat transfer over a wavy wall are studied numerically in the context of saturated natural convection horizontal film boiling. Film boiling computations have been performed using a numerical framework developed for phase change problems on unstructured grids that incorporates a coupled level set and volume of fluid interface capturing algorithm. The film boiling behaviour as influenced by geometric features of the sinusoidal wavy heater is ascertained and discussed in detail. The heater wavelength is varied in a wide range encompassing the disturbance spectrum primarily governing bubble release in horizontal film boiling, for several different amplitude values. A link between geometrical and hydrodynamic aspects is established by showing that the individual peaks of the wavy surface affect interface evolution only for heater wavelengths larger than the critical Rayleigh-Taylor wavelength. Additionally, the effect of wall superheat corresponding to different wavy wall geometries is also discussed. It is observed that the interface dynamics and heat transfer result from a coupled effect of the geometrical features of the heater surface, in addition to an interplay with the wall superheat. While a propensity towards transition in the mode of instability is observed at enhanced wall superheats affecting the interfacial dynamics, the wavy heater topology is observed to avert such a hydrodynamic transition under certain cases. Simultaneously, the effect of wavy geometry on film boiling heat transfer is highlighted to be non-analogous to single phase flows.
机译:在饱和自然对流水平薄膜沸腾的背景下,对液体-蒸汽界面的动力学和不稳定性以及波浪壁上的传热进行了数值研究。已经使用针对非结构化网格上的相变问题开发的数值框架执行了薄膜沸腾计算,该框架结合了耦合的液位集和流体界面捕获算法的体积。确定并详细讨论了受正弦波状加热器的几何特征影响的薄膜沸腾行为。对于几个不同的振幅值,加热器的波长在宽泛的范围内变化,其中包括主要控制水平膜沸腾中气泡释放的干扰光谱。通过显示波浪形表面的各个峰仅在加热器波长大于临界Rayleigh-Taylor波长的情况下影响界面演化,从而建立了几何和水动力方面之间的联系。另外,还讨论了对应于不同波浪形壁几何形状的壁过热的影响。可以观察到,除了与壁过热之间的相互作用外,界面动力学和传热还源于加热器表面几何特征的耦合作用。虽然在影响界面动力学的增强壁过热条件下观察到了以不稳定性模式转变的趋势,但在某些情况下,观察到波浪形加热器拓扑可以避免这种流体动力转变。同时,波浪形几何形状对薄膜沸腾传热的影响被强调为与单相流无关。

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