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Harmonic mechanical excitations of steady convective instabilities: A means to get more uniform heat transfers in mixed convection flows?

机译:稳定对流不稳定性的谐波机械激发:一种在混合对流中获得更均匀传热的方法?

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In laminar mixed convection flows, steady thermoconvective patterns generate non uniform heat and/or mass transfers at walls that can be detrimental in some industrial processes. For instance the longitudinal thermoconvective patterns of Poiseuille-Rayleigh-Benard (PRB) flows generate non uniform thin films or coatings when they are present in cold wall horizontal Chemical Vapor Deposition (CVD) reactors. The aim of this paper is to show that, when the basic steady flow is convectively unstable against an unsteady flow regime, introducing small harmonic mechanical excitations in the basic flow may enable to obtain more uniform time averaged heat transfers. More specifically, three-dimensional direct numerical simulations are used to characterize the temperature field and wall heat transfer associated with unsteady wavy convective instabilities of PRB flows that result from harmonic excitations of the longitudinal thermoconvective rolls at channel inlet. A design of experiments is used to build cubic response surfaces of the different quantities analyzed (growth length of the wavy rolls, magnitude of their spanwise oscillations, wall Nusselt number ...) on a wide range of the flow parameters. Air PRB flows (Pr = 0.71) in channels of aspect ratios equal to Width/Height = 10 and 150 ≤ Length/Height ≤ 300, for Reynolds numbers 100 ≤ Re ≤ 300 and Rayleigh numbers 5000 ≤ Ra ≤ 16,000 are considered. Comparisons with experiments are presented and a good agreement is obtained. The optimal conditions to have uniform heat transfers on the horizontal walls of PRB flows correspond to the minimal growth length of the wavy rolls until saturation and the maximum magnitude of their spanwise oscillations. They are approximately obtained for moderate Reynolds number (Re ≈ 150), high Rayleigh numbers (Ra ≈ 15,000), low excitation frequency and rather high excitation magnitude. A discussion of these results for the applications to CVD in horizontal rectangular reactors at atmospheric pressure is finally proposed.
机译:在层流混合对流中,稳定的热对流模式会在壁上产生不均匀的热量和/或质量传递,这在某些工业过程中可能是有害的。例如,当Poiseuille-Rayleigh-Benard(PRB)流的纵向热对流模式出现在冷壁卧式化学气相沉积(CVD)反应器中时,会生成不均匀的薄膜或涂层。本文的目的是表明,当基本稳定流在非恒定流状态下对流不稳定时,在基本流中引入小的谐波机械激励可以实现更均匀的时间平均传热。更具体地说,使用三维直接数值模拟来表征与PRB流动的不稳定波浪对流不稳定性有关的温度场和壁传热,PRB流动是由通道入口处纵向热对流辊的谐波激发引起的。实验设计用于在各种流量参数上构建不同数量(波浪状卷的生长长度,其跨度振动幅度,壁努塞尔特数...)的不同数量的立方响应面。对于雷诺数100≤Re≤300和瑞利数5000≤Ra≤16,000的情况,考虑空气PRB(Pr = 0.71)在宽高比等于Width / Height = 10且150≤Length / Height≤300的通道中流动。提出了与实验的比较,并获得了良好的协议。在PRB流动的水平壁上具有均匀传热的最佳条件对应于波浪形卷的最小生长长度,直到饱和为止,并且其跨度振动也达到最大。对于中等的雷诺数(Re≈150),较高的瑞利数(Ra≈15,000),较低的激励频率和较高的激励幅度,可以近似获得它们。最后提出了在大气压力下将这些结果用于水平矩形反应器中的CVD的讨论。

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