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Wave characteristics of falling liquid films under the influence of positive and negative inclination or electrostatic forces

机译:正负倾斜或静电力影响下下落的液膜的波动特性

摘要

Falling liquid films are thin liquid layers flowing down rigid vertical or inclined walls driven by gravity. In industry falling films are used in various applications such as refrigeration, cooling of mechanical or electronic systems, chemical processing, desalination and food processing. They generally exhibit higher heat and mass transfer rates compared to flows which are strictly aligned to the rigid wall. This increase in heat and mass transfer is caused by the wavy topology, which is attended by different types of vortices in the liquid and the gaseous phase. The characteristic vortices in the liquid phase are a circulating eddy in the main wave hump (also called circulating wave) and a vortex in the first capillary minimum associated with the phenomenon of flow reversal. The existence and the physical mechanism involved in those vortices are well-known. However, the flow conditions under which they occur have still been unclear. In addition to films flowing down the upper side of an inclined wall, films flowing down the underside of an inclined plate have been considered. In the latter case, the gravitational force acts destabilizing and, owing to the negative value of the inclination number, this condition is called "negative gravity". Besides the two vortices which can occur in both configurations, a further phenomenon that occurs only in hanging film flows is dripping. In the present doctoral thesis, two model approaches have been utilized, namely the weighted integral boundary layer (WIBL) model and direct numerical simulations (DNS) in order to identify the conditions for the onset of circulating waves, flow reversal, and gravitational dripping. For investigating electrostatically induced spraying of a dielectric fluid, the WIBL model and the numerical code of the DNS have been extended by the electrostatic surface force. From the modeling point of view, the developed equations of the WIBL model revealed that the electrostatic force is similar to the gravitational body force with an additional non-linear contribution. From the knowledge obtained by the simulations, analytical criteria for the onset of circulating waves and flow reversal based on the wave celerity, the average film thickness and the maximum and minimum film thickness have been approximated using self-similar parabolic velocity profiles. This approximation has been validated by second-order WIBL and direct numerical simulations. It is shown that the onset of circulating waves in the phase diagram for homoclinic solutions (waves of infinite wavelength) is strongly dependent on the inclination, but independent of the streamwise viscous dissipation effect. On the contrary, the onset of flow reversal shows a clear dependence on the viscous dissipation. Furthermore, simulation results for limit cycles (finite wavelength) reveal a strong increase of the corresponding critical Reynolds number with the excitation frequency. The phenomenon of gravitational dripping is associated with a pressure gradient in crosswise direction. A criterion for the onset of dripping is derived based on a force balance between gravitational forces of the liquid in the main wave hump and surface tension. This force balance is found to be violated in the simulation results of the WIBL model. The model does not account for a crosswise force balance, owing to the integration of the streamwise boundary layer momentum equation across the depth of the film. As a consequence, the model is found to be not well-suited for the prediction of dripping. However, DNS and WIBL results agree well before dripping occurs. The influence of the electrostatic surface force is found to be well-captured by the WIBL model in a specific range of parameters. Due to a quasi-constant pressure in crosswise direction of the film, the physical mechanisms of electrostatically induced spraying differ from the mechanisms involved in dripping. An explanation for the occurrence of spraying is the non-linear growth of the force with an increase in film thickness. Above a critical value of the electric potential, the increase in the destabilizing electrostatic pressure exceeds the increase of the stabilizing surface tension force. Consequently, small perturbations grow infinitely up to spraying, which finally ruptures the film surface.
机译:下降的液膜是薄的液层,在重力作用下顺着刚性的垂直或倾斜壁向下流动。在工业上,降膜可用于各种应用,例如制冷,机械或电子系统的冷却,化学加工,脱盐和食品加工。与严格对准刚性壁的流相比,它们通常表现出更高的传热和传质速率。传热和传质的增加是由波浪形的拓扑结构引起的,液相和气相中的不同类型的涡旋伴随着波浪形的拓扑结构。液相中的特征涡流是主波峰(也称为循环波)中的循环涡流和与流动逆转现象相关的第一毛细管极小值中的涡旋。这些旋涡的存在及其物理机制是众所周知的。但是,其发生的流动条件仍不清楚。除了向下流过倾斜壁的上侧的膜之外,还考虑了向下流向倾斜板的下侧的膜。在后一种情况下,重力作用不稳定,并且由于倾斜数的负值,该条件被称为“负重力”。除了可能在两种配置中出现的两个涡流外,仅在悬膜流动中还会发生的另一种现象是滴落。在本博士论文中,已采用了两种模型方法,即加权积分边界层(WIBL)模型和直接数值模拟(DNS),以识别引起循环波,逆流和重力滴落的条件。为了研究介电液的静电感应喷涂,通过静电表面力扩展了WIBL模型和DNS的数字代码。从建模的角度来看,WIBL模型的已开发方程表明,静电力类似于重力,具有非线性附加作用。从模拟获得的知识中,已经使用自相似的抛物线速度曲线估算了基于波速,平均膜厚以及最大和最小膜厚的循环波发生和逆流的分析标准。该近似值已通过二阶WIBL和直接数值模拟验证。结果表明,在同相溶液的相图中,循环波的开始(无限波长的波)在很大程度上取决于倾角,但与流向粘性耗散效应无关。相反,流动逆转的开始显示出对粘性耗散的明显依赖性。此外,极限循环(有限波长)的仿真结果表明,相应的临界雷诺数随激发频率而大大增加。重力滴落现象与横向压力梯度有关。基于主浪峰中液体的重力与表面张力之间的力平衡,得出滴落开始的标准。发现该力平衡在WIBL模型的仿真结果中被破坏。该模型没有考虑横向力平衡,这是由于跨膜深度的流向边界层动量方程的积分。结果,发现该模型不适用于滴落的预测。但是,DNS和WIBL结果在滴落发生之前就很一致。发现在特定参数范围内,WIBL模型可以很好地捕获静电表面力的影响。由于膜的横向方向上的准恒定压力,静电感应喷涂的物理机制与滴落涉及的机制不同。发生喷涂的一种解释是力随着膜厚的增加而非线性增长。在电位的临界值以上,去稳定化静电压力的增加超过稳定化表面张力的增加。因此,细微的扰动会无限增加直至喷涂,最终使薄膜表面破裂。

著录项

  • 作者

    Rohlfs Wilko;

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  • 年度 2016
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  • 原文格式 PDF
  • 正文语种 eng
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