论文标题
一个理论框架,用于稳定喂养蒸发液滴的全面建模和共同假设的有效性
A theoretical framework for comprehensive modeling of steadily fed evaporating droplets and the validity of common assumptions
论文作者
论文摘要
建立了一个理论框架,以模拟连续喂养的液滴的蒸发,这是高热通量电子热管理中的有希望的工具。使用框架,开发了一个综合模型,用于将均置于加热的平坦基板上的半球形水滴,该液滴融合了所有相关的运输机制:液滴内的浮力和热毛细血管对流以及气体域中蒸气的扩散和对流传输。在界面,质量,动量和热量耦合也可以考虑到所有相关物理方面,包括几种相关的物理方面,包括几个很少考虑的界面现象,例如Stefan气体流量以及从界面到周围环境的辐射热传递。开发的模型利用了两个阶段的温度依赖性特性,包括密度和所有相关物理,包括Marangoni流,这使该模型变得前所未有。此外,利用这种综合模型,发现了一个非单调界面温度分布,具有双温度降低,用于在高基质温度的情况下由于浮力而导致内部对流的半球液滴。还采用了建议的框架来构建几种简化的模型,这些模型采用了液滴蒸发的常见假设和这些模型的计算性能,从而评估了常用的简化假设的有效性。基准模拟表明,气流的省略,即忽略气相中的对流运输,导致蒸发率低估了23-54%。当考虑气体流量但使用Boussinesq近似而不是在整个气体结构域中分配温度依赖性密度的浮力效果时,蒸发速率可低估高达16%。
A theoretical framework is established to model the evaporation from continuously fed droplets, promising tools in the thermal management of high heat flux electronics. Using the framework, a comprehensive model is developed for a hemispherical water droplet resting on a heated flat substrate incorporating all of the relevant transport mechanisms: buoyant and thermocapillary convection inside the droplet and diffusive and convective transport of vapor in the gas domain. At the interface, mass, momentum, and thermal coupling of the phases are also made accounting for all pertinent physical aspects including several rarely considered interfacial phenomena such as Stefan flow of gas and the radiative heat transfer from interface to the surroundings. The model developed utilizes temperature dependent properties in both phases including the density and accounts for all relevant physics including Marangoni flow, which makes the model unprecedented. Moreover, utilizing this comprehensive model, a nonmonotonic interfacial temperature distribution with double temperature dips is discovered for a hemispherical droplet having internal convection due to buoyancy in the case of high substrate temperature. Proposed framework is also employed to construct several simplified models adopting common assumptions of droplet evaporation and the computational performance of these models, thereby the validity of commonly applied simplifying assumptions, are assessed. Benchmark simulations reveal that omission of gas flow, i.e. neglecting convective transport in gas phase, results in the underestimation of evaporation rates by 23-54%. When gas flow is considered but the effect of buoyancy is modeled using Boussinesq approximation instead of assigning temperature dependent density throughout the gas domain, evaporation rate can be underestimated by up to 16%.