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首页> 外文期刊>Journal of Heat Transfer >Spreading Characteristics and Microscale Evaporative Heat Transfer in an Ultrathin Film Containing a Binary Mixture
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Spreading Characteristics and Microscale Evaporative Heat Transfer in an Ultrathin Film Containing a Binary Mixture

机译:含二元混合物的超薄膜的扩散特性和微尺度蒸发传热

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摘要

Using image-analyzing interferometry, the thickness profile, in the range of δ{sub}0 (adsorbed thickness) <δ<3 μm, at the leading edge of a moving ultrathin film with phase change, was measured for a mixture of pentane-octane and compared to that of pure pentane. An improved data-analysis procedure was used to enhance the use of the measured thickness profile. There were significant differences between these two systems, demonstrating the presence of large Marangoni interfacial shear stresses with the mixture. A control volume model was developed to evaluate the differences between the pure fluid and the mixture. The disjoining pressure at the leading edge was found to control fluid flow in the evaporating pure system. However, due to Marangoni stresses, the effect of disjoining pressure on the mixture was found to be small at steady state for the fluxes studied. With an upstream bulk mixture of 2% octane and 98% pentane, a shear stress due to the gradient of the liquid-vapor interfacial surface tension resulting from distillation controlled fluid flow in the contact line region. The average curvature of the evaporating pseudo-steady state pure system was significantly larger (smaller length and larger apparent contact angle at δ = 0.1μm) than the isothermal value, whereas the reverse occurred for the mixture. Using a continuum model, a comparison of numerically obtained Marangoni stresses and local evaporative heat flux profiles between the two systems was also made.
机译:使用图像分析干涉仪,在相变的移动超薄膜的前缘处测量了δ{sub} 0(吸附厚度)<δ<3μm范围内的厚度分布,以分析戊烷-辛烷值与纯戊烷值相比。使用改进的数据分析程序来增强对测得的厚度轮廓的使用。这两个系统之间存在显着差异,表明混合物中存在较大的Marangoni界面剪切应力。建立了一个控制体积模型来评估纯流体和混合物之间的差异。发现在前缘处的分离压力控制着蒸发纯系统中的流体流动。但是,由于Marangoni应力,对于研究的焊剂,分离压力对混合物的影响在稳态下很小。在上游的本体混合物为2%的辛烷和98%的戊烷的情况下,由于在接触线区域内受蒸馏控制的流体流动而产生的液-气界面张力的梯度导致了剪切应力。蒸发的拟稳态纯系统的平均曲率比等温值大得多(在δ=0.1μm时长度更短,表观接触角更大),而混合物则相反。使用连续模型,还对两个系统之间的数值获得的Marangoni应力和局部蒸发热通量曲线进行了比较。

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