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Experimental investigation of convective structure evolution and heat transfer in quasi-steady evaporating liquid films

机译:准稳态蒸发液膜对流结构演变与传热的实验研究

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The stability, convective structure, and heat transfer characteristics of upward-facing, evaporating, thin liquid films were studied experimentally. Dichloromethane, chloroform, methanol, and acetone films with initial thicknesses of 2-5 mm were subjected to constant levels of superheating until film rupture occurred (typically at a thickness of around 50 μm). The films resided on a temperature controlled, polished copper plate incorporated into a closed pressure chamber free of non-condensable gasses. The dynamic film thickness was measured at multiple points using a non-intrusive ultrasound ranging system. Instability wavelength and convective structure information was obtained using double-pass schlieren imaging. The sequence of the convective structures as the film thins due to evaporation is observed to be as follows: (1) large, highly variable cells, (2) concentric rings and spirals, and (3) apparent end of convection. The transition from large, variable cells to concentric rings and spirals occurs at a Rayleigh number of 4800 ± 960. The apparent end of convection occurs at a Rayleigh number of 1580 ± 180. At the cessation of convection, the Nusselt number is nearly unity, indicating that there is little heat transfer in the film due to convection. In films where the Rayleigh number is above this transitional value, the Nusselt number increases with increasing Rayleigh number. The current results suggest that the equilibrium condition at the evaporating surface suppresses surface temperature variation, effectively eliminating thermocapillary-driven instability.
机译:实验研究了向上蒸发的液态薄膜的稳定性,对流结构和传热特性。对初始厚度为2-5 mm的二氯甲烷,氯仿,甲醇和丙酮薄膜进行恒定的过热处理,直到薄膜破裂(通常厚度约为50μm)为止。薄膜驻留在温度控制的抛光铜板上,该铜板并入了无不可凝气体的密闭压力室。使用非侵入式超声波测距系统在多个点测量动态膜厚度。不稳定波长和对流结构信息是使用双通道schlieren成像获得的。观察到由于蒸发而使薄膜变薄时,对流结构的顺序如下:(1)大的,高度可变的晶胞;(2)同心环和螺旋形;(3)对流的明显终点。从大的可变像元到同心环和螺旋线的转变发生在瑞利数为4800±960的情况下。对流的视在末端出现在瑞利数为1580±180的情况下。对流停止时,努塞尔数几乎为1,这表明由于对流,薄膜中的热传递很小。在瑞利数高于此过渡值的电影中,努塞尔数随着瑞利数的增加而增加。目前的结果表明,蒸发表面的平衡条件抑制了表面温度的变化,有效消除了热毛细管驱动的不稳定性。

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