首页> 外文会议>International Conference on Microchannels and Minichannels; 20050613-15; Toronto(CA) >Visualization of Convective Boiling Heat Transfer in Single Micro-Conduits with Different Shapes of Cross Sections
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Visualization of Convective Boiling Heat Transfer in Single Micro-Conduits with Different Shapes of Cross Sections

机译:具有不同横截面形状的单个微管道中对流沸腾传热的可视化

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Visualization experiments of convective boiling in transparent single micro conduits with the same hydraulic diameter but different cross sections are carried out with simultaneous measurement of local heat transfer coefficients and pressure losses. Two different cross sections with the same similar hydraulic diameters are applied: A circular microtube of 210μm in diameter and a square microchannel of 214μmx 214μm cross section. ITO/Ag thin film of 100 nm is sputtered on the outer surface of the conduits for the direct joule heating. The convective boiling shows some periodic variation of different flow patterns in both square and circular conduits. These flow patterns include bubbly, plug, slug, annular and capillary flows. The capillary flow pattern is the independent liquid droplets moving in the flow direction and very rarely observed in conventional tubes. The reason of such variation of flow patterns is that confined spaces limit the bubble growth in radial direction. So the nucleation bubble grows in both upstream and downstream and makes the flow pattern varies radically. The square microchannel conduit has more simple flow pattern variation, more nucleation bubbles and larger local heat transfer coefficients at lower vapor quality. It is due to that corners of the square microchannel act as helps nucleation cavities. Corners also promotes the formation of liquid film and the contact line between liquid and wall, which can stabilize the flow field. Local heat transfer coefficients decrease with increasing local vapor qualities. Local heat transfer coefficients increase with increasing boiling number but have their maximum value when boiling number reaches critical value. Such peculiar heat transfer characteristics can also be explained by the visualization results.
机译:在同时测量局部传热系数和压力损失的情况下,在具有相同水力直径但横截面不同的透明单个微导管中进行对流沸腾的可视化实验。使用了两个具有相同相似水力直径的不同横截面:直径为210μm的圆形微管和横截面为214μmx214μm的方形微通道。将100 nm的ITO / Ag薄膜溅射在导管的外表面上,以直接进行焦耳加热。对流沸腾显示在方形和圆形管道中不同流型的一些周期性变化。这些流动模式包括气泡,塞流,团状,环形和毛细管流。毛细管流动模式是沿流动方向移动的独立液滴,在常规管中很少观察到。流动模式的这种变化的原因是,狭窄的空间限制了气泡沿径向的生长。因此,成核气泡在上游和下游均增长,并使流动方式发生根本变化。方形微通道导管在较低的蒸汽质量下具有更简单的流型变化,更多的成核气泡和更大的局部传热系数。这是由于方形微通道的角起到了帮助形核腔的作用。拐角还促进了液膜的形成以及液与壁之间的接触线,从而可以稳定流场。局部传热系数随着局部蒸气质量的增加而降低。局部传热系数随着沸腾数的增加而增加,但当沸腾数达到临界值时其最大值。这种特殊的传热特性也可以通过可视化结果来解释。

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