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Enhanced Heat Transfer for Boiling of a Refrigerant on a Micro-Structured Cylindrical Surface and Effect of Saturation Temperature

机译:制冷剂在微结构圆柱表面上的沸腾增强传热及饱和温度的影响

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Boiling on the outside surface of cylindrical tubes is an important heat transfer process widely used in industry applications. It is known that boiling heat transfer coefficient increases with increasing saturation temperature. However, a quantitative measure of saturation temperature effect on boiling heat transfer is not readily available, especially for boiling on surfaces of microstructures. This work was motivated by the need to predict evaporator performance in a chiller while taking into account the effect of saturation temperature on boiling heat transfer coefficient. Experiments of boiling of refrigerant R123 on the micro-structured outside surface of an evaporator tube have been performed at three saturation temperatures in the range of 4.4 to 17.8°C. Water flows inside the test tubes and provides heat to the refrigerant for boiling. In addition, experiments of R123 boiling on smooth cylindrical tubes have been performed at the saturation temperature 4.4°C to provide a baseline to quantify the enhancement in boiling heat transfer due to microstructures on the test tubes.For boiling on the micro-structured surface, the boiling heat transfer coefficient increases by nearly 15% for the temperature range considered in this work. Measurements also showed that heat transfer coefficient for boiling on the test tubes of micro-structures is 12.3 times higher than boiling on the smooth surface. The Cooper correlationover-predicted by 40% the boiling heat transfer coefficient on the smooth cylindrical surface, but significantly under-predicted the performance for boiling on the tubes of micro-structures. It is found that the prediction of Cooper correlation multiplied by an enhancement factor 7.9 has a good agreement with measured heat transfer coefficient for boiling on the tubes of micro-structures at all the three saturation temperatures. Visual observations indicated that bubble departure characteristics on the micro-structured surface are different from those on the smooth surface. In addition to promoted bubble nucleation by re-entrant cavities on the micro-structured surface, the different bubble departure characteristics also contribute to the enhancement of boiling performance.
机译:在圆柱管的外表面上沸腾是重要的传热过程,广泛用于工业应用中。众所周知,沸腾传热系数随着饱和温度的升高而增加。然而,饱和温度对沸腾传热的影响的定量测量尚不可用,特别是对于微结构表面上的沸腾。这项工作的动机是需要预测冷却器中的蒸发器性能,同时考虑饱和温度对沸腾传热系数的影响。已经在4.4至17.8℃范围内的三个饱和温度下进行了制冷剂R123在蒸发管的微结构外表面上沸腾的实验。水在试管内流动,并向制冷剂提供热量以使其沸腾。此外,已在4.4°C的饱和温度下进行了R123在光滑圆柱管上沸腾的实验,以提供一个基线来量化由于试管上的微结构而引起的沸腾传热增强。 对于在微结构表面上沸腾,在这项工作中考虑的温度范围内,沸腾传热系数提高了近15%。测量还表明,在微结构试管上沸腾的传热系数是在光滑表面上沸腾的传热系数的12.3倍。库珀相关性 过度预测了光滑圆柱表面上沸腾传热系数的40%,但大大低估了微结构管上的沸腾性能。发现在所有三个饱和温度下,将库珀相关系数乘以增强因子7.9的预测与在微结构管上沸腾的实测传热系数具有良好的一致性。视觉观察表明,微结构表面上的气泡离开特性不同于光滑表面上的气泡离开特性。除了通过微结构表面上的凹腔促进气泡成核外,不同的气泡离开特性也有助于提高沸腾性能。

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