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Two-phase refrigerant flow distribution in a multipass evaporator with vertical upward main tube (3rd report: prediction model of the flow distribution)

机译:主管垂直向上的多程蒸发器中的两相制冷剂流量分布(第三次报告:流量分布的预测模型)

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摘要

In this article, a calculation model that enables to predict two-phase flow distribution in a multipass evaporator is proposed. The model considers the multipass evaporator as the combination of simple elements, i.e. straight pipes and T-junctions, and utilizes the correlations to predict the pressure drop at the elements. For the T-junction, however, we have so little knowledge, especially for the small diameter T-junction, that we make some experiments to evaluate the existing correlations for the junction pressure drop. We also do not have reliable model for predicting the phase separation characteristics, so that we used the empirical equations for liquid division ratio derived in our previous papers. By this model, gas phase flow distribution to each pass is determined as it makes the pressure at the outlet of each pass equal. Calculation results well predict the previously presented experimental data that were obtained under the condition of larger quality at the header inlet. The suitableness of this model suggests that the complexity of the two-phase flow distribution in multipass tube attributes to the phase separation phenomena in dividing two-phase flow at a T-junction.
机译:在本文中,提出了一种能够预测多程蒸发器中两相流分布的计算模型。该模型将多程蒸发器视为简单元素(即直管和T型接头)的组合,并利用相关性预测元素上的压降。但是,对于T型结,我们了解的很少,特别是对于小直径T型结,我们进行了一些实验来评估现有的结压降相关性。我们也没有可靠的模型来预测相分离特性,因此我们使用了以前论文中得出的液分比经验方程。通过此模型,可以确定到每个通道的气相流量分布,因为它使每个通道的出口压​​力相等。计算结果很好地预测了先前介绍的实验数据,这些数据是在集管入口质量较高的条件下获得的。该模型的适用性表明,多通管中两相流分布的复杂性归因于在T型结处划分两相流的相分离现象。

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