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Entrainment mass transfer in annular flow regime of two-phase carbon dioxide

机译:两相二氧化碳环形流动状态下的夹带传质

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Having more heat transfer rate and lower pressure drop, along with better environmental treatment, carbon dioxide has drawn the attention of many researchers. Most of the two-phase heat transfer analyses are involved in estimation of dry-out phenomenon in order to avoid heat transfer drops. Entrainment, because of having great influence on dry-out occurrence, is studied in this article. Most of the available models for entrainment are experiment-based and therefore applicable in restricted conditions. In the present study, a physical model is proposed for simulation of entrainment in annular flow regime of liquid-vapor in a vertical tube. The tube is supposed to be warming up by a constant and uniform heat flux applied on its lateral area. The proposed model is general and can be applied to all kind of fluids of different working conditions; it is verified with some experimental data available in the literature. Entrainment contribution of mass transfer is compared with evaporation contribution through introducing a factor which is called “Mass Transfer Ratio” (MTR). The magnitude of this factor demonstrates the significance of entrainment phenomenon. MTR factor is compared with some widely-used working fluids.
机译:具有更高的传热速率和更低的压降,以及更好的环境处理,二氧化碳引起了许多研究人员的关注。为了避免传热下降,大多数两相传热分析都涉及干燥现象的估计。本文研究了夹带,因为夹带对变干的发生有很大的影响。大多数可用的训练模型都是基于实验的,因此适用于受限条件。在本研究中,提出了一种物理模型,用于模拟垂直管中液体蒸气的环形流动状态下的夹带。该管应该通过在其侧面施加恒定且均匀的热通量来升温。所提出的模型是通用的,可以适用于各种不同工况的流体。已有文献中提供的一些实验数据对此进行了验证。通过引入称为“传质比”的因素,将传质的夹带作用与蒸发作用进行比较。 (地铁)。该因子的大小表明了夹带现象的重要性。将MTR因子与一些广泛使用的工作液进行了比较。

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