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Experimental study on the constituent separation performance of binary zeotropic mixtures in horizontal branch T-junctions

机译:水平支化T形结中二元共沸混合物成分分离性能的实验研究

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In this paper, the constituent separation performance of binary zeotropic mixtures, R134a/R600a, in horizontal branch T-junctions was experimentally investigated. The effects of flow conditions, mixture compositions and T-junction geometries on the constituent separation performance were studied. During the experiments, the inlet mass flux and quality were varied from 200 to 300 kg·m−2·s−1and from 0.1 to 0.9, respectively. Meanwhile, the mass flux of the branch was regulated by keeping the branch-inlet mass flow ratios of 0.3 and 0.5. Furthermore, constituent distributions were compared for three different inlet R134a mass fractions, namely 0.3030, 0.5202 and 0.7053. The required mass fractions of R134a at the inlet and outlet of T-junctions were calculated based on the measured liquid density. As for the T-junction geometry, the diameter ratio of the branch tube to the inlet tube was set to be 0.75 and 1.0, and three branch angles, namely 45°, 90°, 135°, were considered. In order to represent the degree of actual separation to the complete separation, constituent separation efficiency is defined as the difference of the fractions of constituents taken off in the branch. Based on the generated experimental data, it’s found that there generally exists an inflection point of separation around the vapor quality 0.2. Before the inflection point, the efficiency generally increases with the increase of inlet vapor quality. After that, the separation efficiency gradually decreases from the positive to the negative. It means that more R600a is extracted into the branch, due to the lower vapor density and vapor dynamic viscosity. Furthermore, for the three mixture compositions, R134a/R600a with an R134a fraction of 0.3030 has the best constituent separation performance. The largest variation range of outlet fraction is from 0.2559 to 0.3443 under the mass flow ratio of 0.3 and mass flux of 200 kg·m−2·s−1. However, the highest separation efficiency 9.49% is obtained under the mass flow ratio of 0.5. As for the effect of T-junction geometry, when the inlet quality is less than 0.4, increasing the diameter ratio can enhance the constituent separation. Compared with the angles 45° and 135°, the largest separation capacity is obtained by the angle 90°.
机译:本文研究了二元共沸混合物R134a / R600a在水平分支T型结中的成分分离性能。研究了流动条件,混合物组成和T型接头几何形状对组分分离性能的影响。在实验过程中,入口质量通量和质量分别在200至300 kg·m-2·s-1和0.1至0.9之间变化。同时,通过保持分支入口质量流量比为0.3和0.5来调节分支的质量通量。此外,比较了三种不同进口R134a质量分数(即0.3030、0.5202和0.7053)的成分分布。基于测得的液体密度,计算出T型接头进口和出口处R134a所需的质量分数。关于T形结的几何形状,将支管与入口管的直径比设定为0.75和1.0,并且考虑三个支管角,即45°,90°,135°。为了表示实际分离到完全分离的程度,将组分分离效率定义为分支中所提取组分的分数之差。根据生成的实验数据,发现通常在蒸气质量0.2附近存在一个分离拐点。在拐点之前,效率通常随着入口蒸气质量的增加而增加。之后,分离效率从正向负逐渐降低。这意味着由于较低的蒸气密度和蒸气动态粘度,更多的R600a被提取到支链中。此外,对于这三种混合物组合物,R134a分数为0.3030的R134a / R600a具有最佳的成分分离性能。在质量流量比为0.3,质量通量为200 kg·m-2·s-1的情况下,出口分数的最大变化范围为0.2559至0.3443。但是,在质量流量比为0.5时,分离效率最高,为9.49%。至于T型结的几何形状,当入口质量小于0.4时,增大直径比可以增强成分分离。与45°和135°角相比,90°角可获得最大的分离能力。

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