Novel dimensionless predictive flow pattern map for HFOs inside microscale enhanced tubes

Q1 Chemical Engineering
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引用次数: 0

Abstract

Models designated to predict flow patterns in microscale geometries with enhanced surfaces such as micro-finned tubes are scarce in the literature and new low-GWP HFOs could benefit from the utilization of such geometries. Therefore, HFO1234ze(E)’s condensation flow patterns were subjected to visualization inside micro-finned tubes ranging from 4 to 7 mm outer diameters with various geometrical figures. The saturation temperature was set to 30 °C, vapor qualities ranged in the scope of 0.01 to 0.9, and mass fluxes in the magnitude of 100 to 400 kg m-2 s-1. Four distinctive flow patterns are observed, namely intermittent, annular, wavy-stratified, and transitional. Stratification only transpired at low mass fluxes (mainly below 100 kg m-2 s-1) and intermittent flow was only present at vapor qualities close to full condensation. The range in which transitional flow is observable shrinks with a progressive trend of mass flux. The impact of diameter was observed to be negligible, however, a more meticulous assessment highlights smaller ranges of vapor qualities in which transitional flow is present for the tube of 5 mm OD whose helix angle is substantially larger. Datapoints were juxtaposed to previous models of Doretti et al., Chen et al., Mandhane et al., and Jige et al. and the results attested to an inadequacy of accurate predictions made for tube of 4 mm OD. Noting the absence of surface tension force in the aforementioned maps, a novel flow pattern map based on modified Froude versus modified Weber numbers provided an accurate prediction for the three cases under study. Ultimately the model was also deemed fairly suitable for visualization datasets collected from literature.

微尺度增强管内氢氟烯烃的新型无量纲预测流动模式图
用于预测具有增强表面的微尺度几何形状(如微翅片管)中流动模式的模型在文献中很少见,而新型低全球升温潜能值氢氟烯烃可以从利用这种几何形状中获益。因此,HFO1234ze(E)的冷凝流动模式在外径为 4 至 7 毫米、具有不同几何形状的微翅片管内进行了可视化。饱和温度设定为 30 °C,蒸汽质量范围为 0.01 至 0.9,质量通量范围为 100 至 400 kg m-2 s-1。观察到四种不同的流动模式,即间歇式、环状、波浪分层式和过渡式。分层只在低质量通量(主要低于 100 kg m-2 s-1)时出现,间歇流动只在蒸汽质量接近完全凝结时出现。随着质量通量的逐渐增大,可观测到过渡流的范围也在缩小。直径的影响可以忽略不计,但更细致的评估显示,外径为 5 毫米、螺旋角更大的管子出现过渡流的蒸汽质量范围更小。数据点与 Doretti 等人、Chen 等人、Mandhane 等人和 Jige 等人以前的模型进行了对比,结果证明外径为 4 毫米的管子的精确预测是不够的。注意到上述地图中没有表面张力,一个基于修正的弗劳德数和修正的韦伯数的新型流动模式图为所研究的三种情况提供了准确的预测。最终,该模型也被认为相当适合从文献中收集的可视化数据集。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
International Journal of Thermofluids
International Journal of Thermofluids Engineering-Mechanical Engineering
CiteScore
10.10
自引率
0.00%
发文量
111
审稿时长
66 days
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