Hydrodynamic behavior of liquid falling film over horizontal tubes: Effect of hydrophilic circular surface on liquid film thickness and heat transfer

被引:11
作者
Ramadan, Zaher [1 ]
Park, Chan Woo [1 ,2 ]
机构
[1] Jeonbuk Natl Univ, Sch Mech Design Engn, 567 Baekje Daero, Jeonju 561756, Jeonbuk, South Korea
[2] Jeonbuk Natl Univ, Dept Energy Storage, Convers Engn Grad Sch, Jeonju Si 54896, Jeonbuk, South Korea
基金
新加坡国家研究基金会;
关键词
Computational fluid dynamics (CFD); Contact angle; Falling film; Film thickness; Heat transfer coefficient; Wettability;
D O I
10.1016/j.csite.2020.100821
中图分类号
O414.1 [热力学];
学科分类号
摘要
Falling film configurations have widely been used in various types of refrigeration systems, and wettability has played an important role in characterizing the heat and mass transfer due to varying hydrodynamic behavior. The present paper focuses on a three-dimensional computational fluid dynamics (CFD) simulation to investigate the effect of hydrophilic circular surface on hydrodynamic behavior of liquid falling film over the heated horizontal circular tubes. First, the thickness of the liquid falling film and the liquid distribution around the circumferential and axial directions were analyzed at a feed water temperature of 20 degrees C for three film Reynolds numbers of 12, 24, and 36 (50 < (Q) over dot(feed) < 150 ml.min(-1)) and three heat fluxes of 5, 10, and 15 kW m(-2). The influences of the contact angle on the liquid film hydrodynamics and heat transfer were then analyzed. The results showed that at a low feed film Reynolds number, even for super-hydrophilic nature (e.g., contact angles of 0 degrees or 10 degrees), the liquid film failed to cover the first-row tube surface. Increasing the feed film Reynolds number enhanced the liquid film distribution over the tubes and the dry spot decreased, which enhanced the heat transfer performance. At relatively higher contact angles of 30 degrees and 60 degrees (but still hydrophilic nature), the wetted area decreased and dry spots covered most of the second- and third-row tubes, which significantly influenced the thermal performance. Validation of the CFD model based on the volume-of-fluid approach was achieved by comparison with the experimental data, and the experimentally measured values of local heat transfer coefficient were employed for the comparison to support the validity of the present study.
引用
收藏
页数:12
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