Investigations of the spreading of falling liquid films in inclined tubes

被引:14
作者
Eichinger, S. [1 ]
Storch, T. [1 ]
Grab, T. [1 ]
Fieback, T. [1 ]
Gross, U. [1 ]
机构
[1] TU Bergakad Freiberg, Chair Tech Thermodynam, D-09596 Freiberg, Germany
关键词
Falling film evaporation; Structured surface; Film breakup; Wetting behaviour; Inclined surface; Capillary transport; HIGH REYNOLDS-NUMBERS; HEAT-TRANSFER; VERTICAL TUBE; REFLUX CONDENSATION; SHEAR-STRESS; FLAT-PLATE; BREAK-UP; EVAPORATION; SURFACES; FLOW;
D O I
10.1016/j.ijheatmasstransfer.2017.11.142
中图分类号
O414.1 [热力学];
学科分类号
摘要
Starting with an extensive literature review, in this study investigations of the film spreading of falling films inside smooth and structured tubes are presented in dependence of the tube inclination angle (beta = 0 degrees til 20 from the vertical), mass flow rate and fluid temperature (263.15-293.15 K). Experiments are conducted at isothermal conditions and at partly film evaporation as well. The liquid film is observed visually with a camera which can be moved along the total flow length of the liquid without essential disturbance of the liquid respectively gas flow. The liquid used for the investigations is propane (Pr approximate to 3, Ka approximate to 20 . 10(10), Re-smooth tube = 20-950). The experiments reveal that the investigated helically structuring of the internal tube surface leads to an improvement of film spreading even for inclination angles up to beta = 20 degrees. Preliminary tests in an open air-water system clearly showed that the groove structure geometry has an influence on initial wetting and film spreading. Further, the results of the calculated capillary transport from two theoretical approaches are compared and adapted to each other. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:586 / 600
页数:15
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