Effect of surface wettability on flow characteristics in vertical upward gas-liquid two-phase flow

被引:0
作者
Fuculty of Marine Technology, Tokyo University of Marine Science and Technology, 2-1-6 Etchujima, Koto-ku, Tokyo, 135-8533, Japan [1 ]
机构
[1] Fuculty of Marine Technology, Tokyo University of Marine Science and Technology, Koto-ku, Tokyo, 135-8533
来源
Nihon Kikai Gakkai Ronbunshu, B | 2007年 / 7卷 / 1502-1509期
关键词
Contact angle; Flow patterns; Flow visualization; Gas-liquid two-phase flow; Pressure drop; Void fraction; Wettability;
D O I
10.1299/kikaib.73.1502
中图分类号
学科分类号
摘要
To evaluate the effect of pipe wall surface wettability on flow characteristics in a vertical upward gas-liqid two-phase flow, a visualization study was performed using three test pipes : an acrylic pipe, a hydrophilic pipe and a hydrophobic pipe. Such basic flow characteristics as flow patterns, pressure drop and void fraction were investigated in these three pipes. In the hydrophilic pipe, the slug flow to churn flow transition boundary was shifted to a higher gas velocity at a given liquid velocity, whereas the churn flow to annular flow transition boundary was shifted to a lower gas velocity at a given liquid velocity. In the hydrophobic pipe, an inverted churn flow regime was observed in the region where the churn flow regime was observed in the acrylic pipe, while a droplet flow regime was observed in the region where an annular flow regime was observed in the acrylic pipe. At a high gas flow rate, the mean void fraction in the hydrophobic pipe was higher than in the acrylic pipe. The effect of surface wettability on frictional pressure loss was confirmed to be insignificant under the present experimental conditions.
引用
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页码:1502 / 1509
页数:7
相关论文
共 14 条
[1]  
Bemardin J.D., Et al., Contact Angle Temperature Dependence for Water Droplets on Practical Aluminum Surfaces, Int. J. Heat Mass Transfer, 40, 5, pp. 1017-1033, (1997)
[2]  
Barajas A.M., Panton R.L., The Effiects Contact Angle on Two-phase Flow in Capillary Tube, Int. J. Multiphase Flow, 19, 2, pp. 337-346, (1993)
[3]  
lguchi M., Terauchi Y.M., Boundaries among Bubbly and Slug Flow Regimes in Air-water Two-phase Flows in Vertical Pipe of Poor Wettability, Int J. Multiphase Flow, 27, pp. 729-735, (2001)
[4]  
Iguchi M., Terauchi Y.M., Microgravity Effects on the Rising Velocity of Bubbles and Slugs in Vertical Pipes ofGood and Poor Wettability, Int. J. Multiphase Flow, 27, pp. 2189-2198, (2001)
[5]  
Ishii M., Jarlais G.D., Flow Regime Transition and Interfacial Characteristics of Inverted Annular Flow, Nucl. Engrg. Des, 95, pp. 171-184, (1986)
[6]  
Ishii M., Jarlais G.D., Flow Visualization Study of Inverted Amular Flow of Post Dryout Heat Transfer Region, Nucl. Engrg. Des, 99, pp. 187-199, (1987)
[7]  
Obot N.T., Ishii M., Two-phase Flow Flow Regime Transition Criteria in Post-dryout Region Based on Flow Visualization Experiments, Int. J. Heat Mass Transfer, 31, 12, pp. 2559-2570, (1988)
[8]  
Ishii M., Denten J.P., Two-phase Flow Characteristic of Inverted Bubbly, Slug and Annular Flow in Post-critical Heat Flux Region, Nucl. Engrg. Des, 121, pp. 349-366, (1990)
[9]  
Oshinowo T., Charles M.E., Vertical Two-phase Flow. Part 2. Holdup and Pressure Drop, Can J. Chem. Engrg, 56, (1974)
[10]  
Griffth P., Wallis G.B., Two-phase Slug Flow, Trans. ASME, J. Heat Transfer, 83 C, 3, pp. 307-320, (1961)