Modeling of the flow patterns and heat transfer in a turbulent bubbly polydispersed flow downstream of a sudden pipe expansion

被引:21
作者
Pakhomov, M. A. [1 ]
Terekhov, V. I. [1 ]
机构
[1] Russian Acad Sci, Kutateladze Inst Thermophys, Lab Thermal & Gas Dynam, Siberian Branch, Acad Lavrentev Ave 1, Novosibirsk 630090, Russia
基金
俄罗斯科学基金会; 俄罗斯基础研究基金会;
关键词
Polydispersed bubbly flow; Pipe sudden expansion; Heat transfer; Flow structure; Break up and coalescence; INTERFACIAL AREA TRANSPORT; 2-PHASE FLOW; BREAK-UP; PHASE DISTRIBUTION; PRESSURE CHANGE; COALESCENCE; MASS; SIMULATION; STRESS; SHAPE;
D O I
10.1016/j.ijheatmasstransfer.2016.05.054
中图分类号
O414.1 [热力学];
学科分类号
摘要
Results from the numerical simulation of the structure and heat transfer in polydispersed bubbly turbulent flow, downstream of a sudden pipe expansion, are presented. The structure of the mean and fluctuating two-phase bubbly flow at small values of volumetric gas flow rate ratio, beta <= 10%, is qualitatively similar to that of a single-phase fluid flow. Small bubbles are present in almost the entire pipe section, whereas large ones mostly move just through the flow core and shear mixing layer. An increase in the dispersed phase size causes the production of extra turbulence in the liquid phase (up to 30%). The addition of air bubbles results in a significant reduction in the length of the separation region (up to 50%) and a significant increase in the heat transfer rate (up to 100%). These effects are augmented by increasing bubble size and concentration. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1251 / 1262
页数:12
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