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旋流强度对气/雾两相传热传质的影响
引用本文:王小川,贺国,郭朝有,李雁飞.旋流强度对气/雾两相传热传质的影响[J].上海交通大学学报,2013,47(11):1767-1772.
作者姓名:王小川  贺国  郭朝有  李雁飞
作者单位:(海军工程大学 a.热科学与动力工程研究室;b.动力工程学院;c.管理工程系, 武汉 430033)
基金项目:国防预研基金(101050202);海军工程大学自然科学基金(HGDQNJJ12010)资助项目
摘    要:为进一步提高发动机排气集水箱对高温烟气的降温性能,研究了旋流强度对高温烟气与冷却水雾两相流传热传质的影响.利用欧拉 拉格朗日方法和离散相模型对集水箱内横流喷雾冷却过程进行了三维数值模拟.对排气集水箱涡流室某一截面处的气流旋流数进行了理论推导,并将得到的旋流数解析解与数值解进行了比较.结果表明:集水箱涡流室内的旋流是强旋流动,理论解析解与数值解基本吻合;在集水箱排气室形成了一道“屏障”,在其上游区域内雾滴的有效运动行程比其下游区域内雾滴的有效运动行程长;提高烟气旋流强度,可增强两相掺混,延长液滴有效运动行程和蒸发时间;应使水雾雾滴进入烟气流场的初始位置位于“屏障”上游区域,以提高喷雾冷却效果.

关 键 词:传热传质    两相流    喷雾冷却    旋流数    集水箱  
收稿时间:2013-03-04

Effect of Swirl Intensity on Heat and Mass Transfer in Gas-Droplets Two-Phase Flow
WANG Xiao-chuan;HE Guo;GUO Chao-you;LI Yan-fei.Effect of Swirl Intensity on Heat and Mass Transfer in Gas-Droplets Two-Phase Flow[J].Journal of Shanghai Jiaotong University,2013,47(11):1767-1772.
Authors:WANG Xiao-chuan;HE Guo;GUO Chao-you;LI Yan-fei
Institution:(a. Institute of Thermal Science and Power Engineerin; b. College of Power Engineering; c. Department of Management Science, Naval University of Engineering, Wuhan 430033, China)
Abstract:In order to further improve the cooling performance of a water-collecting box (WCB) for the high temperature exhaust gas in an engine exhaust system, a numerical simulation was performed to explore the effect of swirl intensity on the heat and mass transfer between the hot exhaust gas and the water droplets. The Eulerian-Lagrangian method and the discrete phase model were used in the three-dimensional simulation of the cross-flow spray cooling in the WCB. The swirl number was theoretically derived at a certain section of the vortex chamber in the WCB. The analytical swirl number was obtained using an analytical formula and was compared with the numerical solution. The results indicate that the swirling flow in the vortex chamber is strong and that the analytical swirl number agrees well with the numerical solution. A “barrier” is formed in the exhaust chamber, and the effective motion distance of the water droplets in the upstream zone of the “barrier” are longer than that of the droplets in the downstream zone. Raising the swirl intensity of gas flow will enhance the mix of two phases, and the effective motion distances and the evaporating time of the droplets will be prolonged. In order to enhance the spray cooling effect, the initial location where the water droplets enter the gas stream should be in the upstream zone of the “barrier”.
Keywords:heat and mass transfer  two-phase flow  spray cooling  swirl number  water-collecting box  
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