山东大学学报(工学版)
山東大學學報(工學版)
산동대학학보(공학판)
JOURNAL OF SHANDONG UNIVERSITY(ENGINEERING SCIENCE)
2013年
5期
104-110
,共7页
翼片%纵向涡%圆管%层流%强化传热
翼片%縱嚮渦%圓管%層流%彊化傳熱
익편%종향와%원관%층류%강화전열
winglet%longitudinal vortex%tube%laminar flow%heat transfer enhancement
利用三维数值模拟,分析了圆管内添加翼片后流体的流动结构和对流传热特性。模拟中,翼片与壁面呈45°倾斜放置,选取包含1个翼片的1/6通道进行研究。结果表明,翼片可在下游诱导产生2个旋转方向相反的纵向涡,形成对称的涡偶,涡偶外侧为背壁流,内侧为向壁流。纵向涡结构提高了流体在径向上的速度波动,在翼片下游靠近管壁处,最大速度可达到主流平均速度的80%,增强了对速度边界层的扰动。流场的改善使通道内的温度场分布更加均匀,与光滑通道相比,壁面附近的温度梯度可提高接近1个数量级。流体对壁面的冲刷作用使对流传热得到强化,相对于光滑通道,壁面局部Nu数可提高近50倍。纵向涡对通道内流体的强化传热作用随Re的增加而显著提高。
利用三維數值模擬,分析瞭圓管內添加翼片後流體的流動結構和對流傳熱特性。模擬中,翼片與壁麵呈45°傾斜放置,選取包含1箇翼片的1/6通道進行研究。結果錶明,翼片可在下遊誘導產生2箇鏇轉方嚮相反的縱嚮渦,形成對稱的渦偶,渦偶外側為揹壁流,內側為嚮壁流。縱嚮渦結構提高瞭流體在徑嚮上的速度波動,在翼片下遊靠近管壁處,最大速度可達到主流平均速度的80%,增彊瞭對速度邊界層的擾動。流場的改善使通道內的溫度場分佈更加均勻,與光滑通道相比,壁麵附近的溫度梯度可提高接近1箇數量級。流體對壁麵的遲刷作用使對流傳熱得到彊化,相對于光滑通道,壁麵跼部Nu數可提高近50倍。縱嚮渦對通道內流體的彊化傳熱作用隨Re的增加而顯著提高。
이용삼유수치모의,분석료원관내첨가익편후류체적류동결구화대류전열특성。모의중,익편여벽면정45°경사방치,선취포함1개익편적1/6통도진행연구。결과표명,익편가재하유유도산생2개선전방향상반적종향와,형성대칭적와우,와우외측위배벽류,내측위향벽류。종향와결구제고료류체재경향상적속도파동,재익편하유고근관벽처,최대속도가체도주류평균속도적80%,증강료대속도변계층적우동。류장적개선사통도내적온도장분포경가균균,여광활통도상비,벽면부근적온도제도가제고접근1개수량급。류체대벽면적충쇄작용사대류전열득도강화,상대우광활통도,벽면국부Nu수가제고근50배。종향와대통도내류체적강화전열작용수Re적증가이현저제고。
3-D numerical simulations were presented for studying the flow structures and convective heat transfer charac-teristics in a cylinder tube embedded with wing-finned vortex generators.In the numerical simulation, the winglet was upstream placed at an angle of 45 to the tube wall and 1/6 of channel was selected for studying due to symmetry.The results showed that two counter-rotating longitudinal vortices were induced downstream the winglet, forming a symmet-ric vortex pair.The flow inner vortex pair was towards the wall while the flow outer vortex pair was backwards the wall.The longitudinal vortex could improve the magnitude of velocity in the radial direction, and the maximum value in near wall region reached 80% of the average mainstream velocity downstream the winglet.As a result, the winglet booted the disturbance of the velocity boundary layer.The improved velocity field could make the temperature field in the tube more uniform.Compared with the smooth tube, the temperature gradient near the wall could improve approxi-mately an order of magnitude.The flow induced by the longitudinal vortex rushed to the wall, which strengthened the convective heat transfer significantly.The maximum value of the local Nu on the wall surface could reach 50 times of the smooth tube.The improved convective heat transfer performance lead by longitudinal vortex enhanced with the Reynolds numbers increasing.