螺旋片强化的套管式换热器壳侧传热特性Heat Transfer Performance of the Shell Side of Double-Pipe Heat Exchanger Enhanced with Helical Fins
张丽,田密密,吴剑华
摘要(Abstract):
为揭示螺旋片强化套管式换热器壳侧传热的机理,以指导此类换热器的进一步强化,对螺旋片强化的套管式换热器壳侧的传热和阻力特性进行了实验研究,并与光滑内管换热器进行了比较;利用可实现的k-ε湍流模型,对螺旋片强化的套管式换热器壳侧流体的流动和传热特性进行了数值模拟,研究了正交螺旋坐标系下壳侧螺旋通道中的流场结构。实验结果表明,螺旋片能显著提高套管式换热器壳侧的传热性能;在Re为4000~14000,螺旋升角分别为45°、37°、27°、14°的换热器的传热系数是光滑内管换热器的1.3~4.2倍;螺旋升角越小的换热器传热效果越好,但压降也越大。数值模拟结果表明,螺旋片能改变壳侧流场结构,使流场中产生了二次流动,从而强化了传热;螺旋升角越大,螺旋通道中心处的二次流动越弱。因此,对于螺旋升角较大的换热器,采用螺旋片复合其它强化技术改善螺旋通道中心处的二次流动状况是进一步提高其传热性能的关键。
关键词(KeyWords): 螺旋片;套管式换热器;强化传热;螺旋升角;二次流动
基金项目(Foundation): 中央支持地方高校发展专项资金项目(2050205);; 辽宁省高校创新团队项目(2007T143)
作者(Author): 张丽,田密密,吴剑华
参考文献(References):
- [1]GAO Xue-nong(高学农),HUANG Yu-you(黄玉优),CHEN Shu(陈姝).Heat transfer and fluid flow performance of air flowing through the helical channel outside a vertical petal-shaped fin tube(立式花瓣管外空气螺旋流动传热及流阻性能研究)[J].J Chem Eng of Chinese Univ(高校化学工程学报),2006,20(4):653-656.
- [2]DENG Xian-he(邓先和),WANG Shi-ping(王世平),LIN Pei-sen(林培森),et al.Effect of the fin shape of transversal outside finned tube on heat transfer of longitudinal flow(管外周向低翅片翅形对纵向流传热性能的影响)[J].J Chem Eng of Chinese Univ(高校化学工程学报),1995,9(4):387-391.
- [3]SU Xin(苏欣),MENG Ji-an(孟继安),CHENG Xin-guang(程新广),et al.Optimal velocity field for laminar convection heat transfer in a cylinder and its application in engineering(圆筒内层流对流换热的最佳速度场与工程应用)[J].J Tsinghua Univ(Sci&Tech)(清华大学学报(自然科学版)),2005,45(5):677-680.
- [4]SU Xin(苏欣),CHENG Xin-guang(程新广),MENG Ji-an(孟继安),et al.Verification and characteristics of laminar field coordination equation(层流场协同方程的验证及其性质)[J].Journal of Engineering Thermophysics(工程热物理学报),2005,26(2):289-291.
- [5]FAN Hong-ming(樊洪明),HE Zhong-yi(何钟怡),WANG Xiao-hua(王小华).Large eddy simulation of a curved duct flow(弯曲管段内流动的大涡模拟)[J].Joural of Hydrodynamics Ser.A(水动力学研究与进展A辑),2001,16(1):78-83.
- [6]Jacobi A M,Shah R K.Heat transfer surface enhancement through the use of longitudinal vortices:a review of recent progress[J].Experiment Thermal and Fluid Science,1995,11(3):295-309.
- [7]Fiebig M.Vortices generators and heat transfer[J].Trans ICHemE,1998,76(2):108-172.
- [8]Yilmaz M,Comakli O,Yapici S.Enhancement of heat transfer by turbulent decaying swirl flow[J].Energy Conversion and Management,1999,40(13):1365-1376.
- [9]GAO Xiang(高翔),LUO Zhong-yang(骆仲泱),ZHOU Jin-song(周劲松),et al.Study on heat transfer enhancement characteristics with a decaying swirl flow(衰减性旋流强化传热性能的研究)[J].Proceedings of the CSEE(中国电机工程学报),2003,23(5):184-188.
- [10]Bolinder C J,Sunden B.Numerical prediction of laminar flow and forced convective heat transfer in a helical square duct with a finite pitch[J].Int J Heat Mass Transfer,1996,139(15):3101-3115.
- [11]Chen H J,Zhang B Z,Zhang J S.Fluid flow in rotating helical squared ducts[J].Joural of Hydrodynamics Ser.B,2003,15(3):49-56.
- [12]Germano M.The Dean equations extended to a helical pipe flow[J].J Fluid Mech,1989,203:289-305.
- [13]Bolinder C J.Flow visualization and LDV measurements of laminar flow in a helical square ducts with finite pitch[J].Experimental Thermal and Fluid Science,1995,11(4):348-363.
- [14]YAO Yu-ying(姚玉英),CHEN Chang-gui(陈常贵),CHAI Cheng-jing(柴诚敬).The Principle of Chemical Engineering(化工原理上册)[M].Tianjing(天津):Tianjing University Press(天津大学出版社),1996.
- [15]Holman J P.Heat Transfer[M].9th ed.New York:McGraw-Hill Higher Education,2002.