带亲水层波纹翅片管换热器析湿工况空气侧换热与压降关联式

为得到带亲水层波纹翅片的换热器在析湿工况下空气侧的换热和压降关联式,对7个带亲水层波纹翅片管换热器在23个工况下进行了试验研究。根据试验数据,运用多元线形回归方法拟合得到了带亲水层波纹翅片管换热器析湿工况下空气侧的换热和压降关联式。所拟合的换热和压降关联式平均误差分别为6.5%和9.1%,在±15%误差范围内分别能涵盖90.3%和79.2%的试验数据。将新开发的关联式与目前已有的4个换热与压降关联式进行了对比分析,结果表明新的关联式精度明显好于已有的关联式。     

微通道换热器结露工况下换热特性及其影响的 试验研究

微通道换热器因体积小、制冷剂充注量少、换热效率高等优点,已被广泛应用到汽车空调和空调系统的冷凝器,但作为蒸发器使用时,会因换热器表面空气结露而影响换热性能。以微通道换热器为研究对象,分析在结露条件下,不同的入口空气湿度、风速和微通道换热器布置倾角等参数对微通道换热器的出口空气温度、空气侧压降、换热量和换热系数的影响程度,研究发现:空气入口湿度对微通道换热器出口空气温度影响较大,相对湿度提高10%,出口温度约提高1.3℃;迎面风速对换热器空气侧压降影响很大,风速从1.5 m/s提高到3.0 m/s,压降增加一倍以上,风速大小为2.5 m/s时,换热器换热效果最佳;换热器倾角较入口相对湿度和迎面风速对微通道换热性能影响较小。     

微通道蒸发器高风速湿工况性能试验研究

为了研究微通道蒸发器在高风速湿工况下的热力性能和漂水特性，对不同翅片间距和表面特性的微通道换热器进行了试验研究。结果表明，亲水表面处理的微通道蒸发器不能改善湿工况热力性能和凝水排除效果，相反会恶化。亲水表面处理对换热因子j影响不显著，但使风侧阻力系数f增加。在测试工况条件下，亲水表面处理对换热因子j的影响小于1%，风阻系数增大4%～9%。j和f对翅片密度、空气湿度和风速的变化不敏感。亲水表面微通道换热器增大连续性水桥形成机会，增大漂水风险。常规工况下光箔和亲水箔均未发现漂水现象；高湿工况下光箔未发现漂水，亲水箔在风速4.5 m/s和较小翅片间距1.7 mm时，出现轻微漂水。     

湿热地区运行参数对波纹翅片管换热器性能的影响研究

鉴于波纹翅片管换热器热湿工况运行优化缺少指南,建立了某9排管空气-水逆流式波纹翅片管换热器的传热除湿数学模型,利用MATLAB编程开展仿真,试验验证了仿真结果之后,在广州和杭州2种湿热气候条件下,探究了水流速度、风速以及进口水温对换热器换热、除湿性能的影响规律.结果显示:风速对换热量影响最大,进口水温对除湿量影响最大;...     

车用百叶窗翅片管式换热器对空气侧强化传热作用的研究进展

百叶窗翅片管式换热器是车用换热器主要选型之一,其结构对空气侧强化传热作用有着极其重要的影响。本文总结了近几年来国内外在百叶窗翅片管式换热器的结构参数对空气侧强化传热影响方面的研究,包括翅片间距、管排数、翅片高度、百叶窗开窗角度、翅片厚度及翅片形状对空气侧换热系数、压降的影响。最后,在百叶窗结构的基础上,提出了在翅片上打孔形成百叶型多孔翅片来进一步强化空气侧换热的建议。     

析湿工况下开缝翅片管换热器空气侧热质比拟关系特性分析

对开缝翅片管换热器在析湿工况下空气侧热质比拟关系进行试验研究,分析翅片间距和入口相对湿度对空气侧热质比拟关系特性的影响.研究结果表明,随着翅片间距的增加,热质比拟关系值逐渐增大.当入口水温为12℃时,随着入口相对湿度的增加,热质比拟关系逐渐增加,而当入口水温为6℃时,入口相对湿度对热质比拟关系几乎没有什么影响.试验得到的热质比拟关系值的范围为0.5～3.7,刘易斯关系式对于开缝翅片管换热器不适用.利用多元线性回归的方法开发热质比拟关系hδ(hmcp,a)的关联式,所开发关联式在±15%误差范围内能涵盖87.3%的试验数据,平均误差为7.1%.此外,在数据处理过程中,提出一个新的参数--传质翅片效率,以此来求解空气侧的传质系数.     

低温工况下翅片管换热器结霜特性研究

介绍了低温工况下（＜－5℃）翅片管换热器霜层形成及其生长，研究了翅片管换热器本身特性（如翅片间距、翅片形状以及翅片表面状况等）对层生长速度、结霜量以及压降的影响，为低温工况下翅片管换热器结构参数的优化及表面状况的改善，提供了重要的依据。     

波纹翅片传热与流动特性数值仿真分析

采用数值计算方法,进行了波纹翅片传热与流动阻力特性的仿真研究。计算了波纹翅片上下表面换热系数沿着流动长度方向的变化特性;进行了波纹翅片无量纲曲率半径对换热系数、努塞尔数、管道压降、摩擦因子、管道进出口空气温差等的影响研究,绘制了波纹翅片换热性能评价图。研究结果表明,波纹翅片上下表面换热系数的大小沿着翅片长度方向呈现正弦形式波动,波动幅值逐渐较小;无量纲曲率半径的减小有利于提高波纹翅片的换热效果,但波纹翅片内空气流动的阻力也随之增大;换热性能评价图显示波纹翅片换热性能的增长率小于流动阻力的增长率。该研究内容为机车及动车组板翅式换热器空气翅片选型提供参考。     

正弦波纹翅片管换热器传热和阻力特性的试验研究

对不同翅片间距、不同管排数的9个正弦波纹翅片管换热器元件进行了试验研究,给出了工业常用雷诺数范围内各元件翅片侧空气的换热和阻力性能关联式。文中还给出了包括翅片间距及管排数影响的通用关联式,为设计和选用正弦波纹大套片换热器提供了依据。     

湿工况下翅片管换热器空气侧特性研究进展

概述了目前国内外对湿工况下各类翅片管式换热器空气侧特性的实验研究,通过对翅片管换热器湿工况空气侧特性的分析和介绍,提出了现有研究的不足。     

Impacts of fouling and cleaning on the performance of plate fin and spine fin heat exchangers

An experimental study was conducted to investigate the effects of air-side fouling and cleaning on the performances of various condenser coils used in unitary air-conditioning systems. A total of six condenser coils with different fin geometry and row number were tested. Performance tests were performed at three different conditions: clean-as-received, after fouling, and after cleaning. In all cases, it was observed that the fouling was mostly confined to the frontal face of the heat exchanger as reported in the previous investigations. The amount of deposited dust was more dependent on fin geometry for the single-row heat exchangers than for the double-row heat exchangers. The predominant effect of fouling was to cause a more significant increase in air-side pressure drop than a degradation in heat transfer performance. For the single-row heat exchangers, the pressure drop increased by 28 to 31%, while the heat transfer performance decreased by 7 to 12% at the standard air face velocity of 1.53 m/s depending on fin shape. For the double-row heat exchangers, the pressure drop increased by 22 to 37%, and heat transfer performance decreased by only 4-5% at the same air face velocity. Once the contaminated coils were cleaned according to the given cleaning procedure the original performance of the heat exchangers could almost be recovered completely. The pressure drop could be restored within 1 to 7% and the heat transfer performance could be recovered to within 1 to 5% of the originally clean heat exchangers. Therefore, it is concluded that a periodic application of the specified cleaning technique will be effective in maintaining the thermal performance of the condenser coils.     

散热器翅片结构对流体流动及换热过程影响的数值仿真研究

用CFD软件FLUENT对散热器常用的平翅片和波纹翅片表面的流体流动及换热过程进行了数值模拟,获得了翅片表面的流场、温度场、压力场以及换热量、换热系数的变化规律。模拟结果表明在相同气流量的条件下,波纹翅片的压力损失比平翅片的大,平均表面换热系数及换热量均比平翅片的高,翅片的形状结构对流场分布和强化换热效果的影响较大。     

Wet surface heat transfer and pressure drop of aluminum parallel flow heat exchangers at different inclination angles

The effect of inclination angle on the heat transfer and pressure drop characteristics of brazed aluminum heat exchangers was experimentally investigated under wet conditions. Three samples having different fin pitches (1.25, 1.5 and 2.0 mm) were tested. Results show that heat transfer coefficients are not affected by the inclination angle. However, friction factors increase as the inclination angle increases with negligible difference between the forward and backward inclination. The effect of fin pitch on the heat transfer coefficient and on the pressure drop is also discussed. Comparison of the dry and wet surface heat transfer coefficients reveals that dry surface heat transfer coefficients are significantly larger than wet surface heat transfer coefficients. Possible explanation is provided by considering the condensate drainage pattern. The data are also compared with the existing correlation. This paper was recommended for publication in revised form by Associate Editor Man-Yeong Ha Nae-Hyun Kim is a Professor of Mechanical Engineering, University of Incheon. His area of interest spans boiling and condensation, heat transfer enhancement and heat exchanger design. He has been active in heat transfer community, and was a Chairman of Thermal Engineering Division of KSME. He holds several editorial position including Journal of Enhanced Heat Transfer. He is a recipient of Asian Academic Award awarded by SAREK and JSRAE.     

横向管间距对开缝翅片管性能的影响及降噪方法的探讨

在分析窗式和分体式空调器特点的基础上,探讨两种家用空调器的优缺点。应用SIMPLE算法对空调用开缝翅片管表面的传热及流动阻力特性进行了三维数值模拟,研究了横向管间距对空调器换热和阻力性能的影响,在翅片间距和进口流量保持不变的情况下,计算了横向管间距从10.5mm变化到12.5mm等五种工况,得出随着横向管间距的增大,换热器两端压降减小,换热略有增加以及单位泵功换热量先增加然后减小的结论。计算结果表明,当横向管间距为11.97mm时单位泵功换热量最大。     

椭圆管开缝翅片换热表面特性的三维数值分析

研究了平片圆管表面,开缝片圆管和开缝片椭圆管表面的流动和换热特性。翅片表面的缝为辐射布置,下游布置较多的缝。椭圆管的长短轴之比为2.25,与圆管具有相同的周长。研究结果表明,两种开缝片的换热量远大于平片,椭圆管开缝片的压降低于圆管开缝表面。在泵功消耗减少2.5%时,椭圆管开缝的换热量比圆管开缝高7%。椭圆管虽不能改善温度梯度和速度场的协同,然而压降远低于圆管开缝片,使其具有较好的综合特性。     

Heat transfer and pressure drop amidst frost layer presence for the full geometry of fin-tube heat exchanger

The present study numerically solves the flow and thermal fields in the full geometry of heat exchanger modeling with frost layer presence on the heat exchanger surface. The effects of air inlet velocity, air inlet temperature, frost layer thickness, fin pitch, fin thickness, and heat exchanger shape on the thermo-hydraulic performance of a fin-tube heat exchanger are investigated. Heat transfer rate rises with increasing air inlet velocity and temperature, and decreasing frost layer thickness and fin pitch. Pressure drop rises with increasing air inlet velocity and frost layer thickness, and decreasing fin pitch. The effect of fin thickness on heat transfer and pressure drop is negligible. Based on the present results, we derived the correlations, which express pressure drop and temperature difference between air inlet and outlet as a function of air inlet velocity and temperature, as well as frost layer thickness.     

板翅式换热器中新型微凸翅片结构设计及性能分析

为提高翅片区域的换热效率、改善板翅式换热器的整体换热性能,提出了一种新型微凸翅片结构。基于结构参数多采样点处的热力学性能仿真结果构建近似模型,以翅片热功率最高为优化目标、压降为约束,使用序列二次规划法确定了微凸体结构参数（微凸高度、微凸夹角、微凸开口长度）的最优值;对微凸体排列间距、排列方式进行优化,确定了改进微凸翅片结构的具体参数值。通过对翅片流道内温度场、压力场分析,以及与相同尺寸的平直翅片的换热性能对比,验证了所提出的新型微凸翅片结构的有效性。     

CFD analysis of fin tube heat exchanger with a pair of delta winglet vortex generators

Among tubular heat exchangers, fin-tube types are the most widely used in refrigeration and air-conditioning equipment. Efforts to enhance the performance of these heat exchangers included variations in the fin shape from a plain fin to a slit and louver type. In the context of heat transfer augmentation, the performance of vortex generators has also been investigated. Delta winglet vortex generators have recently attracted research interest, partly due to experimental data showing that their addition to fin-tube heat exchangers considerably reduces pressure loss at heat transfer capacity of nearly the same level. The efficiency of the delta winglet vortex generators widely varies depending on their size and shape, as well as the locations where they are implemented. In this paper, the flow field around delta winglet vortex generators in a common flow up arrangement was analyzed in terms of flow characteristics and heat transfer using computational fluid dynamics methods. Flow mixing due to vortices and delayed separation due to acceleration influence the overall fin performance. The fin with delta winglet vortex generators exhibited a pressure loss lower than that of a plain fin, and the heat transfer performance was enhanced at high air velocity or Reynolds number.