雨滴型凹坑流道换热板流动换热性能与优化

基于WORKBENCH,研究了雨滴型凹坑流道换热板的流动换热性能,并对其进行多目标优化研究。以努塞尔数Nu,阻力系数f,综合传热性能η为目标函数,考察了凹坑的前缘半径R_1,后缘半径R_2,凹坑深度H_d,凹坑间距P等结构参数对雨滴型凹坑流道各优化目标的影响。结果表明:雨滴型凹坑流道内的流动分离和涡流碰撞增强了湍流强度,有效强化了传热,并且高传热区出现在凹坑后缘。雨滴型凹坑板的Nu是平板的1.9~4.5倍,阻力系数是平板的2.3~3.5倍,η可达1.42~3.04。凹坑深度H_d对Nu、f、η影响都比较显著,而凹坑间距P对这三者的影响都比较小,当3.5mmH_d4.5mm且25.0mmR_130.0mm时有较好的η。通过对雨滴型凹坑板在1 358≤R_e≤6 926的数据结果进行关联,得到了凹坑板流动换热的准则关系式。     

凹坑深度对透平叶片前缘换热的影响

涡轮叶片前缘由于受到燃气的冲击,热负荷较高,其冷却和换热情况极大的影响了燃机的性能,因此是涡轮叶片上最关键的传热区,在对涡轮进行传热设计和计算时必须对该区域予以考虑。设计冲击靶面,对凹坑结构进行冲击,建立模型,通过数值计算分析其冷却效果。通过对凹坑的温度场进行对比分析,给出凹坑深度的变化对冲击靶面换热的影响。对于带凹坑结构,通过凹坑深度分析叶片前缘换热效果,当凹坑深度不太大时,凹坑深度的增加会增强冲击靶面的换热;当凹坑深度增加得较大时,则会明显降低冲击靶面的换热。     

无反向流脉动条件下波纹管内流体传热及阻力特性研究

利用数值模拟与实验相结合的方法,在无反向流脉动条件下,分析脉动参数雷诺数Re、斯特劳哈尔数St及振动分率P对波纹管中流体的传热和阻力特性的影响。入口速度为脉动速度,入口温度设为300 K,出口设为自由出口,壁面采用恒温壁面,温度为350 K。研究表明：波纹管内流体处于层流状态时,随着Re的增大,传热强化幅度不断增大;流体处于湍流状态时,传热强化幅度随Re的增大而降低;随着St的增加,传热强化幅度增大;振动分率P对传热强化幅度的影响不明显;平均摩擦系数随着Re的增大而减小,随着振动分率P的增加而小幅度增大,在一个脉动周期内摩擦系数呈正弦规律变化,且随着St的增大发生明显变化,但平均值几乎不变。     

板式换热器性能的数值模拟

建立了人字形板式换热器冷热双流道的流体流动与传热计算模型,利用计算流体力学软件对5组不同速度工况下换热器内流体的流动和传热进行了数值模拟,分析了换热器流道内的速度场、温度场和压力场.结果表明:数值模拟得到的板式换热器进、出口温差和压降与试验测量值的误差均小于6%;换热器内流体的流动和传热存在明显的不均匀性,导致其进、出口的另一侧出现明显的传热"死区";换热器的总传热系数和流道阻力均随着流体流速的增大而增大.     

表面活性剂减阻流体湍流空间结构试验研究

本文应用PIV(Paticle Image Veloeimetry)和PDA(Phase Doppler Anemometry)在二维流道内对CTAC(Cetyltrimethyl Ammonium Chloride)减阻流体湍流流场进行试验研究,得到减阻流体湍流速度分布。研究表明：在完全减阻区内,减阻流体的减阻性能随雷诺数的增大而增大,在过渡减阻区内,减阻流体的摩擦系数则随着雷诺数的增大而逐渐回升,最终回到与溶剂相当的水平上;减阻流体的速度分布曲线在近壁面处与牛顿流体层状速度曲线趋近,但二者并不完全重合;在流道近壁面处,水湍流流动时所能观测到的强烈的旋涡波动在减阻流体中基本消失,与此同时,在此区域内减阻流体的速度轮廓线与流道几乎平行,且该平行轮廓线部分所占比例较牛顿流体湍流流动时相应部分要大很多,减阻流体的湍流强度受到了极大的抑制。     

C型混沌结构中传热强化的数值分析

随着对强化传热的广泛重视与研究,利用混沌对流来强化传热的新技术得到了关注.利用CFD软件Fluent对C型混沌结构内的流体流动与传热进行数值模拟,对比了C型混沌结构与普通平直结构在流体流动场、温度场分布和传热特性等细观信息,分析了C型混沌结构的强化传热性能及特点.分析结果表明,C型混沌结构使流体在较小速度下产生混沌对流,这种流态增加了流体的扰动与湍动,增大主流区或近壁处流动的混合,强化了流道内的传热,使流道横截面上的温度分布均匀化;混沌对流内的传热Nu数和Po数(即fRe值)不再象普通层流为一定值,而随Re数的增大而增大.     

波纹板式换热器传热与流动特性分析

通过数值模拟的方式,对一种用于低粘度流体的波纹板式换热器的传热特性和阻力性能进行分析,以控制变量法分析了流体速度对传热特性及阻力性能的影响;搭建了板式换热器测试平台,验证了数值模拟结果的正确性和可行性;用等速法拟合了Nu-Re与Eu-Re的相关准则式,并采用JF因子评价换热器综合性能。结果表明：模拟结果与实验结果相比误差在10%以内;当流体流速小于1.0 m/s时,换热器传热系数和压降随着流速的增大而增大,但综合换热性能逐渐变差,在此流速范围内,总传热系数随冷流体进口温度升高而增大。     

立管内椭球颗粒群强化传热特性模拟研究

为提高液固两相流传热效率，通过添加椭球形颗粒改善立式换热管内液固两相流分布，采用CFD-DEM数值模拟颗粒长径比β、颗粒进口体积分数α以及流体进口速度v与管内椭球形颗粒群传热的关系，并根据PEC指数评价颗粒强化传热能力。模拟结果表明：在1.5≤β≤2.5，2％≤α≤4％，1.0m/s≤v≤1.5m/s参数内，椭球形颗粒PEC指数总高于球形颗粒，即前者强化换热效果优于后者。     

板壳式换热器板片流动与传热性能的数值模拟

针对板壳式换热器的人字形板片建立了单流道物理模型,并利用数值模拟软件分析了其重要结构参数波纹夹角的变化引起的模型流场、速度场和温度场的变化情况,以及对其传热性能的影响。结果显示:换热板片波纹夹角的变化使得流体的流动状态发生了变化,随着波纹夹角的增大,流体的流态由十字交叉流逐渐转变为曲折流。随着波纹角度的增大,流体的扰动程度加强,湍流程度提高,与此同时,努塞尔数和传热因子增大,传热性能增强。模拟结果表明波纹夹角对板壳式换热器流动和传热性能具有较大的影响,可以成为板壳式换热器优化设计的一个重要方向。     

膜加湿器热质交换过程的理论分析

膜加湿器是保证质子交换膜燃料电池(PEMFC)正常高效运行的重要组成部分.以燃料电池的板式膜加湿器为研究对象,根据热质交换原理对膜加湿器的传热传质过程进行了理论计算,分析了空气质量流量、膜内加湿侧进口温度和膜内加湿侧进口湿度对传热传质过程的影响.在传热方面:当空气质量流量不同时,随着膜内加湿侧进口温度的变化,膜内的热流量变化趋势不一致;当膜内加湿侧进口相对湿度为95%时,随着空气质量流量的变化,膜内热流量变化不大.在传质方面:当加湿侧进口相对湿度不变时,膜中水传输速率随着空气质量流量的增大而减小;当空气质量流量不变时,膜中水传输速率随着加湿侧进口相对湿度的增大而增大.     

Numerical Simulation of Flow and Heat Transfer in a Dimpled Channel with a Fish-Scale Pit

A new dimple configuration (fish-scale pit) is proposed here. Numerical simulations of steady compressible flow were performed to determine the turbulent flow behavior and heat transfer capability in a dimpled channel with the fish-scale pit or spherical pit. The results show that the wall heat transfer coefficient of the surface with the fish-scale pit is higher than that with the spherical pit, and the surface with the fish-scale pit is better in terms of reducing friction drag. This indicates the prospective applications of surfaces with the fish-scale pits, which can enhance wall heat-transfer and reduce skin-friction drag.     

Heat Transfer and Fluid Flow on Dimpled Surface With Bleed Flow

This study investigates the effects of bleed flow on heat transfer and fluid flow on a dimpled surface in a rectangular channel. The heat transfer on a dimpled surface with bleed flow is compared with that on a dimpled surface without bleed flow. The height of the channel is 15.0 mm. The dimples are arrayed in staggered on the bottom surface of the channel with a pitch of 15.0 mm. The dimple depth is 3.75 mm and the dimple footprint diameter is 13.0 mm. The bleed hole is installed on the inner surface of the dimple and the diameter of the hole is 1.3 mm. The tests were conducted with varying Reynolds numbers from 1000 to 10,000 and 0.5% of total mass flow is flowing out through a bleed hole. A numerical method was employed to determine the detailed heat transfer coefficients. Commercial computational fluid dynamics software, ANSYS CFX 13.0, is adopted and the Shear Stress Transport model is set to turbulent model. As a result, the overall heat transfer rate on dimpled surface with bleed flow is 10–20% higher than that without bleed flow.     

Influence of the Reynolds number and the spherical dimple depth on turbulent heat transfer and hydraulic loss in a narrow channel

The paper presents detailed numerical study of heat transfer enhancement by a spherical dimple placed on a wall in a narrow channel. RANS approach with MSST model is applied to investigate the influence of the depth to diameter ratio Δ and the Reynolds number on the flow and heat transfer. Numerical model was successfully validated using LDV measurements, pressure loss data and LES results. Special attention is paid to identification of the flow topology at different Δ and Reynolds numbers. Contribution of different heat exchanger surface parts to the heat transfer enhancement is analyzed. Application of entropy production as a criterion of heat exchanger efficiency is discussed. Detailed information gained from the present computations can be used to get a deep insight into flow physics over dimpled surfaces and as a benchmark for validation of numerical and experimental methods.     

Cavity receiver thermal performance analysis based on total heat loss coefficient and efficiency factor

A cavity structure effectively decreases the heat loss of a receiver. This paper applies the widely used collector analysis method to derive the total heat loss coefficient and efficiency factor for a cavity receiver. Based on the derived factors, this paper investigates the effect of different parameters, such as absorber surface temperature and emissivity, on thermal performance. The absorber surface emissivity significantly affects the total heat loss coefficient at high temperatures. The effect of the absorber surface temperature on the total heat loss coefficient is significant, while the effect of the ambient temperature on the total heat loss coefficient can be ignored. The present results can help to determine the testing conditions for the cavity receiver by using molten salt as the heat transfer fluid.     

Enhancement of heat transfer in turbulent channel flow over dimpled surface

A systematic numerical investigation of heat transfer in turbulent channel flow over dimpled surface is conducted. Both symmetric (or spherical) and asymmetric dimple with different depth ratios (h/D) and skewness (Dx and Dz) are considered for a series of Reynolds numbers Re_2H (based on bulk velocity and full channel height) between 4000 and 6000 while Prandtl number Pr is fixed at 0.7. It is found that the optimum dimple configuration for enhancing heat transfer measured in terms of the volume goodness factor is obtained for the case of asymmetric dimple with a depth ratio of h/D = 15% and stream-wise skewness of Dx = 15%. The heat transfer capacity in terms of Nusselt number is significantly increased, while the associated pressure loss is kept almost to the same level as the symmetric dimple with the same depth ratio. The present study also suggests that the heat transfer enhancement is closely related to ejection with counter-rotating flow, intensified secondary flow and vortex structures at the downstream rim of asymmetric dimple. All these findings suggest that a carefully designed asymmetric dimpled surface presents a viable means of enhancing heat transfer compared to the symmetric dimple.     

球突翅片的传热流动特性及等效热阻数值分析

为了提高翅片管换热器的传热系数和减小压降,提出了一种球突型翅片,通过数值模拟研究其传热与流动性能,同时应用(火积)耗散理论对其传热的不可逆性进行分析。计算结果表明:与平片相比,其传热能提高26.21%～39.53%,而阻力系数仅提高16.62%～27.04%,同时综合性能增加16.54%～32.56%;这说明该翅片具有高传热系数低压降的特点,是一种性能优良的翅片。通过(火积)耗散分析可以看出:球突翅片的等效热阻减小,其传热的不可逆性减弱。     

Heat transfer analysis of plain and dimpled tubes with different spacings

Heat transfer enhancement by modifying the surface of tubes is commonly practiced throughout the world. Grooves, dimples, flutes or corrugations are placed inside and outside the surface of tubes and channels for enhancement. In this article, a novel method for heat transfer enhancement by varying the spacing between the tubes is reported. A comparison is made between the heat transfer performance of plain tubes and dimpled tubes at different spacings. For analysis, an experimental setup is fabricated and assembled. The flow is externally forced laminar flow of air over a hot tube maintained at constant temperature. Four different velocities of air 0.4, 0.6, 0.8, and 1.0 m/s are considered in this study. Tube surface temperature, heat transfer coefficient, heat transfer rate and Nusselt number are the parameters studied to analyze the thermal behavior of tubes at different spacings of 1.0, 1.5, 2.0, 2.5, 3.0, and 3.5 cm. From the experimental investigation it is found that, apart from heat transfer enhancement by providing dimples on the tube surfaces, there is an optimal spacing between the tubes after which no further improvement is obtained. In this study, 3.0 cm is found to be the optimal spacing for both plain and dimpled tubes. However, the percentage value of heat transfer enhancement is greater with optimal spacing and for all velocities of air in dimpled tubes.     

Experimental investigation of impingement heat transfer on a flat and dimpled plate with different crossflow schemes

A nine-by-nine jet array impinging on a flat and dimpled plate at Reynolds numbers from 15,000 to 35,000 has been studied by the transient liquid crystal method. The distance between the impingement plate and target plate is adjusted to be 3, 4 and 5 jet diameters. Three jet-induced crossflow schemes, referred as minimum, medium and maximum crossflow correspondingly, have been measured. The local air jet temperature is measured at several positions on the impingement plate to account for an appropriate reference temperature of the heat transfer coefficient. The heat transfer results of the dimpled plate are compared with those of the flat plate. The best heat transfer performance is obtained with the minimum crossflow and narrow jet-to-plate spacing no matter on a flat or dimpled plate. The presence of dimples on the target plate produce higher heat transfer coefficients than the flat plate for maximum and minimum crossflow.     

球形腔式太阳能吸热器性能的数值研究

利用蒙特卡洛光线追踪法分析了6种不同开口比(D/d)的球形腔式吸热器的光学性能,并以光学模拟所得壁面能流作为热分析的边界条件导入CFD软件中,运用CFD软件对6种不同开口比的球形腔式吸热器进行流固耦合传热计算,获得了球形腔式吸热器和内部流体的温度场分布。通过计算球形腔式吸热器的反射光损失、对流热损失和热辐射损失,得到聚光器/球形腔式吸热器系统的光热转化效率为81.9%～84.4%,球形腔式吸热器的最佳开口比1相似文献   

Compound heat transfer enhancement of a dimpled tube with a twisted tape swirl generator

Friction and compound heat transfer behaviors in a dimpled tube fitted with a twisted tape swirl generator are investigated experimentally using air as working fluid. The effects of the pitch and twist ratio on the average heat transfer coefficient and the pressure loss are determined in a circular tube with the fully developed flow for the Reynolds number in the range of 12,000 to 44,000. The experiments are performed using two dimpled tubes with different pitch ratios of dimpled surfaces (PR = 0.7 and 1.0) and three twisted tapes with three different twist ratios (y/w = 3, 5, and 7). Experiments using plain tube and dimpled tube acting alone are also carried out for comparison. The experimental results reveal that both heat transfer coefficient and friction factor in the dimpled tube fitted with the twisted tape, are higher than those in the dimple tube acting alone and plain tube. It is also found that the heat transfer coefficient and friction factor in the combined devices increase as the pitch ratio (PR) and twist ratio (y/w) decrease. In addition, an empirical correlation based on the experimental results of the present study is sufficiently accurate for prediction the heat transfer (Nu) and friction factor (f) behaviors.