矩形微槽道饱和沸腾临界热流密度特性

对矩形微槽中的流动沸腾临界热流密度进行了实验研究。研究CHF随质量流速、进口过冷度和出口干度的增加而出现的变化趋势,以及槽道尺寸对CHF的影响。搭建试验平台,在不同槽道当量直径、较大范围的质量流速和不同进口过冷度条件下,获得以去离子水为工质两相沸腾传热的实验数据。由于常规尺寸槽道CHF预测关联式并不具有普遍性,所以提出了一个适用于微槽道饱和沸腾CHF的预测模型。并通过与该文以及参考文献中实验数据进行对比,验证了该模型的适用性。     

竖直微槽道内EHD强化饱和沸腾传热研究

针对微槽内饱和沸腾汽泡建立了简化模型,并利用COMSOL Mu ltiphysics软件对电场中汽泡动力学特性进行了数值模拟,分析了微槽道内EHD(electrohydro dynam ics)强化沸腾传热机理。实验以去离子水为工质,研究了外加直流电场下两种规格的矩形微细槽道内饱和沸腾传热强化特性,电压在0~28kV内,EHD技术对微细槽道内的饱和沸腾传热有明显的强化效果。     

微槽道纳米流体饱和沸腾CHF特性研究

以水和三种不同质量分数(0.2%、0.5%和1.0%)的Al2O3纳米流体作为实验工质,在三种不同尺寸微槽道中进行饱和沸腾传热实验,研究沸腾传热过程中临界热流密度(Critical Heat Flux,简称CHF)的变化特性。主要分析了微通道水力半径、纳米流体浓度、进口过冷度和临界热力学干度等因素对CHF的影响。实验结果发现:在水力半径较小的槽道内CHF发生得比较早;CHF随纳米流体浓度的增大而增大;CHF随进口过冷度增大有细微增大的趋势;CHF随临界热力学干度的增大而减小。文中还将实验结果与现有的、工况条件与本实验相近的理论模型进行了拟合比较,发现理论模型能较好预测本实验。     

微槽道中纳米流体沸腾换热特性研究

为研究纳米流体在微槽道中的沸腾换热特性及规律,分别以去离子水和体积浓度为0.2%、0.5%的水基Al2O3纳米流体为工质进行试验,研究质量流速、热流密度、进口过冷度、槽道尺寸等因素对沸腾传热系数的影响及其两相摩擦压降与出口干度的关联分析和沸腾换热关联式对比拟合.试验结果表明:在一定热流密度和质量流速下,传热系数随槽道尺...     

微针肋槽道内去离子水换热特性

设计了槽肋比为1:2和2:1的矩形大长宽比微针肋散热器,并实验研究了去离子水在其内的流动换热性能。结果表明：当进口温度为40 ℃、微针肋槽道在雷诺数小于650、最高壁面温度低于77 ℃时,单位面积散热量可达21.32 W/cm²。当雷诺数一定时,同一个槽道壁面温度沿着流动方向不断增加、同一个位置壁面温度随着加热功率的增加而增大,局部努谢尔数沿着流动方向先减小后逐渐增加并趋于定值。当针肋流动换热长度较长时,其入口效应可以忽略,槽道平均努谢尔数随着雷诺数的增大而增大,与加热功率无关;为了更好地表达微针肋槽道内的换热特性,考虑了槽肋比、流动雷诺数等影响,拟合了去离子水在微针肋槽道内的对流换热关系式。     

矩形微槽道纳米流体饱和沸腾临界热流密度特性

针对纳米流体在微小尺度传热领域的应用,在常压下对微槽道中纳米流体的流动沸腾临界热流密度进行实验研究。分别以体积浓度为0.2%、0.5%的水基Al2O3纳米流体为工质进行试验,研究不同质量流速、槽道尺寸以及体积浓度等因素对沸腾CHF的影响。对比水为工质实验结果,表明:槽道尺寸、质量流速对于水-Al2O3纳米流体和纯水的CHF影响一致。其它参数一定的工况下,纳米流体CHF比纯水大,且随着纳米流体体积浓度增大,出口壁面过热度会增大。最后介绍一个微槽道沸腾CHF的预测模型,在评价其不足的基础上提出一个关于CHF的预测公式,与实验数据进行对比,验证该公式的适用性。     

沸腾换热及临界热流的动态微液层模型

对于水平面上的池内饱和沸腾传热机理,本文提出了一种新的微液层理论模型。与以前的理论模型不同的是,微液层模型给出了传热面上气-液-固接触的动态构造。饱和沸腾换热的主要机理在于动态微液膜的蒸发并与单个气泡的动力学过程密切相关。该模型能很好地预测充分发展的核沸腾换热曲线。由沸腾曲线上的极大值而很自然地导出临界热负荷。理论计算结果和已有的实验的结果相当吻合。     

放射状槽道与毛细芯复合表面池沸腾换热研究

本文将“米”字形放射状槽道强化面积大、气泡脱离阻力小与毛细芯成核位点多等优点相结合,设计加工出一系列铜基放射状槽道与烧结毛细芯耦合散热表面,在10 K、20 K和30 K三个不同过冷度下进行了HFE-7100池沸腾换热实验,得到不同表面在不同过冷度条件下的沸腾换热性能。结果表明,槽深对换热影响较大,耦合毛细芯的铜基散热结构可以进一步提高临界热流密度和换热系数。最大临界热流密度和换热系数分别可达130.1 W/cm²和0.94 W/(cm²·K),并对实验过程中的气泡动力学行为进行了分析。     

具有微槽的圆管流动沸腾实验研究

1引言行化行业大量的立、卧式重沸器等中都涉及沸腾相变传热。超大规模集成电路的正常工作需要具有10’W／m’量级甚至更高的散热能力山，航天热环境控制也同样要求在小温差下具有极高的散热强度问。对于这些高热流、低温差传热问题，往往也采用沸腾相变的方法解决。沸腾强化技术研究有很长历史，已发展出许多有效的方法，Thome问对过去数十年的工作做了系统的综述。具有烧结多孔表面薄展的HIGHFLUX管则，机加工扩展表面的THERMOEXEC－E管问，西德研制的GEWA－T管问，虽然在强化池沸腾时具有优异性能，很少用于强化流动沸腾。在…     

微液层模型预测过冷沸腾的临界热流密度

本文利用微液层模型对过冷沸腾的临界热流密度（CHF）进行了理论预测。过冷沸腾的强化换热主要是通过单个气泡的形成和消失造成的对流换热强化而引起的。对等热流面,CHF在高过冷区趋近于常数;对等温面,CHF随过冷度的增加而增加。过冷度增加时,蒸发换热量减少,总热流密度主要由蒸发区外的导热引起。     

Dependence of the critical heat flux at boiling on the coolant physical properties

It has been experimentally proved that heat transfer at boiling appears to be the problem with the conjugated boundary conditions. Heat transfer and critical heat fluxes at boiling depend both on physical properties of the boiling liquid and on the number of characteristics of the heat transferring wall. Various experimental data of the problem of boiling liquid with various physical properties have been analysed. To eliminate or minimize influence of the properties of the cooled wall on the value of critical heat transfer, the data obtained at boiling on the thick cooled wall only from the stainless steel or nichrome are considered. To eliminate effect of capillary forces specific linear size of heat transferring wall satisfied the condition ≥ 2.0.     

Accurate prediction of the critical heat flux for pool boiling on the heater substrate

While the influence of liquid qualities, surface morphology, and operating circumstances on critical heat flux (CHF) in pool boiling has been extensively studied, the effect of the heater substrate has not. Based on the force balance analysis, a theoretical model has been developed to accurately predict the CHF in pool boiling on a heater substrate. An analytical expression for the CHF of a heater substrate is obtained in terms of the surface thermophysical property. It is indicated that the ratio of thermal conductivity (k) to the product of density (ρ) and specific heat (c_p) is an essential substrate property that influences the CHF. By modifying the well-known force-balance-based CHF model (Kandlikar model), the thermal characteristics of the substrate are taken into consideration. The bias of predicted CHF values are within 5% compared with the experimental results.     

Experimental and numerical study of swirling subcooled flow boiling of water in a vertical annulus

In this paper, the effect of making swirling flow inside an annulus on the subcooled boiling heat transfer has been studied and discussed both experimentally and numerically. The Eulerian-Eulerian model and control volume technique have been used for numerical modeling of the problem. The experimental results show that the critical heat flux values are enhanced by making swirling flow. The experimental and numerical results also indicate that by making swirling flow inside the annulus, the subcooled boiling heat transfer coefficients are increased. Moreover, the experimental and numerical values of the boiling heat transfer coefficients show good agreement with each other.     

EHD强化微槽道两相流传热动力学研究

以去离子水为工质,对当量直径分别为1.33mm和2mm的竖直矩形微槽道进行了EHD两相流饱和沸腾传热实验研究,运用分维数、关联维数和Kolmogorov熵对槽道进出口压差波动信号进行了动力学研究,分析了槽道尺寸和外加高压电场对传热系数和非线性特征量的影响规律,结果表明:有无电场情况下,各系统均具有非线性混沌特性,并且有外加高压电场系统的混沌程度比无外加高压电场系统的混沌程度更强烈,槽道尺寸越小,系统的混沌程度越强烈,混沌程度越强烈的系统对应的传热系数越大。     

Enhancement in nucleate pool boiling heat transfer on nano-second laser processed copper surfaces

ABSTRACT

The present paper reports the experimental investigation of pool boiling heat transfer on multiscale functionalized copper surfaces. Multiscale functionalized surfaces are fabricated by employing the nano-second laser surface process (NLSP) technique. The heat transfer coefficients (HTCs) of functionalized surfaces are estimated experimentally by using water and acetone as pool liquid. Tests are performed at atmospheric pressure, and saturated pool boiling condition with heat flux varyies between 0 and 330 kW/m². The maximum HTCs for functionalized surface and reference polished surface were found to be 41,500 W/m²K and 23,000 W/m²K, respectively, with water and 22,000 W/m²K and 14,000 W/m²K, respectively, with acetone.     

Critical heat flux enhancement of pool boiling using a porous nanostructured coating

Surface coating techniques are commonly used to increase heat transfer and control critical heat flux. In this research, we used anodizing—an electrochemical coating process—to coat an aluminum oxide layer on the aluminum plain surface. This porous nanostructured coating has uniform, cylindrical, parallel nanochannels, and closed end pores. Next, we conducted saturated pool boiling tests on the anodized samples, using deionized water and the CHFs were measured. We found that porous nanostructured coatings, due to their improved surface characteristics, particularly wettability, increased CHF values and also critical heat flux increased linearly with decreasing the contact angle.     

池沸腾传热的数学分析

在统计方法的基础上,对于池沸腾换热的传热机理提出了一个数学模型. 在没有增加新的经验常数的条件下,从该模型中可得到池沸腾热流密度是壁面过热度、活化穴最小与最大尺寸、流体的接触角与流体物理特性的函数. 该模型可以较好地解释润湿性如何影响沸腾热流密度. 对不同的接触角,模型预测的结果与实验相符合. 关键词： 池沸腾 传热 数学模型     

Experimental investigation of heat transfer from different pin fin in a rectangular channel

In this study, the effect of both hexagonal pin fins (HPFs) and cylindrical pin fins (CPFs) into the rectangular channel on heat transfer augmentation, Nusselt number and friction factor were experimentally investigated. In planning of the experiments, different Reynolds number, pin fin array, pin fin geometry and the ratio of the distance between pin fin spacing (s) to the pin fin hydraulic diameter (s/D_h) were chosen as the design parameters. Air was used as the fluid. The Reynolds number, based on the channel hydraulic diameter of the rectangular channel, was varied from 3188 to 19531. In the experiments, the heating plate was made of stainless steel foil. The foil was electrically heated by means of a high current DC power supply to provide a constantly heated flux surface. The heat transfer results were obtained using the infrared thermal imaging technique. The heat transfer results of the hexagonal pin fins (HPFs) and cylindrical pin fins (CPFs) are compared with those of a smooth plate. Best heat transfer performance was obtained with the hexagonal pin fins. The maximum thermal performance factor ((?), was obtained as Re = 3188, staggered array, s/D_h = 0, ? = 2.28.