自然循环加热段内对流传热特性的实验研究

本文以常压去离子水为工质,对自然循环工况下上升加热段内单相水的对流传热特性进行了实验研究。实验结果表明,自然循环工况下上升加热段内工质的物性变化及由浮升力引起的自由流动对对流传热特性有重要影响。通过分析,提出了计算自然循环工况下上升加热段内单相水的对流换热系数的经验关系式。     

声空化场下单相对流传热的实验研究

以水、乙醇和丙酮为工质，首次通过实验研究了声空化场的热效应、单相对流换热受空化时间．纳米颗粒和实验工质的影响及恒热流密度下单相对流换热系数随声空化强度的变化，并就其强化传热机理进行了分析。     

ZrO2纳米流体的对流换热系数测定及机理浅析

建立了测量圆管内纳米流体流动与传热性能的实验系统,测量了不同粒子浓度的ZrO2/水纳米流体在雷诺数为3 000～18 000范围内的管内对流换热系数以及不同位置处纳米流体对流换热系数的变化情况.实验结果显示,在液体中添加纳米粒子显著增大了液体的管内对流换热系数,例如,在相同雷诺数时,与纯水相比,如果纳米粒子的质量浓度从1.6%增大到4.1%,则纳米流体的对流换热系数增加的比例从1.09增大到1.2.此外,从颗粒的浓度、粒径两方面分析纳米流体强化传热的机理.     

外磁场作用下磁流体的对流换热特性

实验研究了外加磁场作用下水基磁流体的对流换热特性,分别测量了均匀磁场和梯度磁场条件下磁流体横掠加热细丝的对流换热系数,分析了外加磁场强度和方向对磁流体传热性能的影响.实验结果表明,外加磁场是影响磁流体对流换热的一个重要因素,应用外加磁场可以控制磁流体对流换热过程.     

底部局部加热多孔介质自然对流传热的格子Boltzmann模拟

运用格子Boltzmann方法研究了底部局部加热多孔介质方腔的自然对流传热.方腔的上壁面为低温热源,下壁面为局部高温热源,左右壁面为绝热条件.重点分析了高温热源位置a及尺寸b对多孔介质方腔自然对流传热性能的影响,提出了平均Nusselt数Nu和位置a及尺寸b的拟合关系式.研究结果表明:高温热源位置及尺寸对多孔介质方腔内自然对流传热性质的影响很大,且存在最佳高温热源位置(a=4/16)和尺寸(b=0.75),以达到最强的对流换热强度(Nu_(max)≈10.35)和最大的对流换热量(Q_(max)≈5.69).     

自然对流的LB方法模拟及其非线性特性

采用LB方法和QUICK差分方法模拟了方腔内竖直平板自然对流和底部加热方腔内自然对流换热问题.实现了LB方法对具有孤立体的封闭空间内耦合的流动和传热问题的数值模拟,所得数值结果与QUICK差分方法的数值结果及已有的烟可视化实验结果一致;两种方法对底部加热方腔内自然对流问题的预测结果均出现了静态分岔和动态分岔;根据底部加热方腔内自然对流换热数值结果给出的极限环型速度相图和功率谱表明,两种方法得到的数值结果的非线性特性一致.     

烧结金属纤维板大空间自然对流实验研究

实验研究了烧结金属纤维板在大空间下的自然对流换热,分析了倾角、孔隙率、纤维丝经、Ra数和金属纤维导热系数对换热性能的影响.实验结果表明:存在最优的角度(60°左右)使烧结金属纤维板的自然对流换热性能最好,但倾斜角度对烧结金属纤维板的换热影响没有光板显著;加热面的平均Nu数随着纤维直径和孔隙率的增加均先增加后减小;在实验...     

小温差喷雾碰壁蒸发过渡段换热特性分析

本文对小温差下水平面的喷雾碰壁蒸发传热特性进行了实验研究.通过对实验数据的分析发现,喷雾碰壁蒸发换热过程可分为三个阶段,即雾化工质单相冲击对流换热段、过渡换热段、充分沸腾换热段.在喷雾碰壁蒸发换热过程中,总的热流密度由单相冲击对流换热的热流密度和沸腾换热的热流密度两部分组成.据此,提出并改进了喷雾碰壁蒸发换热过程中过渡段换热系数的处理方法,将有利于对喷雾碰壁换热的进一步研究.     

斜翅型冷凝强化换热管传热性能的实验研究

对一种斜翅型外翅片带内螺纹的冷凝强化换热管进行传热性能的实验研究。管外冷凝换热的制冷剂为R134a,管内对流换热的介质为水。分别在定热流密度与定水流速的条件下进行一系列工况的实验,得到相应的实验数据。在定热流密度条件下,利用Wilson图解法得到管内的换热系数数据及相应的计算关联式。在定水流速的条件下,利用分离方法得到管外冷凝换热系数数据及相应的计算关联式。将强化管换热系数数据与光管换热系数的理论计算值进行了比较,结果表明:冷凝强化换热管管内对流换热的强化倍率为2.4,管外凝结换热系数随壁面过冷度的增加而增大,管外凝结换热的强化倍率为:1.78～3.92。     

流体在烧结多孔槽道中对流换热的实验研究

本文对空气和水流过烧结青铜颗粒水平多孔槽道表面上的对流换热进行了实验研究。结果表明:与空槽道表面换热相比,实验段充满烧结多孔介质后,水流过实验段的平均对流换热系数可提高7～9倍,空气可提高3～30倍;烧结多孔结构的强化换热能力大于非烧结的堆积床;直径的增大能提高水在多孔结构内的换热能力,但对空气而言在实验流量范围内无明显作用。     

小通道扁管内纳米流体流动与传热特性

建立了测量小通道扁管内纳米流体流动与对流换热性能的实验系统,测量了不同粒子体积份额的水-Cu纳米 流体的管内对流换热系数和摩擦阻力系数,实验结果表明,在相同雷诺数条件下,小通道扁管内纳米流体的对流换热系数 大于纯液体,且随粒子的体积份额的增加而增大,而纳米流体的阻力系数并未明显增大。     

Heat Transfer and Pressure Drop Characteristics of Graphene Oxide/Water Nanofluid in a Circular Tube Fitted with Wire Coil Insert

In this work, heat transfer and pressure drop characteristics of graphene oxide/water nanofluid flow through a circular tube having a wire coil insert were studied. The required graphene oxide was synthesized via the Hummer method and characterized using Fourier transform infrared spectroscopy (FTIR), X-ray diffraction (SRD), and scanning electron microscope (SEM) methods. Dispersing graphene oxide in the water, nanofluids with 0.02, 0.07, and 0.12% volume fraction were prepared. An experimental set-up was designed and made to investigate the heat transfer performance and pressure loss of nanofluids. All experiments were carried out in the constant heat flux at tube wall conditions. The volumetric flow rates of the nanofluid were adjusted at 6, 8, and 10 L/min. Thermal conductivity, specific heat, density, and viscosity as thermophysical properties of the nanofluid were calculated using graphene oxide and water properties at the average temperature via appropriate relations. These properties were applied to calculate the convective heat transfer coefficient, Nusselt number, and friction factors for each experiment. Finally, the constant and exponents of Duangthongsuk and Wongwises's correlations for Nusselt number and friction factor were corrected by experimental results. The achieved experimental data have shown good agreement with those predicted. The results have shown that 0.12 vol% of graphene oxide in the water can enhance convective heat transfer coefficient by about 77%. As a result, it can be concluded that the graphene oxide/water can be used in the heat transfer devices to achieve more efficiency.     

亚临界与超临界压力水在管内的对流传热与传质

本文对含有金属腐蚀物杂质的亚临界与超临界压力水在竖直加热圆管内的受迫对流与混合对流传热与传质进行了数值模拟，分析了变物性、浮升力以及压力等因素对管内对流传热与传质的影响。结果表明：浮升力使自下而上流过竖直加热圆管的对流传热和传质增强；在不同的温度条件下，超临界压力水的热物性对传热传质的影响有很大不同。     

EHD效应强化管内油的强制对流换热实验

本文以高粘性流体为实验工质,对水平光滑管内油的层流流动换热进行了直流高压电场强化（ＥＨＤ效应）实验研究。以实验方法调查了其换热系数强化率与外加电场强度、热流密度及流动速度,油温等因素的相关性。实验证实了外加直流高压电场能对管内层流强制对流换热起着很好的强化作用。验证了高粘性流体在ＥＨＤ效应下,综合换热性能同样有大幅度增加。     

最小煅耗优化在椭圆管换热中的应用

本文以(?)耗最小作为目标,以流动过程中的功率消耗一定作为约束条件,结合能量守恒方程和质量守恒方程得到了对流换热的优化场方程。通过数值计算,对优化场方程下的椭圆管对流换热问题进行了研究。结果表明,椭圆管优化速度场为多纵向涡结构,在这种优化场下换热能力增加的幅度远大于阻力增加的幅度,证明了以(?)耗最小作为目标的优化理论能够用于指导强化换热元件的设计。     

ENHANCEMENT OF FORCED CONVECTIVE HEAT TRANSFER IN NARROW CONCENTRIC ANNULI BY TURBULENCE PROMOTERS

Abstract

Forced convective heat transfer in a narrow concentric annulus was enhanced by turbulence promoters to improve the heat removal from a high-temperature gas-cooled reactor, a gas-cooled fusion reactor, and other narrow flow passages. The present experiments, which differed from those performed in conventional research, were carried out to examine the effect of turbulence promoters on the inner insulated wall opposite the outer smooth heated wall. This was achieved by changing the ratio of the pitch and the height P/ε, the ratio of the height and the space ε/ε¹, and the type of turbulence promoters used. Experimental results were examined for the local heat transfer coefficient distribution on the smooth outer tube, the average heat transfer coefficient, the friction factor, and the thermal performance. Five kinds of evaluations for thermal performance were carried out.P24     

纳米流体对流换热的实验研究

建立了测量纳米流体对流换热系数的实验系统,测量了不同粒子体积份额的水-Cu纳米流体在层流与湍流状态下的管内对流换热系数,实验结果表明,在液体中添加纳米粒子增大了液体的管内对流换热系数,粒子的体积份额是影响纳米流体对流换热系数的因素之一。综合考虑影响纳米流体对流换热的多种因素,提出了计算纳米流体对流换热系数的关联式。     

Effect of nonstationary thermal gravitation-capillary convection on temperature distribution in a thin vertical wall

Time dependences of temperature distributions in a thin metal wall were studied experimentally under two conditions of convective heat transfer in a tank model. In the first case, the vertical working wall was heated from within due to a convective heat flux from the opposite wall heated monotonously, and it was cooled due to heat transfer to the ambient medium. Dependence of the temperature field on a thin wall at the stage of convective flow development was retraced with the help of the thermographic camera and thermocouple sensors. In the second case, the tank wall was heated uniformly by IR radiation from the outside, and non-stationary convective flow and volumetric liquid heating were formed inside. Time dependence of temperature distribution over the wall height is studied. It is shown that the flow structure and convective heat transfer in a fuel layer with free boundary are subjected not only to the buoyancy force, but also to the thermocapillary effect. The local features of the flow affect temperature distribution in a thin wall.     

管内超临界压力水的混和对流换热

本文利用FLUENT6.0软件,数值研究了超临界压力下水在光管内作层流流动和换热特性,着重考察了重力引 起的二次流的影响。研究发现垂直管中由于浮力作用,速度曲线不再是抛物线,而成M状,并在壁面附近出现峰值;重 力作用下,物性的剧烈变化在水平管垂直流动方向引起了很强的二次流,从而影响了阻力特性和换热特性。