等温容器内多孔介质强化导热研究

等温容器是在充放气过程中容器内温度基本保持不变的一种特殊容器,在气动系统中有着广泛的应用.为强化放气过程中容器壁向内部的导热,以容器截面为研究对象,对内部铜丝的分布进行了探讨.在细铜丝填充密度一定的情况下,基于多孔介质模型,以容器截面导热热阻最小为目标,优化出两层和三层变密度填充下金属丝的分布.其热阻与均匀填充时相比,分别减少了37.63%和43.70%.研究结果表明,通过改变等温容器内细铜丝的分布可以强化容器壁向内部的导热.     

含内热源可燃性多孔介质中的传热研究

煤粉、弹药等含内热源的可燃性多孔介质传热过程在自然界和工程中广泛存在。文中分析了可燃多孔介质的热传递机理，建立了相应的导热计算模型，给出了典型物种在内热源作用下的内部温度场。     

多孔表面强化沸腾传热的研究

一、前言 当前全世界普遍重视节省能源,降低产品能耗已成为重要的研究课题。构成节能对象的机器设备中,有众多的热交换器,因此,研究提高现有传热设备的性能和探求新的强化方法,对于降低能耗具有重要意义。     

管内填充多孔介质强化换热的数值研究

管内填充多孔介质强化换热的基本原理是构造热边界层,增大壁面附近流体的温度梯度,并且流动阻力增幅不大。本文运用数值模拟的方法,模拟填充多孔介质管内的流场和温度场,探讨填充比例φ、渗透率Da以及空隙率ε对管内对流换热的影响规律。研究表明,提高填充比例φ和减小渗透率Da都能明显提高换热效果,但也增加了管内流动阻力。空隙率ε对强化换热作用不大,但高空隙率可以明显降低管内流动阻力,在实际中应选用空隙率较大的多孔介质。     

含湿毛细多孔介质湿区相变传热传质干燥三方程模型

含湿毛细多孔介质的干燥过程是复杂的相变传热传质过程。该过程涉及渗流、扩散、传热、毛细效应和相变等机理，建立了含湿毛细多孔介质湿区干燥过程相变传热传质数学模型，采用全隐式有限差分方法对一维模型进行了数值计算。得到了含湿毛细多孔介质湿区干燥过程中的液相饱和度、温度和混合气体压力的变化，并分析了该计算结果。     

高温下多孔体中的传热

叙述了多孔体中高温气体焓和辐射能转换的基本原理;并介绍了目前在几个方面的应用例和取得的实际效果。     

多孔表面管沸腾传热试验研究

针对烧制成多孔表面管,进行了传热性能研究,试验表明：多孔管可以显著地强化多孔侧沸腾传热,民同规格光滑管传热性能试验对比,其沸腾给热系数比光滑管提高５－６倍。     

多孔介质-双层玻璃幕墙传热与流动特性

基于多孔介质具有吸收和贮存太阳能的特点,在双层玻璃幕墙通道内设置了多孔介质层,利用多孔介质充分收集与贮存太阳能用于建筑供暖,并采用数值模拟法研究了幕墙的传热与流动特性.结果表明,玻璃幕墙能充分利用太阳能加热新风供暖,集热效率高又节能,有推广价值.     

声空化场下浸没在多孔介质中水平圆管传热的实验研究

在水平圆管外填充固体颗粒情况下,以丙酮为工质,通过改变声空化强度、距离,颗粒直径,多孔层高度和液体过冷度等相关参数对水平圆管单相及沸腾换热的影响进行了实验研究。并分析了影响水平圆管换热的因素,及沸腾滞后的影响规律。     

薄层毛细多孔介质湿区干燥过程相变传热传质常压模型

对液相歼余饱和度Sir作了一个定义,把含湿毛细多孔介质干燥区域分为湿区和干区。建立了以液相饱和度S和温度T为参数的湿区干燥过程相变传热传质常压模型。采用全隐式有限差分方法以模型进行了数值计算。数值解表明,模型能很好地预测湿区干燥过程中的液相饱和度S和温度T的变化。     

Heat Transfer Enhancement in Shell-and-Tube Heat Exchangers Using Porous Media

A numerical simulation has been carried out to investigate the heat transfer enhancement in a shell-and-tube heat exchanger using a porous medium inside its shell and tubes, separately. A three-dimensional geometry with k-? turbulent model is used to predict the heat transfer and pressure drop characteristics of the flow. The effects of porosity and dimensions of these media on the heat exchanger's thermal performance and pressure drop are analyzed. Inside the shell, the entire tube bundle is wrapped by the porous medium, whereas inside the tubes the porous media are located in two different ways: (1) at the center of the tubes, and (2) attached to the inner wall of the tubes. The results showed that this method can improve the heat transfer at the expense of higher pressure drop. Evaluating the method showed that using porous media inside the shell, with particular dimension and porosity can increase the heat transfer rate better than pressure drop. Using this method inside the tubes leads to two diverse results: In the first configuration, pressure loss prevails over the heat transfer augmentation and it causes energy loss, whereas in the second configuration a great performance enhancement is observed.     

多孔介质气体润滑轴承气热耦合研究

考虑气体温度梯度对工质物性及轴承热稳定性的影响,以及润滑气体和多孔介质的传热耦合,在满足Darcy定律条件下三维求解雷诺方程,计算了轴承间隙和多孔介质中气体的压力及温度分布。分析了3个给定供给压力(0.5、0.65和0.8 MPa)、3种轴承偏心率(0.2、0.5、0.8)对轴承的承载能力、偏位角及润滑流量的影响,计算结果表明：在不同的轴偏心率下均存在有一段轴承最佳渗透系数范围,表征该范围承载能力最强;偏心率越大,轴承承载能力越高,最佳渗透系数区间也越明显;轴承压缩数越大承载能力也越高;间隙中温度分布不均匀导致轴承承载能力降低,通过调整压力和偏心率增加介质的润滑流量,及时导出摩擦产生热量降低间隙中气膜温度,可使轴承平衡稳定运行。     

扭曲椭圆管换热器壳程强化传热的数值研究

基于扭曲椭圆管的换热器是一种新型的新风系统换热器,针对扭曲椭圆管及其应用特点,设计了两种不同结构参数的新风系统换热器。应用FLUENT软件,在夏季工况下对两种不同结构参数的新风系统换热器壳程进行模拟分析,并通过与实验数据的对比,验证计算模型的可靠性。结果显示在相同体积流量下,随着壳程开孔面积的增大,对流换热系数h不断减小,压降Δp不断减小,综合性能系数h/Δp1/3变化不明显;随着螺距的减小,对流换热系数h不断增大,压降Δp不断增大,综合性能系数h/Δp1/3也不断增大;流场分析显示,扭曲椭圆管换热器壳程流道内,呈现出明显沿着扭曲椭圆管壁面的螺旋流,使得空气在流道内充分扰动,增强换热效果。     

Experimental Study of Condensation Heat Transfer Promotion on a Fluted Tube with Thin Porous Coatings

The article is a presentation of a new method for enhancement of filmwise condensation heat transfer on a vertical tube. The method is that a tube is fluted on its outer surface and coated with metallic powder on the crest, which is called a fluted tube with coatings. The experimental results show that the enhancement of condensation is more notable because of the dual function of Gregorig effect and the thin porous coatings.     

Heat Transfer Enhancement of Spray Cooling on Flat Aluminum Tube Heat Exchanger

This study provides an experimental analysis on the heat transfer performance of a flat aluminum tube microchannel heat exchanger with spray cooling. The effects of water spraying rate, airflow rate, and relative humidity were investigated. The test results show that the heat transfer performance increased with increasing the water spraying rate but without the penalty of increased flow resistance at low spray conditions. This effect is further enhanced by increasing the water spraying rate. However, when the spraying rate is high, part of the nonevaporated drops attached to the fin surface and formed a liquid film, which caused the flow passage to become narrower. Further increase in the spraying rate resulted in part of the flow passages being blocked by the nonevaporated water drops and caused a region of poor heat transfer. The friction coefficient jumped drastically at this condition. This phenomenon deceased gradually with increasing airflow rate. High inlet air humidity resulted in the water accumulation phenomenon appearing at lower water spraying rates. The evaporative cooling effect decreased and flow friction increased. The test results just described show that the water spray is able to significantly improve the air-side heat transfer performance. The optimum spray rate for each airflow rate must be carefully determined.     

波纹内翅片管内空气强化传热特性的研究

研究了一种波纹内翅片管的换热特性，得出了所测参数范围内沿程温度及换热系数分布特点，并比较了相同管径的内翅片波纹管和光管的综合换热效果，结果表明：高Re数时管子与翅片间的接触热阻对传热性能有较大影响；波纹内翅片管的综合换热效果强于光管，而且在低流速下换热强化效果更加明显。     

Heat and Mass Transfer with Condensation in Non-Saturated Porous Media

Heat and mass transfer with condensation in porous media was numerically studied coupling with distributions of temperature, vapor concentration, pressure and water saturation. The transport processes in porous media displayed two distinct stages, or early and late stages. Different characteristics during these stages were described with the consideration of physical nature. A systematical investigation was conducted to explore the influence of different parameters on the processes, including the temperature, the particle diameter, the porosity, and the thermal conductivity of the particle. A modeling experiment was conducted to partially validate the calculation.     

三叶膨胀管换热器壳程强化传热的数值研究

三叶膨胀管是一种新型强化传热管,针对纵向流换热器特点,设计了三种不同管束结构参数的三叶膨胀管自支撑纵向流换热器。应用FLUENT软件及Realizable k-ε湍流模型,对三种不同结构参数的三叶膨胀管换热器壳程强化传热特性展开了数值模拟,并通过与实验数据的对比,验证了计算模型的可靠性。计算了不同壳程介质流速下,三叶膨胀管换热器壳程的换热系数与压降值,并获得了壳程流体流线以及相应的温度场、速度场和二次流分布图。结果发现,在壳程水流速一致的情况下,管束横向间距越大的三叶膨胀管换热器,壳程拥有更高的综合换热性能和更低的压降值,但相应地,换热系数也更低。流场分析显示,壳程流体流线呈现出三维纵向旋流形态,二次流的出现改变了速度场和温度场分布,二次流的强度随着管束横向间距的减小而增大。