采用多孔介质和肋片复合传热强化的数值研究

本文采用数值计算方法分析了圆管中填充多孔介质和肋片时在充分发展段的流动与传热特性.结果表明,在管内部分填充多孔介质的情况下增加适量的不连续肋片能达到如下两个目的:(1)不连续的肋片能在壁面上扰动流体来强化换热而阻力增加不大;(2)不连续的肋片能在壁面上支撑多孔介质使其在径向固定.计算结果表明,这种复合强化方法的Nu和PEC值比只在管内填充多孔介质时平均高出54%和36%.     

圆管内插入螺旋片状多孔介质的换热性能及场协同分析

采用数值计算的方法,以水为流动介质,研究了圆管内插入螺旋片状多孔介质在充分发展的层流区的换热及流动综合性能,并与环状和圆柱状多孔介质插入物进行了对比,此外,利用场物理量协同原理对计算结果进行了分析。结果表明,在圆管内插入螺旋片状多孔介质可以有效提高换热与流动的综合性能,其PEC达到3.60～3.95.     

固-液相变糊状区的格子Boltzmann研究

为深入探讨固-液相变材料在相界面内(糊状区)的流动和传热对固-液相变过程的影响,本文基于"焓-多孔介质"模型,提出研究糊状区的"多相流-多孔介质"两区域复合模型,将糊状区的高含液率视为多相流区域,而低含液率区域视为多孔介质,采用格子Boltzmann方法对固-液相变糊状区的流动和传热过程进行研究.重点讨论了相变温度半径,不同高、低含液率区的分界点γ_(tr)对糊状区的发展、迁移以及对相变过程的影响.研究结果表明糊状区厚度随相变半径的增大而增加,进而影响相变过程中流动和换热;对比复合模型的不同高、低含液率分界点γ_(tr)时和单纯多孔介质模型时的糊状区的边界、流动和换热情况,表明将糊状区高液相率区采用多相流模型进行分析,可以正确反映出高含液率区域内固相微粒随液相流动的特性及其对相变过程的影响。     

水流经垂直多孔介质同心套管的传热实验研究

本文报道了水向上流经垂直多孔介质同心套管混合对流的传热实验装置和进口段对流换热的实验结果.内装多孔介质的同心套管内热边界层的发展不同于空同心套管,多孔介质对流动的“扰动”明显地影响传热,在热边界层发展段的自然对流影响较大,且随着热边界层的发展其影响逐渐减小.     

圆管内插入环状多孔介质的换热性能研究及其场协同分析

本文运用数值计算的方法,以空气为流动介质,研究了圆管内插入环状多孔介质在充分发展的层流区的换热及流动综合性能,并进行了场协同分析.结果表明,在圆管内插入环状多孔介质可以有效提高换热与流动的综合性能,其PEC值随Re数的增大呈现缓慢增大的趋势.多孔材料的孔隙率对综合性能的影响最为明显,孔隙率越高,综合性能越好.     

内置螺旋片的强化传热管的数值模拟研究

本文采用数值计算的方法,以水为流动介质,对内置螺旋片的强化传热管进行流动与传热特性的分析.结果表明,在管内插入螺旋片可以有效提高换热与流动的综合性能,雷诺数Re在300O～12000之间时,其PEC值在1.60～2.40之间.     

多孔介质模拟用于气膜冷气流动研究的尝试

本文采用多孔介质模拟与带真实气膜孔流动模拟方法,对平板气膜孔模型在低速条件下进行对比研究,以确定适用于涡轮冷却叶片气膜冷气与主流流动影响研究的多孔介质模拟方法。结果表明,采用流场参数进行多孔介质关键参数迭代计算,可以简化多孔介质方法在气膜冷气流动模拟中的应用。多孔介质模拟方法可以在较小的网格量下,获得较为详细的流场信息,对气膜冷气的流量、冷气射流速度、掺混平均的速度剖面、掺混损失、充分掺混区的平均气膜冷却效率、绝热壁温等进行较为准确的模拟。     

射流冲击泡沫金属流动液膜传热的实验研究

薄液膜蒸发由于其优良的传热特性而被广泛应用于工业领域。在流动液膜上表面覆盖铜质泡沫金属,并耦合空气射流冲击,能够进一步强化传热。多孔泡沫金属提供的毛细驱动力能够有效控制流动液膜的厚度以避免干涸,同时多孔材料特殊的固体骨架构造可以扩大固液、气液传热面积。为了研究射流冲击条件下多孔介质覆盖流动液膜的传热特性,本文通过实验方法,对包括液膜流速Vf、空气射流速度Va、液膜厚度δf和多孔介质孔隙率ε在内的影响因素进行分析,研究并对比这些因素对加热壁面温度Tw、表面传热系数hw以及传热系数提升率的影响。     

多孔介质强化池内沸腾换热特性

为探讨多孔介质对强化池内沸腾传热的机理,在38×3mm的容器内上,应用多相流VOF模型,耦合多孔介质流动与传热模型,通过添加用户自定义程序实现了对光滑和多孔加热壁面的池内沸腾传热过程进行数值模拟。数值模拟结果与实验结果相符合,所建立的数学模型为多孔介质的沸腾传热研究提供了依据。     

多孔介质中熔融盐流体高温斜温层蓄热的热特性

对熔融盐高温斜温层蓄热过程进行了较深入的理论与实验研究.基于多孔介质局部热平衡理论,建立了多孔介质中熔融盐流体斜温层蓄热的局部热平衡数值模型,研究了熔融盐、多孔介质孔隙结构参数对多孔介质中熔融盐流体传热与流动的影响规律,并在熔融盐传热-蓄热实验平台上进行了试验研究.结果表明:与熔融盐单相流体斜温层(无填充多孔介质)蓄热系统相比,多孔介质填料能够减少斜温层的厚度和改善其形状,采用单位体积热容量(pc)s大于(pc)f,孔隙率(?)小于0.4有利于降低斜温层厚度及其移动速度.揭示了多孔介质中熔融盐流体斜温层蓄热系统的蓄热特性,为熔融盐高温斜温层蓄热的设计和运行控制提供依据.     

三维有序排列多孔介质对流换热的数值研究

利用CFD软件数值研究了颗粒三维有序堆积多孔介质的对流换热问题. 采用颗粒直径分别为14 mm,9.4 mm和7 mm的球形颗粒有序排列构成多孔介质骨架,在多孔骨架的上方有一恒热流密度的铜板. 采用流固耦合的方法研究了槽通道内温度分布和局部对流换热系数的分布以及对流换热的影响因素. 研究结果表明:热渗透的厚度和温度边界层的厚度在流动方向上逐渐增大,并且随流量的增加而减小;当骨架的导热系数比较高时,对流换热随颗粒直径的减小而略有增大;对流换热系数随聚丙烯酰胺溶液浓度的增大而减小,黏性耗散减弱了对流换热. 关键词： 多孔介质 温度场 局部对流换热系数 数值模拟     

Amélioration du transfert thermique par un dépôt poreux sur la paroi d'un échangeur tubulaire

A study of flow regime and heat transfer in an annular heat exchanger partially filled with a porous medium is presented in this work. Constant heat flux and constant wall temperature boundary conditions on the inner cylinder are considered, while the outer cylinder is assumed adiabatic. The study is for both the thermal entry region and the thermally fully developed region. The flow in the porous region is modelled either by the Darcy-Brinkman equation for which an exact solution is developed or by the Darcy-Brinkman-Forchheimer equation in order to take into account inertial effects. For this case a numerical solution based on a control volume method is discussed. The results emphasize the effect of the porous layer attached to the inner cylinder on the thermal development length and heat transfer rate. It is shown that the porous substrate reduces the thermal entry length. When the effective thermal conductivity of the saturated porous medium is of the order of the fluid thermal conductivity, the local Nusselt does not vary monotonically with the thickness of the substrate. However, the use of a porous matrix always leads to an increase in the heat transfer rate provided its thermophysical properties and thickness are well chosen.     

多纵向涡对管内湍流换热特性影响的数值分析

对多纵向涡对管内湍流换热和流阻特性进行了数值分析。结果表明,多纵向涡可明显强化管内湍流换热,其流阻增加与换热增强相当。在计算范围内管内湍流换热时纵向涡对越多强化效果越好,多纵向涡的尺度应与热边界层厚度相当。同时,管内多纵向涡沿轴向还具有不易衰减的特性,这为多纵向涡的应用提供了方便。     

Analytical Analysis of Heat Transfer and Entropy Generation in a Tube Filled with Double-Layer Porous Media

The heat transfer and entropy generation in a tube filled with double-layer porous media are analytically investigated. The wall of the tube is subjected to a constant heat flux. The Darcy-Brinkman model is utilized to describe the fluid flow, and the local thermal non-equilibrium model is employed to establish the energy equations. The solutions of the temperature and velocity distributions are analytically derived and validated in limiting case. The analytical solutions of the local and total entropy generation, as well as the Nusselt number, are further derived to analyze the performance of heat transfer and irreversibility of the tube. The influences of the Darcy number, the Biot number, the dimensionless interfacial radius, and the thermal conductivity ratio, on flow and heat transfer are discussed. The results indicate, for the first time, that the Nusselt number for the tube filled with double-layer porous media can be larger than that for the tube filled with single layer porous medium, while the total entropy generation rate for the tube filled with double-layer porous media can be less than that for the tube filled with single layer porous medium. And the dimensionless interfacial radius corresponding to the maximum value of the Nusselt number is different from that corresponding to the minimum value of the total entropy generation rate.     

多孔介质中超临界C O2对流换热数值模拟

本文对超临界二氧化碳在多孔结构中的对流换热进行了数值模拟研究.结果表明,超临界条件下二氧化碳剧烈的变物性对多孔介质中的对流换热会产生很大影响;局部热平衡条件下对流换热系数的数值计算值比局部非热平衡条件下的计算结果大;对流换热系数随着颗粒直径的增大而增大.     

INTERNAL HEAT TRANSFER TO POWER-LAW FLUID FLOWS THROUGH POROUS MEDIA

Heat transfer and pressure drop were measured for flow of aqueous solutions of Carbopol 934 ® and Carbopol EZ1 ® through a vertical tube filled with porous media. The heated stainless steel test section has an inside diameter of 2.25 cm, and is 200 diameters long. The porosity was varied from 0.32 to 0.68 by using uniform spherical glass beads. Uniform heat flux thermal boundary condition was imposed by passing direct electric current through the tube wall. Over a range of 45 < Re a < 7,000, 21 < Pr a < 58, 0.62 < n < 0.80, 1.6 < D/d < 4.5, and polymer concentration from 250 to 500 ppm, the friction factor data agreed with the Newtonian prediction. Heat transfer to power-law fluids increases with increasing Re a and Pr a , and decreasing porosity. A new correlation was proposed for predicting the heat transfer to power-law fluid flows through confined porous media.     

Theoretical analysis of porous radiant burners under 2-D radiation field using discrete ordinates method

This paper describes a theoretical study to investigate the heat transfer characteristics of porous radiant burners (PRBs). In the present work, a 2-D rectangular model is used to solve the governing equations for porous medium and gas flow before the premixed flame to the exhaust gas. The gas and the solid phases are considered in non-local thermal equilibrium and combustion in the porous medium is modeled by considering a non-uniform heat generation zone. The homogeneous porous media, in addition to its convective heat exchange with the gas, may absorb, emit and scatter thermal radiation. The radiation effect in the gas flow is neglected but the conductive heat transfer is taken into account. In order to analyze the thermal characteristics of porous burners, the coupled energy equations for the gas and porous medium in steady condition are solved numerically and the discrete ordinates method (DOM) is used to obtain the distribution of radiative heat flux in the porous media. Finally, the effects of various parameters on the performance of porous radiant burners are examined. The present results are compared with some reported theoretical and experimental results by other investigators and good agreement is found.     

INTERNAL HEAT TRANSFER TO VISCOELASTIC FLOWS THROUGH POROUS MEDIA

Heat transfer and pressure drop were measured for flow of water, mineral oil, and aqueous solutions of viscoelastic polymers through a vertical tube filled with porous media. The heated stainless steel test section has an inside diameter of 2.25 cm, and is 200 diameters long. The porosity was varied from 0.32 to 0.68 by using uniform spherical glass beads. Uniform heat flux thermal boundary condition was imposed by passing direct electric current through the tube wall. Over a range of the parameters 8 &lt; Re &lt; 31,000, 7 &lt; Pr &lt; 245, 0.22 &lt; d/D &lt; 0.6, and polymer concentration from 100 to 500 parts per million, the friction factor data for Newtonian fluids agreed with the predictions in the literature. Drag reduction was noticed in the turbulent flow of dilute viscoelastic polymer solutions (Praestol at 100 and 200 wppm; polyox at 500 wppm) at φ &lt; 0.68. Viscoelastic effect on heat transfer was insignificant. A new correlation was proposed for predicting heat transfer to Newtonian as well as viscoelastic flows through confined porous media.     

Effects of Solid Matrix and Porosity of Porous Medium on Heat Transfer of Marangoni Boundary Layer Flow Saturated with Power-Law Nanofluids

The effect of the solid matrix and porosity of the porous medium are first introduced to the study of power-law nanofluids,and the Marangoni boundary layer flow with heat generation is investigated.Two cases of solid matrix of porous medium including glass balls and aluminum foam are considered.The governing partial differential equations are simplified by dimensionless variables and similarity transformations,and are solved numerically by using a shooting method with the fourth-fifth-order Runge-Kutta integration technique.It is indicated that the increase of the porosity leads to the enhancement of heat transfer in the surface of the Marangoni boundary layer flow.