螺旋槽管管内湍流流动与换热的三维数值模拟

利用Fluent对5种不同槽深的螺旋槽管进行了模拟求解,得出了湍流状态下螺旋槽管内流体的速度场和温度场,从微观上说明了螺旋槽管的强化传热机理。分析了槽深对螺旋槽管阻力性能和换热性能的影响。数值计算结果表明,该类螺旋槽管在湍流工况下的平均Nu数大约是光管的1.6—2.1倍,平均阻力系数f大约是光管1.5—4.5倍。与实验数据进行比较发现,数值模拟具有相当的可靠性。     

组合曲线回归法计算螺旋扁管管内对流传热系数

针对螺旋扁管壁面温度难于准确测试的特点,提出采用线性曲线回归与非线性曲线回归相结合的方法进行管内传热系数计算.进行了光管与螺旋扁管管内对流传热实验,并用该方法计算管内对流传热系数.光管传热系数计算值与经典公式的大偏差小于6%.螺旋扁管管内传热系数的计算值略大于通过测量壁温获得的传热系数值,分析了二者存在差异的原因.组合...     

水平内微肋管局部凝结换热性能实验与数值求解

以Ｒ１１为工质，蒸汽凝结压力为１４７－２６５ｋＰａ，质量流率４ｔｙ１５３ｋｇ／ｍ２ｓ，本文对二维内微肋管和三维内微肋管水平管内凝结分层流区局部换热系数进行了系统的实验。与光管比较，二维内微肋管和三维内微肋管局部凝结换热系数分别提高了１４７－７８３％和２６１－９９７％。本文首次从理论分析入手建立了二维内微肋管水平管内凝结分层流区局部换热系数分析模型并进行了数值求解。计算结果与本文实验相当吻合。     

内螺纹肋管内流动与传热的数值模拟

本文以空气为介质(Pr=0.698),通过数值模拟的方法在Re=600-2000的范围内对内螺纹肋管内周期性充分发展的层流流动进行了模拟分析,说明了不同Re、螺纹肋的旋转角度α、螺纹肋的牙数N8对速度环量、Nu、Nu和阻力系数的影响,并通过对Nu和速度环量之间的关系进行了分析,得出在内螺纹肋管内强化换热流动中决定换热强度的物理量一速度环量。     

无网格方法中的背景积分方案及单颗粒下降过程的数值模拟

在用无网格方法对有边界移动的气固两相流动进行数值模拟时发现,如果采用背景积分网格对求解域进行积分,将会产生压力场的数值振荡,使计算结果失真.详细分析了产生这种数值振荡的原因,提出了解决方案,并计算了一个颗粒在管道内的下降过程.计算结果表明,提出的解决方案能有效地降低压力场的数值振荡,从而使无网格方法能应用于气固两相流动的直接数值模拟.     

涡流管内三维强旋转流场数值模拟与分析

涡流管内可压缩气体的强旋转流动是涡流管能量分离的根本原因和驱动力,因而涡流管内流场研究是揭示涡流管能量分离物理机制的首要关键问题。由于涡流管内可压缩气体的三维强旋转湍流流动,实验测量中存在诸多问题,而CFD数值模拟技术对此具有很大的优势。文中以涡流管内部流场为研究对象,建立了涡流管计算域模型并进行网格划分,讨论了边界条件、湍流模型以及线性方程组求解策略等问题,对不同冷气流率下的涡流管内三维强旋流流场结构特性进行数值模拟,获得了不同冷气流率下的旋转运动、轴向运动、径向运动和循环流的分布特性。研究表明Realizableκ-ε湍流模型能够充分反映强旋流动特点,数值模拟结果与文献中实验值基本吻合。     

带肋气膜冷却平板的数值模拟研究

本文对不带肋和带45°肋气膜冷却平板的三维对流换热与导热耦合传热问题进行了数值模拟。网格划分采用非结构化网格,湍流模型为SSTκ-ε模型,近壁处采用壁面函数法,采用SIMPLEC算法求解速度和压力的耦合。计算获得了不带肋和带45°肋气膜冷却平板的流场分布和平板内外表面的换热系数值。结果表明带45°肋的气膜冷却平板通道流场结构比较复杂,平板表面平均温度较无肋气膜冷却平板表面平均温度下降,而在近气膜孔区域冷、热表面平均换热系数较无肋时增大。     

圆管内插入螺旋片强化传热数值模拟及(火积)耗散分析

本文对圆管内插入不同中空比(d~*=d_1/D)空心轴螺旋片的湍流传热过程进行了数值模拟研究,结果显示内插空心轴螺旋片圆管内的传热性能明显得到提升,平均努谢尔特数相比光滑圆管提高了105%~385%;并从((?))耗散与传热效率的角度定量分析了内插螺旋片强化传热机理,结果发现内插螺旋片管内传热效率在91.3%~92.3%之间,均高于光管。     

非结构化网格下自由分子微电热推力器数值模拟

采用非结构化网格,压力边界条件的DSMC-FVM耦合方法对自由分子微电阻加热推力器微喷管内的流动与换热进行了数值模拟.分析了微喷管的流场特征,证明所采用的DSMC-FVM多尺度方法对微喷管内流场与温度场模拟是合适而且必要的.     

子网格在DSMC中的作用及三角形子网格

本文采用直接模拟蒙特卡罗方法对二维微通道内Poiseuille流动进行了数值模拟,通过对不同网格密度下计算结果与"收敛"结果的比较,得到了计算网格特别是子网格系统对计算结果的影响;在此基础上,发展了基于Delaunay三角形非结构网格的子网格系统,讨论了采用该子网格的非结构化网格对模拟结果的影响,结果表明:该方法能有效提高模拟的准确性,而常规无子网格的非结构网格将"虚假"地增加气体流动的稀薄性。     

Performance of a compact,spiral coil heat exchanger

A spiral coil heat exchanger consists of a number of horizontal layers of spirally wound, finned tubes connected to vertical manifolds at the inner and outermost turns of each coil. This design has advantages in heat recovery and air-conditioning applications. Two theoretical models to predict the performance of this compact heat exchanger are presented based upon unmixed and mixed air-flow considerations. Results of experimental studies on a laboratory model of the spiral coil heat exchanger agree well with the predicted performance of the theoretical models. Charts of effectiveness vs NTU suitable for design are presented.     

Compact heat exchangers based on individually finned flat multichannel tubes

Attempts to design prospective aluminium heat exchangers based on individually finned flat multichannel tubes manufactured according to a waste-free technology of obtaining surfaces by undercutting and flanging thin layers of metal (fins) aer considered in this paper. Technological peculiarities of arranging and assembling radiators based on individually finned tubes, experimental data on aluminium radiators and heat exchangers based on heat tubes of capillary structure, and their analysis are also presented.     

伴随有水蒸气凝结的烟气对流换热的实验研究

本文通过实验研究了冷凝式燃气热水器中烟气伴随有水蒸气凝结的受迫对流换热过程。着重介绍实验系统、测试方法和对塔板式换热器和肋片板式换热器的实验研究结果。实验表明,有水蒸气凝结时的烟气对流换热系数远大于无凝结时的换热系数,可提高数倍。在冷凝式换热器中,塔板式换热器的换热系数大于肋片板式换热器。     

Heat transfer expansion on outer surfaces of heat pipes

Some peculiarities of production technology for finned surfaces on round and flat heat pipes for heat exchangers are considered in the present paper. A comparison of different types of finned tubes is presented. The experimental investigation agrees with the data of the analysis.     

Pumping Power Minimization in Staggered Finned Circular and Elliptic-Tube Heat Exchangers in Turbulent Flow

An experimental study aimed at minimizing pumping power required to supply air through a finned tube bundle configuration is presented in this article. Results were obtained for the Reynolds number based on the smaller ellipse axis (RE_2b) ranging from 2,650 to 10,600, i.e., in turbulent flow. In the turbulent regime, pressure drops are expected to vary with eccentricity. Experimental optimization results for finned circular and elliptic tubes show that pumping power can be minimized with respect to tube spacing and eccentricity. In comparison with values obtained for circular tubes, the optimal elliptical arrangements show pumping power reductions from 5% to 10%.     

EXPERIMENTAL INVESTIGATION OF HEAT TRANSFER AND PRESSURE DROP CHARACTERISTICS OF W-TYPE SPIRALLY FLUTED TUBES

A new w-type spirally fluted tube with enhanced heat transfer characteristics was developed and manufactured. The heat transfer and pressure drop characteristics of tubes with various geometric parameters were measured over a range of Reynolds numbers from 8,000 to 30,000 for water flowing horizontally through the tube with steam condensing on the outside surface. Experimental correlations for the pressure drop and the heat transfer coefficient were developed from a large amount of data using multivariable linear regression analysis. Factors influencing the heat transfer and flow were analyzed. The experiments showed that heat transfer coefficient can be increased by 3–8% with the pressure drop reduced by 5–10% compared with an ordinary spirally fluted tube.     

Natural frequencies of finned heat exchanger tubes

The heat transfer of heat exchanger tubes is often enhanced by rolling external fins on to the tubes. These fins contribute to both the mass and the stiffness of the tubes. Calculations of the bending natural frequencies of finned tubes with only the mass contribution considered lead to values which are up to 10% lower than experimental values. A simple correction is derived to account also for the stiffening effect of the fins. With this correction good agreement with experiments is obtained.     

两种内翅片管对流换热与阻力特性的实验研究

本文通过实验方法研究了当内翅片管几何尺寸及形状基本相同时,在内翅片上增加凸起对其换热和阻力的影响,并拟合出了所测参数范围内换热和阻力的实验关联式,结果表明在翅片管上增加凸起确实有强化换热的作用,同时阻力增加明显。通过对实验管综合性能的比较,发现增加凸起的换热管更适用于压缩机中冷器。     

低温发电用翅片管换热器传热特性的数值模拟分析

为了深入研究低温余热发电系统用翅片管换热器的传热特性,文中建立了翅片管换热器计算模型,对工质R123在翅片管换热器内的传热性能进行数值模拟,比较管内工质R123在不同流速与温度时的换热特性,利用最小二乘法原理,对烟气侧和工质侧的换热关联式进行了拟合,得到了二者的换热准则方程,此外,利用实验方法对模拟结果进行验证。