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螺旋折流片换热器壳侧传热与流动的数值模拟 总被引:9,自引:1,他引:8
提出了一种强化管壳式换热器壳侧传热的螺旋折流片式换热器新方案,该方案在部分管子上套上螺旋折流片,不仅强化传热,而且对相邻管子形成支撑;利用FLUENT流体计算软件对同心套管螺旋折流片式换热段的壳侧流场、温度场进行了数值模拟,并讨论了螺旋角对其强化传热和阻力性能的影响。结果显示螺旋折流片诱导的涡旋流动对于减薄边界层,促进近壁流体与主流区流体的动量和质量交换进而强化传热有明显的作用,传热系数可比光管提高约40%-100%,但其流动阻力也将增大。 相似文献
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建立三叶型花瓣扭曲螺旋缠绕管的几何模型,对管内的流动和传热特性进行模拟,分析不同结构参数对换热性能的影响,利用响应面法对该管的换热性能进行拟合。结果表明,与传统的光管缠绕管相比,三叶型花瓣扭曲螺旋缠绕管产生的扭转力改善了温度分布不均的现象且换热性能提高了40%;当缠绕半径取最小值,节距取最大值时,换热系数h可达到最大值4.16 kW/(m2·K);三阶多项式能够最准确地描述换热系数与输入参数的关系,其中h的MRS为0.17%,RMSE为0.006,R2为0.999。 相似文献
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蒸气在倾斜细小直径圆管内的流动凝结换热特性 总被引:1,自引:0,他引:1
细小管内的流动凝结换热具有许多超常换热特性,经典的Nusselt分析方法已不能满足需要。在以往研究的基础上,本文进一步通过实验探析换热温差和蒸气流量对不同直径的细小管内流动凝结换热的影响。研究表明,管径越小,换热温差对凝结换热系数的影响程度越低;通过流量和倾角对凝结换热数的影响,分析了重力引发的流动分层和剪切力对凝结液的排除两种因素对细管传热强化的作用机制。本文的实验结果和用于常规尺度下的通用关联式对比表明,采用细管,管内的流动凝结换热得到无可置疑的强化 相似文献
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《工程热物理学报》2017,(9)
依据涡旋流动强化传热技术,变传统直流道的梅花形支撑孔板为螺旋流道的梅花形支撑孔板,进而设计出一种新型螺旋梅花形孔板换热器,建立了相应的数学模型,并对其传热与流动特性进行了仿真计算。通过与梅花形孔板换热器的对比分析,展示了新型换热器壳程强化换热机理,并进一步探索了螺旋流道的螺旋角对新型换热器的影响。计算结果表明:在研究范围内,新型换热器壳程平均对流换热系数高于传统换热器,但同时壳程压降也相对应增加,在一定雷诺数范围内新型换热器综合性能参数优于传统换热器。当螺旋角为27°、雷诺数小于19672时,其综合性能比传统换热器较佳;探究了不同螺旋角的影响,发现螺旋角越大,新型换热器压降越大,同时换热能力也越强。 相似文献
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目前国际上对超临界水冷堆进行了大量的研究,但对其堆芯内超临界流体流动传热的认识还十分欠缺.本文采用CFX对超临界水冷堆典型子通道内的流动传热特征进行了CFD研究,对比分析了四边形和三角形布置的两类子通道流动传热特征.计算结果表明二阶SSG湍流模型能较好地模拟子通道内的超临界流体流动和传热特征.流动特征的分析表明四边形子通道内的二次流比三角形子通道内的复杂,强度也更大.两类子通道内的湍流脉动特征类似,当栅距较小时其间隙处的湍流交混系数都在0.02~0.025之间.四边形子通道的周向温度和换热不均匀性比三角形子通道的强烈. 相似文献
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Experimental results on convective heat transfer from a single cube on a flat surface are presented for different attack angles
to the incident flow and Reynolds numbers. The character of vortex formation and the effect of flow structure on heat transfer
at detached flow around a cube were studied by visualization. Local heat transfer and heat transfer averaged over the separate
faces and the whole lateral surface of the cube were studied. Contribution of separate cube faces to total heat transfer depending
on the attack angle was estimated. Data obtained were compared with those published in literature. The reasons for observed
differences caused by the effect of many factors: boundary layer thickness, turbulence level of the incident flow, channel
constraint, etc., are analysed. 相似文献
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Coupled flow and heat transfer of power-law nanofluids on non-isothermal rough rotary disk subjected to magnetic field 下载免费PDF全文
Yun-Xian Pei 《中国物理 B》2022,31(6):64402-064402
We study the coupled flow and heat transfer of power-law nanofluids on a non-isothermal rough rotating disk subjected to a magnetic field. The problem is formulated in terms of specified curvilinear orthogonal coordinate system. An improved BVP4C algorithm is proposed, and numerical solutions are obtained. The influence of volume fraction, types and shapes of nanoparticles, magnetic field and power-law index on the flow, and heat transfer behavior are discussed. The obtained results show that the power-law exponents (PLE), nanoparticle volume fraction (NVF), and magnetic field inclination angle (MFIA) have almost no effects on velocities in the wave surface direction, but have small or significant effects on the azimuth direction. The NVF has remarkable influences on local Nusselt number (LNN) and friction coefficients (FC) in the radial direction and the azimuth direction (AD). The LNN increases with NVF increasing while FC in AD decreases. The types of nanoparticles, magnetic field strength, and inclination have small effects on LNN, but they have remarkable influences on the friction coefficients with positively correlated heat transfer rate, while the inclination is negatively correlated with heat transfer rate. The size of the nanoparticle shape factor is positively correlated with LNN. 相似文献
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以蒸馏水为工质,在闭式循环喷雾冷却系统上,变化喷雾流量,研究了表面几何结构对喷雾传热性能的影响。从对流换热和相变换热比例关系的角度,对喷雾换热机理进行了实验研究。结果表明:与光滑表面相比,微结构表面可明显增强喷雾换热强度,这主要归因于相变换热的增强。表面温度较低时,直肋面换热效果最好 ;增大流量,光面换热增强,而直肋面变化不明显。表面温度较高时,方肋面换热效果最好;随着流量增大,所有面换热均增强。对于微结构表面,相变换热份额均大于50%,故而以相变换热为主;而光滑表面,即使在温度较低时,相变换热份额也大于20%。临界热流密度与三相接触线长度正相关,流量为15.9 mL/min时,方肋面、直肋面和光面的临界热流密度依次为159.1,120.2,109.8 W/cm2,蒸发效率分别为96.0%,72.5%,67.1%。 相似文献
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HEAT TRANSFER IN HIGH-PRESSURE COMPRESSOR GAS TURBINE INTERNAL AIR SYSTEMS: A ROTATING DISC-CONE CAVITY WITH AXIAL THROUGHFLOW 总被引:1,自引:0,他引:1
This article reports on heat transfer measurements made on a rotating test rig representing the internal disc-cone cavity of a gas turbine high-pressure (H.P.) compressor stack. Tests were carried out for a range of flow rates and rotational speeds at engine representative nondimensional conditions. The rig also had a central drive shaft, which could rotate in the same direction as the discs, contrarotate relative to the discs, or remain static. Measurements of heat transfer were obtained from a conduction solution method using measured surface temperatures as boundary conditions. Results from the outer surface of the cone are in reasonable agreement with theoretical predictions for the heat transfer from a free cone in turbulent flow. The heat transfer measurements from the inner surface of the cone reveal two regimes of heat transfer: one governed by rotation, the other by action of the throughflow. In the rotationally dominated regime, the heat transfer from the inner surface of the cone is higher for a co-rotating shaft than for either a static or contra-rotating shaft. In the throughflow-dominated regime the heat transfer shows little consistent dependence on the direction of shaft rotation. Tests carried out at different values of surface-to-fluid temperature difference add support to the hypothesis that in the rotationally dominated regime the heat transfer occurs through a process of free convection, where the buoyancy force is induced by rotation. The heat transfer from the disc is significantly lower than that from the inner surface of the cone and more or less insensitive to the sense of shaft rotation. The disc average Nusselt numbers show similar behavior to those from the inner surface of the cone and suggest that the disc heat transfer too is governed either by rotationally induced buoyancy or by the axial throughflow. 相似文献
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Subcooled flow boiling heat transfer experiments were performed with water and ethylene glycol/water mixtures at five flow velocities and four fluid inlet temperatures. Both turbulent flow and laminar flow were tested in a special test facility with its experimental test section heated from the bottom surface only. Boiling curves and subcooled flow boiling heat transfer coefficients of the tested fluids were determined from the experimental measurements. Predictive correlations of the subcooled flow boiling heat transfer coefficients were developed based on the experimental data. Comparisons are presented of wall temperatures between the experimental measurements and the correlation predictions. 相似文献
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毛细管内薄液膜轮廓和传热特性研究 总被引:2,自引:0,他引:2
本文认为毛细管的相变传热机理为液膜的导热和表面蒸发;表面蒸发受蒸汽温度、汽液界面的温度以及汽液压力差的共同控制。汽液流动机理为流动受脱离压力梯度、毛细力梯度支配。汽液相互作用机理为存在由于蒸发导致的动量转移切应力和由于汽液流速不同产生的摩擦切应力。提出的物理模型中较为全面地考虑了毛细管内传热、汽液流动及其相互作用。对毛细管半径和传热功率对薄液膜轮廓和传热特性影响程度的计算结果表明,随着毛细管半径的减小、传热功率的增大,蒸发界面区的长度会有所减小,这是针对微小空间得出的不同于常规情况的结论。 相似文献