首页> 外文会议>ASME International Mechanical Engineering Congress and Exposition >CFD INVESTIGATION OF DEVELOPING AND REDEVELOPING LAMINAR FLOW AND HEAT TRANSFER CHARACTERISTICS IN COILED TUBE SYSTEMS FOR CONSTANT WALL TEMPERATURE HEATING AND COOLING (PART II: SPIRAL CONFIGURATIONS)
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CFD INVESTIGATION OF DEVELOPING AND REDEVELOPING LAMINAR FLOW AND HEAT TRANSFER CHARACTERISTICS IN COILED TUBE SYSTEMS FOR CONSTANT WALL TEMPERATURE HEATING AND COOLING (PART II: SPIRAL CONFIGURATIONS)

机译:CFD调查恒壁温度加热卷材管系统开发和重建层流流量及传热特性(第二部分:螺旋配置)

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In this paper developing and redeveloping laminar fluid flow and heat transfer performance in spiral coiled tube heat exchanger systems with specified coil-to-tube radius ratios (5 to 45), spiral pitch and inside-to-outside flow are investigated using appropriate numerical modeling techniques in the CFD package (Fluent v6.2). The CFD models employ variable thermo-physical properties in the analysis of uniform wall temperature heating and cooling of common working fluids such as air and water. The CFD models developed in Part I of this investigation are extended to analyze spiral tube configurations. Appropriate dimensionless variables used to describe the (re)developing hydrodynamic and thermal flow for coiled tube systems are defined and discussed. The spiral configuration is unique in that fully developed flow is not attained for the coil-to-tube radius ratios used in this work. In spiral configurations, the centrifugal effects are not constant as the radius of curvature is not constant. Flows within the spiral flow passages are analyzed as re-developing or re-establishing hydrodynamic and thermal flows. As with the helical flow configuration, it has been shown that in addition to the radius ratio and the Dean and Prandtl numbers, the heat transfer performance also depends upon the interactions (expansion and suppression) between the viscous and thermal boundary layers due to secondary flows caused by the centrifugal forces inherent in coiled tube systems. The predictions of the numerical simulations also showed that the local friction factor and heat transfer performance continuously vary along the length of the tube. The results obtained from this work indicate the limits of application of the friction factor and heat transfer correlations reported in the literature.
机译:在本文中,使用特定的数值模型研究了具有规定的线圈到管半径比(5至45)的螺旋线管热交换器系统中开发和重新开发的层流体流动和传热性能,使用适当的数值模型研究螺旋间距和内外流动CFD包装中的技术(Fluent V6.2)。 CFD模型在分析均匀壁温加热和冷却诸如空气和水中的普通工作流体的冷却中采用可变热物理性质。在该调查的第I部分开发的CFD模型扩展以分析螺旋管配置。定义和讨论了用于描述卷绕管系统的流体动力学和热流动的适当的无量纲变量。螺旋配置在本工作中使用的线圈到管半径比没有达到完全发育的流动。在螺旋配置中,随着曲率半径不是恒定的,离心效应不是恒定的。分析螺旋流动通道内的流动作为重新开发或重新建立流体动力学和热流。与螺旋流量配置一样,已经表明,除了半径比和院长和普朗特数量之外,传热性能还取决于由于次级流量引起的粘性和热边界层之间的相互作用(膨胀和抑制)由卷绕管系统中固有的离心力引起的。数值模拟的预测还表明,局部摩擦因子和传热性能沿管的长度连续变化。从该工作中获得的结果表明文献中报告的摩擦因子和传热相关的应用的限制。

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