首页> 外文会议>PID-vol.9; ASME International Mechanical Engineering Congress and Exposition; 20041113-19; Anaheim,CA(US) >INVESTIGATION AND DEVELOPMENT OF PROPOSED GENERAL PRESSURE DROP AND HEAT TRANSFER CORRELATIONS FOR LAMINAR FLOW IN A TOROIDAL COILED TUBE SYSTEM
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INVESTIGATION AND DEVELOPMENT OF PROPOSED GENERAL PRESSURE DROP AND HEAT TRANSFER CORRELATIONS FOR LAMINAR FLOW IN A TOROIDAL COILED TUBE SYSTEM

机译:环形管网中层流拟议的总压降与传热相关性的研究与开发

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In this paper, the laminar flow pressure drop and heat transfer correlations published and applied to plain, coiled tube heat exchanger systems are extensively investigated. It was found that most correlations obtained for toroidal geometric systems have been applied to the analysis of helical and spiral tube systems. While toroidal (and helical) coils have a constant radius of curvature about the coil center-point (and center-line), spiral coils have a continuously varying radius of curvature, in which the flow does not reach a typical fully developed flow condition. The centrifugal forces, arising from the curved flow path, contribute to the enhancement of heat transfer (at the cost of additional pressure drop) over straight tube heat exchangers of the same length. In this paper, using published correlations and available experimental test data for pressure drop and heat transfer in toroidal tube systems, the proposed general correlations are developed by using a filtered-mean multiple regression method. The Coiling Influence Factors for the friction factor and heat transfer, CIF_f and CIF_h, respectively; defined and used in the authors' previous works it was found that the deviations between the proposed and published correlations are within about 3% for friction factor and 5-20% for heat transfer, depending on working fluid. In order to assess the validity of applying the generalized correlations developed in this work for toroidal tube systems, onto other curved tube systems, a numerical analysis of toroidal coil systems, using the commercially available CFD package (Fluent 6) has been explicitly performed. A comparison is made between the CFD result for average heat transfer (CIF_h) with that predicted by the proposed general correlation for toroidal coils and available experimental data. As an extension of this work, a comparison of curved tube over straight tube heat exchanger effectiveness is made to highlight its use as a design optimization parameter and motivation for additional coiled tube heat exchanger research.
机译:在本文中,广泛研究了层流压力降和传热相关性,并将其应用于普通的盘管式换热器系统。已经发现,对于环形几何系统获得的大多数相关性已被应用于螺旋和螺旋管系统的分析。环形(和螺旋形)线圈绕线圈中心点(和中心线)具有恒定的曲率半径,而螺旋形线圈具有连续变化的曲率半径,在这种情况下,流量无法达到典型的完全展开的流量条件。由弯曲的流动路径产生的离心力有助于在相同长度的直管式热交换器上增强热传递(以增加的压降为代价)。在本文中,利用已发表的相关性和可用的环形管系统中压降和传热的实验测试数据,通过使用滤波均值多元回归方法建立了拟议的一般相关性。摩擦系数和传热的线圈影响系数分别为CIF_f和CIF_h。在作者以前的工作中定义和使用的结果表明,根据工作流体的不同,建议的和已公布的相关性之间的偏差在摩擦系数的范围内约为3%,对于传热的偏差在5-20%之内。为了评估在这项工作中开发的用于环形管系统的广义相关性在其他弯曲管系统上的有效性,已使用市售CFD套件(Fluent 6)明确进行了环形线圈系统的数值分析。将平均传热的CFD结果(CIF_h)与建议的环形线圈一般相关性预测的结果和可用的实验数据进行了比较。作为这项工作的扩展,比较了弯管与直管式换热器的有效性,以突出其作为设计优化参数的用途以及其他盘管式换热器研究的动机。

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