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Study of Laminar Flow Forced Convection Heat Transfer Behavior of a Phase Change Material Fluid

机译:相变材料流体的层流强迫对流换热行为研究

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摘要

The heat transfer behavior of phase change material fluid under laminar flow conditions in circular tubes and internally longitudinal finned tubes are presented in this study. Two types of boundary conditions, including uniform axial heat flux with constant peripheral temperature and uniform axial and peripheral temperature, were considered in the case of circular tubes. An effective specific heat technique was used to model the phase change process assuming a hydrodynamically fully-developed flow at the entrance of the tube. Results were also obtained for the phase change process under hydro dynamically and thermally fully developed conditions. In case of a smooth circular tube with phase change material (PCM) fluid, results of Nusselt number were obtained by varying the bulk Stefan number. The Nusselt number results were found to be strongly dependent on the Stefan number. In the case of a finned tube two types of boundary conditions were studied. The first boundary condition had a uniform axial heat flux along the axis of the tube with a variable temperature on the peripheral surface of the tube. The second boundary condition had a constant temperature on the outer surface of the tube. The effective specific heat technique was again implemented to analyze the phase change process under both the boundary conditions. The Nusselt number was determined for a tube with two fins with different fin height ratios and fin thermal conductivity values. It was determined that the Nusselt number was strongly dependent on the Stefan number, fin thermal conductivity value, and height of the fins. It was also observed that for a constant heat axial flux boundary condition with peripherally varying temperature, the phase change slurry with the internally finned tube performed better than the one without fins. A similar trend was observed during the phase change process with internal fins under the constant wall temperature boundary condition.
机译:本文研究了相变材料流体在层流条件下在圆形管和内部纵向翅片管中的传热行为。对于圆管,考虑了两种边界条件,包括均匀的轴向热通量和恒定的外围温度,以及均匀的轴向和外围温度。假定管入口处有流体动力学充分发展的流动,则使用有效的比热技术对相变过程进行建模。还获得了在水动力和热充分发展条件下相变过程的结果。在具有相变材料(PCM)流体的光滑圆形管的情况下,通过改变整体Stefan数获得Nusselt数的结果。发现Nusselt数结果强烈依赖于Stefan数。对于翅片管,研究了两种边界条件。第一边界条件具有沿着管的轴线的均匀的轴向热通量,并且在管的外围表面上具有可变的温度。第二边界条件在管的外表面上具有恒定的温度。再次采用有效的比热技术来分析两个边界条件下的相变过程。对于具有两个具有不同鳍高比和鳍热导率值的鳍的管,确定了努塞尔数。可以确定,努塞尔数在很大程度上取决于Stefan数,鳍片导热系数值和鳍片高度。还观察到,对于温度随周向变化而恒定的轴向热通量边界条件,具有内部翅片管的相变浆料的性能要优于没有翅片的相变浆料。在恒定壁温边界条件下,内部翅片在相变过程中观察到类似的趋势。

著录项

  • 作者

    Ravi Gurunarayana;

  • 作者单位
  • 年度 2010
  • 总页数
  • 原文格式 PDF
  • 正文语种 en_US
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