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Heat transfer enhancement using streamlined tubes in polymer heat exchangers.

机译:在聚合物换热器中使用流线型管增强传热。

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摘要

Tubes with streamlined outer surface, such as elliptical, lenticular and teardrop shapes, are considered for use in heat exchangers made of polymers. The objective of this study is to determine the effect of tube minor-to-major axis ratio and arrangement on pressure drop and heat transfer of streamlined tubes in crossflow. The two-dimensional flow and temperature fields across individual and banks of streamlined tubes are simulated in the subcritical flow regime. For unsteady flow across individual streamlined tubes, both drag and Nusselt number decrease as the minor-to-major axis ratio is decreased. For banks of streamlined tubes, the pressure drop decreases as the gap-to-diameter ratio is increased due to the decrease in the local pressure gradient in the gap. For banks of streamlined tubes with a gap-to-diameter ratio of 0.25, the pressure drop increases as the minor-to-major axis ratio is decreased. As the gap-to-diameter ratio is increased, banks of streamlined tubes behave like individual tubes; the pressure drop decreases as the minor-to-major axis ratio is decreased. Compared with banks of circular tubes, banks of streamlined tubes always reduce pressure drop. The average heat transfer coefficient of banks of streamlined tubes is reduced as the minor-to-major axis ratio of the tubes is decreased or the gap-to-diameter ratio is increased.; To use the streamlined tubes in a heat exchanger, tube wall thickness must be selected to withstand the internal fluid pressure and minimize the thermal resistance. Mechanical design curves are provided which related to tube deformation and strain with the tube geometry, material properties and internal pressure load. The heat transfer of streamlined tubes with nonuniform wall thickness is evaluated using a tube efficiency, which depends only on the tube geometry and the Biot number. The tube efficiency is calculated based on a two-dimensional conduction analysis and varies from 0 to 1.; Streamlined tubes can be used in polymer heat exchangers to reduce pressure drop. However, the heat transfer of streamlined tubes may be less than circular tubes because of the added conductive resistance. Heat transfer of streamlined tubes can be improved by increasing the material conductivity or modulus.
机译:具有流线型外表面(例如椭圆形,双凸透镜和泪滴形)的管被认为可用于由聚合物制成的热交换器。这项研究的目的是确定管道短轴与长轴之比和布置对流线型管道中压降和传热的影响。在亚临界流态下,模拟了流线型管的单个和排的二维流场和温度场。对于流经各个流线型管的不稳定流量,随着短轴与长轴之比的减小,阻力和努塞尔数均减小。对于流线型的管束,由于间隙中局部压力梯度的减小,随着间隙直径比的增加,压降减小。对于具有0.25的间隙直径比的流线型管束,随着短轴与长轴之比的减小,压降增加。随着间隙直径比的增加,流线型管束的行为就像单个管一样。随着短轴与长轴之比的减小,压降减小。与圆形管束相比,流线形管束总是可以减少压降。当流线管的短轴与长轴之比减小或间隙直径比增大时,流线型管束的平均传热系数减小。为了在热交换器中使用流线型管,必须选择管壁厚度以承受内部流体压力并使热阻最小。提供了机械设计曲线,这些曲线与管的变形和应变以及管的几何形状,材料特性和内部压力载荷有关。使用管效率评估具有不均匀壁厚的流线型管的热传递,该效率仅取决于管的几何形状和比奥数。管效率是基于二维传导分析计算的,范围从0到1。流线型管可用于聚合物热交换器,以减少压降。然而,由于增加的导电电阻,流线型管的热传递可能小于圆形管。流线型管的热传递可以通过增加材料的电导率或模量来改善。

著录项

  • 作者

    Li, Zhihua.;

  • 作者单位

    University of Minnesota.;

  • 授予单位 University of Minnesota.;
  • 学科 Engineering Mechanical.
  • 学位 Ph.D.
  • 年度 2005
  • 页码 152 p.
  • 总页数 152
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 机械、仪表工业;
  • 关键词

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