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Natural convection heat transfer in heat exchangers with vertical helical coils.

机译:带有垂直螺旋形盘管的热交换器中的自然对流换热。

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摘要

Natural convection heat transfer was studied in shell-and-coil heat exchangers. One or more helical coils were installed in a cylindrical shell to form a natural convection shell-and-coil heat exchanger. A heated aqueous solution of 40% propylene glycol was pumped through the coils. Water from a storage tank circulated naturally on the shell side of the heat exchanger. The helical coils were made of copper tubes of 4.76, 6.35, 7.94 and 9.52 mm outer diameter. Coil outer diameter was varied from 35.7 to 74.5 mm and coil pitch from 1.00 to 5.96 tube diameters. Two shell diameters of 51 and 77 mm were tested and the shell height was either 382 or 762 mm. Experiments were conducted for glycol mass flow rates from 0.00185 to 0.0343 kg/s and heat transfer rates from 160 to 2300 W.The effects of tube diameter, coil diameter, coil pitch, shell diameter and shell height on the shell-side heat transfer coefficient were studied. Axial temperature profiles in the heat exchangers were analyzed. The shell-side heat transfer coefficient decreased with increasing coil surface area. The optimum dimensionless pitch for the coils was found to be in the range, 1.25
机译:在壳管式换热器中研究了自然对流换热。将一个或多个螺旋形线圈安装在圆柱壳中,以形成自然对流壳壳式热交换器。将加热的40%丙二醇水溶液泵入线圈。来自储水箱的水在热交换器的壳体侧自然循环。螺旋线圈由外径为4.76、6.35、7.94和9.52毫米的铜管制成。线圈外径在35.7到74.5毫米之间变化,线圈间距在1.00到5.96毫米之间。测试了两个直径分别为51和77毫米的外壳,外壳高度为382或762毫米。进行了乙二醇质量流量从0.00185至0.0343 kg / s,传热速率从160至2300 W的实验。管直径,盘管直径,盘管节距,壳直径和壳高度对壳侧传热系数的影响被研究了。分析了热交换器中的轴向温度分布。壳侧传热系数随着线圈表面积的增加而降低。发现线圈的最佳无量纲螺距在1.25的范围内

著录项

  • 作者

    Taherian, Hessam.;

  • 作者单位

    DalTech - Dalhousie University (Canada).;

  • 授予单位 DalTech - Dalhousie University (Canada).;
  • 学科 Engineering Mechanical.
  • 学位 Ph.D.
  • 年度 1998
  • 页码 218 p.
  • 总页数 218
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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