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Influence of alternating V-rows tube layout on thermal-hydraulic characteristics of twisted elliptical tube heat exchangers

机译:交替V型管布置对扭椭圆管热交换器热液压特性的影响

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摘要

An innovative alternating V-rows triangular tube layout was devised for the twisted elliptical tube heat exchangers to enhance heat transfer between adjacent tubes. Under the same tube circumference, altogether eleven twisted elliptical tube heat exchangers with two tube layouts, diverse aspect ratios of twisted elliptical tubes and different twisted pitches were constructed and simulated, including five coupling-vortex schemes, five parallel-vortex schemes and a smooth round tube scheme R10.8. Water with constant physical properties was adopted as the working fluid. Shell-side Reynolds number varies from 2000 to 10,000. The results show that the concurrent flow and the irregular channel in coupling-vortex schemes, and the larger aspect ratio and the smaller twisted pitch of twisted elliptical tubes help intensify turbulence and secondary flow. Compared with R10.8, the averaged Nu and Nu·f~(-1/3) of coupling-vortex scheme C14.2S50 are improved by 132.8% and 47.1%, respectively. Under shorter twisted pitch, smaller aspect ratio and lower Reynolds number, coupling-vortex schemes can acquire superior heat transfer capability than corresponding parallel-vortex schemes but will not increase manufacturing cost. Compared with P12.3S50, the maximum and averaged Nu of C12.3S50 are increased by 9.5% and 7.8% while the maximum and averaged Nu·f~(-1/3) are increased by 6.4% and 4.9%.
机译:设计了一种创新的交替V-Rows三角形管布局,用于扭曲的椭圆管热交换器,以增强相邻管之间的热传递。在相同的管圆周下,构造和模拟具有两个管布局的11个具有两个管布局的扭曲椭圆管热交换器,扭曲椭圆管的不同纵横比和不同的扭曲间距,包括五个耦合涡旋方案,五个平行涡旋方案和光滑的圆形方案管计划R10.8。采用恒定物理性质的水作为工作流体。壳牌雷诺数的数量从2000年变化到10,000。结果表明,耦合 - 涡旋方案中的并发流动和不规则通道,以及较大的纵横比和较小的扭曲椭圆管的扭曲间距有助于加强湍流和二次流动。与R10.8相比,偶联涡旋方案C14.2S50的平均Nu和Nu·F〜(-1/3)分别提高了132.8%和47.1%。在较短的扭曲间距,较小的纵横比和更低的雷诺数,耦合 - 涡旋方案可以获得比相应的平行涡流方案更高的传热能力,但不会增加制造成本。与P12.3S50相比,C12.3S50的最大和平均NU增加了9.5%和7.8%,而最大和平均NU·F·F〜(-1/3)增加了6.4%和4.9%。

著录项

  • 来源
    《International Journal of Heat and Mass Transfer》 |2020年第10期|120070.1-120070.14|共14页
  • 作者单位

    Engineering Research Center of BEEE Ministry of Education China jiangsu Provincial Key Laboratory of Solar Energy Science and Technology School of Energy and Environment Southeast University Nanjing 210096 China Department of Energy Science Lund University P.O. Box 118 SE-22100 Lund Sweden;

    Engineering Research Center of BEEE Ministry of Education China jiangsu Provincial Key Laboratory of Solar Energy Science and Technology School of Energy and Environment Southeast University Nanjing 210096 China;

    Department of Energy Science Lund University P.O. Box 118 SE-22100 Lund Sweden;

    Engineering Research Center of BEEE Ministry of Education China jiangsu Provincial Key Laboratory of Solar Energy Science and Technology School of Energy and Environment Southeast University Nanjing 210096 China;

    Engineering Research Center of BEEE Ministry of Education China jiangsu Provincial Key Laboratory of Solar Energy Science and Technology School of Energy and Environment Southeast University Nanjing 210096 China;

    Engineering Research Center of BEEE Ministry of Education China jiangsu Provincial Key Laboratory of Solar Energy Science and Technology School of Energy and Environment Southeast University Nanjing 210096 China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Twisted elliptical tube heat exchangers; Alternating V-rows triangle tube layout; Coupling-vortex; Spiral flow; Heat transfer enhancement;

    机译:扭曲的椭圆管换热器;交替的V-Rows三角管布局;耦合 - 涡旋;螺旋流动;传热增强;

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