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Journal of Enhanced Heat Transfer

Theory and Application in High Performance Heat and Mass Transfer 

ISSN for PRINT: 1065-5131

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$577.00

Issues per year:

4

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2004, Volume11

Issue 4

  232 pages  

DOI: 10.1615/JEnhHeatTransf.v11.i4   

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  • Numerical Study on Low Reynolds Number Convection in Alternate Elliptical Axis Tube
  • Ji-An Meng
    School of Aerospace, Department of Engineering Mechanics, Education Ministry Key Lab of Enhanced Heat Transfer and Energy Conservation, Tsinghua University, Beijing 100084, China

    Xing-Gang Liang
    Department of Engineering Mechanics, Education Ministry Key Lab of Enhanced Heat Transfer and Energy Conservation, Tsinghua University, Beijing 100084, China

    Zhi-Xin Li
    School of Aerospace, Department of Engineering Mechanics, Education Ministry Key Lab of Enhanced Heat Transfer and Energy Conservation, Tsinghua University, Beijing 100084, China

    Zeng-Yuan Guo
    Department of Engineering Mechanics, Education Ministry Key Lab of Enhanced Heat Transfer and Energy Conservation, Tsinghua University, Beijing 100084, China


    ABSTRACT

    This work numerically investigates the convection of the novel alternate elliptical axis tube by FLUENT 6.0 with laminar, Reynolds stress, and RNG k-ε models. The Nusselt numbers are found to be increased 100−500% for Re=500−2300 with low cost in resistance increase. The enhancement is due to the multi-longitudinal vortices. The comparison with experiments for Re = 500−10,000 shows that the Nusselt number obtained from different models all agree well with experiments. As for the resistance coefficient prediction, the Reynolds stress model is very close to the experiments for Re = 500−2500, and the RNG k-ε model is very close to experiments for Re < 4000.

    DOI: 10.1615/JEnhHeatTransf.v11.i4.80

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