菜单
  

     
    From the vibration analysis of STHE it is found that the
    tube length has major impact on shell acoustic frequency,
    the tube natural frequency, bundle cross flow, critical
    velocity, vortex shedding ratio. From Table 2 and Fig-
    ure 3 to  Figure 7, it can be concluded that up to mid
    span of the tube (i.e. 500 cm) the tube natural frequency,
    bundle cross flow, critical velocity, and vortex shedding
    ratio are gradually increasing & then decreases up to the
    end of tube length. Also, the mechanisms of flow-in-
    duced vibration are studied and the several main mecha-
    nisms are introduced. We finally come to the conclusion
    that the main parameter which largely affects the vibra-
    tions caused due to flow are dependent on unsupported
    tube length and varies at various locations across the tube
    length as unsupported tube length varies. The various
    other parameters which affect the flow induced vibration
    are critical velocity, natural frequency of tubes, cross-
    flow velocity and acoustic frequency.
     
    8. References
     
    [1]  H. Hiromitsu, M. Kouichi, N. Eiichi and F. Tohru, “Vor-
    tex Shedding from Tube Banks with Closely Mounted
    Serrated Fin,”  Journal of Environmentand Engineering,
    Vol. 6, No. 1, 2011, pp. 69-80. doi:10.1299/jee.6.69
    [2]  C. W. M. van der Geld and J. M. W. M. Schoonen, “De-
    sign Improvement of Shell  and Tube Heat Exchanger  
    based on Practical Experience and Numerical Analysis,”
    Design Report, Eindhoven University of Technology,
    Netherlands, 1991, pp. 74-87.  
    [3]  S. Wang, J. Wen and Y. Li, “An Experimental Investiga-
    tion of Heat Transfer Enhancement for a Shell-and-Tube
    Heat Exchanger,” Applied Thermal Engineering, Vol. 29
    No. 11-12, 2009, pp. 2433-2438.
    doi:10.1016/j.applthermaleng.2008.12.008
    [4]  V. K. Patel and R.V. Rao, “Design Optimization of Shell-
    and-Tube Heat Exchanger Using Particle Swarm Opti-
    mization Technique,” Applied Thermal Engineering, Vol.
    30, No. 11-12, 2001, pp. 1417-1425.
    doi:10.1016/j.applthermaleng.2010.03.001
    [5]  A. L. H. Costa and E. M. Queiroz, “Design Optimization
    of Shell and Tube Heat Exchangers,”  Applied Thermal
    Engineering, Vol. 28, No. 14-15, 2008, pp. 1798-1805.
    doi:10.1016/j.applthermaleng.2007.11.009
    [6]  R. Hosseini, A. Hosseini-Ghaffar and M. Soltani, “Ex-
    perimental Determination of  Shell Side Heat Transfer
    Coefficient and Pressure Drop for an Oil Cooler Shell-
    and-Tube Heat Exchanger with Three Different Tube
    Bundles,” Applied Thermal Engineering, Vol. 27, No. 5-6,
    2007, pp. 1001-1008.
    doi:10.1016/j.applthermaleng.2006.07.023
    [7]  V. Hejazi, M. A. Akhavan-Behabadi and A. Afshari,
    “Experimental Investigation of Twisted Tape Inserts Per-
    formance on Condensation Heat Transfer Enhancement
    and Pressure Drop,”  International Communications in
    Heat and Mass Transfer, Vol. 37, No. 9, 2010, pp. 1376-
    1387. doi:10.1016/j.icheatmasstransfer.2010.07.021
    [8]  I. Conté and X. F. Peng, “Numerical and Experimental
    Investigations of Heat Transfer Performance of Rectan-
    gular Coil Heat Exchangers,”  Applied Thermal Engi-
    neering, Vol. 29, No. 8-9, 2009, pp. 1799-1808.
    doi:10.1016/j.applthermaleng.2008.08.013
    [9]  Y. Li, X. Jiang, X. Huang, J. Jia and J. Tong, “Optimiza-
    tion of High-Pressure Shell-and-Tube Heat Exchanger for
    Syngas Cooling in an IGCC,”  International Journal of
    Heat and Mass Transfer, Vol. 53, No. 21-22, 2010, pp.
    4543-4551. doi:10.1016/j.ijheatmasstransfer.2010.04.038
     摘要:本论文将通过分析流体诱导振动来设计优化管壳式换热器,并提供简易的方法。流体诱导振动会造成管壳式换热器的管子破坏,而振动分析有助于其设计优化。流体诱导振动造成管子破坏的主要原因是管壳式换热器的尺寸,研究发现,当管壳式换热器尺寸增大时,它的表面积增大,管子的数量随之增加,因此,了解并且分析振动变得十分困难。此外,研究表明流体诱导振动分析是机械和传热设计的重要组成部分。细节设计、装配、检测与分析工作由阿法拉伐(印度)有限公司及Pune-10公司执行。
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