ASSESSMENT OF A ONE-EQUATION TURBULENCE MODEL FOR STRONGLY HEATED GAS FLOWING UPWARD IN A VERTICAL TUBE

Adam H. Richards and Robert E. Spall

References

  1. [1] C.A. Bankston & D.M. McEligot, Turbulent and laminar heattransfer to gases with varying properties in the entry regionof circular ducts, International Journal of Heat and MassTransfer, 13, 1970, 319–344.
  2. [2] R.J. Moffat & W.M. Kays, A review of turbulent-boundary-layer heat transfer research at Stanford, Advances in HeatTransfer, 16, 1984, 241–365.
  3. [3] A.D. Carr, M.A. Connor, & H.O. Buhr, Velocity, temperatureand turbulence measurements in air for pipe flow with combinedfree and forced convection, Journal of Heat Transfer, 95, 1973,445–452.
  4. [4] D.M. McEligot, The effect of large temperature gradients onturbulent flow of gases in the downstream region of tubes, Ph.D.thesis, Stanford University, 1963. Also TID-19446.
  5. [5] D.P. Mikielewicz, A.M.Shehata, J.D. Jackson, & D.M.McEligot, Temperature, velocity and mean turbulence struc-ture in strongly heated gas flows – comparison of numericalpredictions with data, International Journal of Heat and MassTransfer, 45, 2002, 4333–4352.
  6. [6] K. Ezato, A.M. Shehata, T. Kunugi, & D.M. McEligot, Nu-merical prediction of transitional features of turbulent forcedgas flows in circular tubes with strong heating, Journal of HeatTransfer, 121, 1999, 546–555.
  7. [7] A.M. Shehata & D.M. McEligot, Mean structure in the viscouslayer of strongly-heated internal gas flows: measurements,International Journal of Heat and Mass Transfer, 41, 1998,4297–4313.75
  8. [8] K.R. Perkins, Turbulence structure in gas flow laminarizing byheating, Ph.D. thesis, University of Arizona, 1975.
  9. [9] A.M. Shehata, Mean turbulence structure in strongly heatedair flows, Ph.D. thesis, University of Arizona, 1984.
  10. [10] S. Satake, T. Kunugi, A.M. Shehata, & D.M. McEligot, Directnumerical simulation for laminarization of turbulent forcedgas flows in circular tubes with strong heating, InternationalJournal of Heat and Fluid Flow, 21, 2000, 526–534.
  11. [11] A.M. Shehata & D.M. McEligot, Turbulence structure in theviscous layer of strongly heated gas flows, Technical ReportINEL-95/0223, Idaho National Engineering Laboratory, 1995.
  12. [12] B.E. Launder & B. Sharma, Application of energy-dissipationmodel of turbulence to the calculation of flow near a spinningdisc, Lett & Heat Transfer, 1, 1974, 131–138.
  13. [13] A.H. Richards, R.E. Spall, & D.M. McEligot, An assessmentof turbulence models for strongly-heated internal gas flows,Proc. 15th IASTED Int. Conf. on Modeling and Simulation,Marina Del Rey, CA, March 1–3, paper 111, 2004, 119–124.
  14. [14] R.E. Spall, A.H. Richards, & D.M. McEligot, An assessment ofk − ω and v2 − f turbulence models for strongly heated internalgas flows, Numerical Heat Transfer: Part A: Applications, 46,2004, 831–849.
  15. [15] H.C. Chen & V.C. Patel, Near-wall turbulence models forcomplex flows including separation, AIAA, 26(6), 1988, 641–648.
  16. [16] B.E. Launder & D.B. Spalding, Lectures in mathematicalmodels of turbulence (Academic Press, London, England, 1972).
  17. [17] P.A. Durbin & B.A. Pettersson Reif, Statistical theory and mod-eling for turbulent flows (John Wiley & Sons Ltd, Chichester,England, 2001).
  18. [18] M. Wolfshtein, The velocity and temperature distributionin one-dimensional flow with turbulence augmentation andpressure gradient, Journal of Heat and Mass Transfer, 12,1969, 301–318.
  19. [19] F.W. Dittus & L.M.K. Boelter, Heat transfer in automobileradiators of the tubular type, Publication in Engineering.,University of California, Berkeley, 2, 1930, 443–461.
  20. [20] D.M. McEligot, L.W. Ormand, & H.C. Perkins, Internal lowReynolds number turbulent and transitional gas flow with heattransfer, Journal of Heat Transfer, 88, 1966, 239–245.

Important Links:

Go Back