UFR 3-07 References

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Natural and mixed convection boundary layers on
vertical heated walls (B)

Underlying Flow Regime 3-07 © copyright ERCOFTAC 2004


References

Axcell, B.P. (1975), “The effect of buoyancy on turbulent forced convection”, Ph. D. Thesis, Manchester University.

Brown, C.K. and Gauvin, W.H. (1965), “Combined free and forced convection, II. Heat transfer in opposing flow”, The Canadian J. Chem. Eng., Dec 1965, pp. 313-318.

Brown, C.K. and Gauvin, W.H. (1966), “Temperature profiles and fluctuations in combined free and forced convection flows”, Chem. Eng. Science, Vol. 21, pp. 961-970.

Buyukalaca, O. (1993), “On turbulent convective heat transfer”, Ph.D. Thesis, University of Manchester.

Byrne, J.E. and Ejiogu, E. (1971), “Combined free and forced convection heat transfer in a vertical pipe”, Paper C118171, Symposium on Heat and Mass Transfer by Combined Forced and Natural Convection, Inst. Mech. Engr. Manchester.

Carr, A.D., Connor, M.A. and Buhr, H.O. (1973), “Velocity, temperature and turbulence measurements in air pipe flow with combined free and forced convection”, Trans. ASME, J. Heat Transfer, Vol. 95, pp. 445-452.

Cotton, M.A. and Jackson, J.D. (1987), “Comparison between theory and experiment for turbulent flow of air in a vertical tube with interaction between free and forced convection”, Mixed Convection Heat Transfer &emdash; 1987 (eds. V. Prasad, I. Catton and P. Cheng), ASME publication HTD-84, 1987, pp. 43-50.

Craft, T.J., Gerasimov, A.V., Iacovides, H. and Launder, B.E. (2002), “Progress in the generalisation of wall function treatments”, Int. J. Heat and Fluid Flow, 23, No. 2, pp. 148-160.

Easby, J.P. (1978), “The effect of buoyancy on flow and heat transfer for a gas passing down a vertical pipe at low turbulent Reynolds numbers”, Int. J. Heat and Mass Transfer, Vol. 21, pp. 791-801.

Eckert, E.R. and Diaguila, A.J. (1954), “Convective heat transfer for mixed, free and forced flow through tubes”, Trans. ASME, Vol. 76, pp. 497-504.

Fewster, J. (1976), “Mixed forced and free convective heat transfer to supercritical pressure fluids flowing in vertical pipes”, Ph. D. Thesis, Manchester University.

Gerasimov, A.V. (2002), “CFD Quality and Trust, Development and Validation of an analytical wall function strategy for modelling forced, mixed and natural convection flows”, IMC report number PM/GNSR/5106.

Herbert, L.S. and Sterns, U.J. (1968), “An experimental investigation of heat transfer to water in film flow”, Canadian Journal of Chemical Engineering, Vol. 46, pp. 401-412.

Herbert, L.S. and Sterns, U.J. (1972), “Heat transfer in vertical tubes - interactions of forced and free convection”, Chemical Engineering Journal, Vol. 4, pp. 46-52.

Huang P.G. and Leschziner M.A. (1983), “An Introduction and Guide to the Computer Code TEAM”, Report TFD/83/9/(R), Thermofluids Division, Department of Mechanical Engineering, UMIST.

Jackson, J.D. and Fewster, J. (1977), “Enhancement of turbulent heat transfer due to buoyancy for downward flow of water in vertical tubes”, Heat Transfer and Turbulent Buoyant Convection, International Centre for Heat and Mass Transfer, Dubrovnik, Yugoslavia, 1976 (eds Spalding, D.B. and Afgan, N.), Hemisphere Publishing Corporation, Washington D.C., pp. 759-775.

Jackson, J.D. and Hall, W.B. (1979), “Influences of buoyancy on heat transfer to fluids flowing in vertical tubes under turbulent conditions”, Turbulent Forced Convection in Channels and Bundles, Theory and Applications to Heat Exchangers and Nuclear Reactors, Vol. 2, (eds. Kakac, S. and Spalding, D.B.), Advanced Study Institute Book, pp. 613-640.

Jackson, J.D., Cotton, M.A. and Romero, E. (1989), “Heat transfer from roughened surfaces under conditions of combined forced and free convection”, Paper presented at Eurotherm seminar no. 9, Heat Transfer in Single Phase Flows — Recent Developments and Enhancement, Ruhr-Universitat Bochum, Federal Republic of Germany.

Jackson, J.D, He, S., Xu, Z., and Wu, T. (2000), “CFD Quality and Trust — generic studies of thermal convection”, Technical report HTH/GNSR/5029, School of Engineering, University of Manchester.

Khosla, J., Hoffman, T.W. and Pollock, K.G. (1974), “Combined forced and natural convective heat transfer to air in a vertical tube”, Proc. 5th Int. Heat Transfer Conference, Tokyo, Paper NC4.4.

Launder, B.E. and Sharma, B.I. (1974), “Application of the energy-dissipation model of turbulence to the calculation of flow near a spinning disc”, Lett. Heat Mass Transfer, Vol. 1, pp. 131-138.

Leschziner, M.A. (1982), “An introduction and guide to the computer code PASSABLE”, Report, University of Manchester Institute of Science and Technology.

Li, J.K. (1994), “Studies of buoyancy influenced convective heat transfer to air in a vertical tube”, Ph. D.Thesis, University of Manchester.

Perkins, K.R. and McEligot, D.M. (1975), “Mean temperature profiles in heated laminarizing air flows”, Trans. ASME C., J. Heat Transfer, November 1975.

Petukhov, B.S. and Nolde, L.D. (1959), “Heat transfer to water in a vertical heated tube for upward and downward flow”, Teploenergetika, Vol. 6, pp. 72-80.

Petukhov, B.S. and Strigin, B.K. (1968), “Experimental investigation of heat transfer with viscous inertial-gravitational flow of a liquid in vertical tubes”, Teplofizika Vysokikh temperatur, Vol. 6, No. 5, pp. 933-937.

Polyakov, A.F. and Shindin, S.A. (1988), “Development of turbulent heat transfer over the length of vertical tubes in the presence of mixed air convection”, Int. J. Heat Mass Transfer, Vol. 31, pp. 987-992.

Rouai, N.M. (1987), “Influences of buoyancy and imposed flow transients on turbulent convective heat transfer in a tube”, Ph.D. Thesis, University of Manchester.

Steiner, A. (1971), “On the reverse transition of turbulent flow under the action of buoyancy forces”, J. Fluid Mech., Vol. 47, Part 3, pp. 71-75.

Vilemas, J.V., Poskas, P.S. and Kaupas, V.E. (1992), “Local heat transfer in a vertical gas-cooled tube with turbulent mixed convection and different heat fluxes”, Int. J. Heat Mass Transfer, Vol. 35, No. 10, pp. 2421-2428.

Yu, L.S.L. (1991), “A computational study of turbulent mixed convection in vertical tubes”, Ph. D. Thesis, Unversity of Manchester.


LIST OF FIGURES

Figure 1 Downward flow of air in a heated tube, inlet Re=14815, Gr=3.812x107, Bo=0.0499, Tw=83.3°C, Ta=23.1°C, outlet Tw=212.0°C, Ta=137.1°C. Also shown are predictions for a different set of conditions. CFD predictions by Gerasimov (2002).

Figure 2 Downward flow of air in a heated tube, inlet Re=7044, Gr=8.010x107, Bo=0.5573, Tw=58.3°C, Ta=20.5°C, outlet Tw=147.9°C, Ta=105.0°C. Also shown are predictions for a different set of conditions, inlet Re=5016, Gr=8.003x107, Bo=1.7816, Tw=72.7°C, Ta=20.9°C, outlet Tw=195.3°C, Ta=143.9°C. CFD predictions by Gerasimov (2002).

Figure 3 Downward flow of air in a heated tube, inlet Re=4097, Gr=6.800x107, Bo=3.0268, Tw=71.8°C, Ta=20.1°C, outlet Tw=194.4°C, Ta=147.7°C. CFD predictions by Gerasimov (2002).

Figure 4 Upward flow of air in a heated tube, inlet Re=15023, Gr=2.163x108, Bo=0.1124, Tw=74.0°C, Ta=19.1°C, outlet Tw=222.4°C, Ta=130.4°C. Also shown are predictions for a different set of parameters. CFD predictions by Gerasimov (2002).


© copyright ERCOFTAC 2004



Contributors: Mike Rabbitt - British Energy


Front Page

Description

Test Case Studies

Evaluation

Best Practice Advice

References