Abstract
A numerical study of a natural convection in a rectangular cavity with the low-Reynoldsnumber differential stress and flux model is presented. The primary emphasis of the study is placed on the investigation of the accuracy and numerical stability of the low-Reynolds-number differential stress and flux model for a natural convection problem. The turbulence model considered in the study is that developed by Peeters and Henkes (1992) and further refined by Dol and Hanjalic (2001), and this model is applied to the prediction of a natural convection in a rectangular cavity together with the two-layer model, the shear stress transport model and the time-scale bound\(\overline {v^2 } - f\) model, all with an algebraic heat flux model. The computed results are compared with the experimental data commonly used for the validation of the turbulence models. It is shown that the low-Reynolds-number differential stress and flux model predicts well the mean velocity and temperature, the vertical velocity fluctuation, the Reynolds shear stress, the horizontal turbulent heat flux, the local Nusselt number and the wall shear stress, but slightly under-predicts the vertical turbulent heat flux. The performance of the\(\overline {v^2 } - f\) model is comparable to that of the low-Reynolds-number differential stress and flux model except for the over-prediction of the horizontal turbulent heat flux. The two-layer model predicts poorly the mean vertical velocity component and under-predicts the wall shear stress and the local Nusselt number. The shear stress transport model predicts well the mean velocity, but the general performance of the shear stress transport model is nearly the same as that of the two-layer model, under-predicting the local Nusselt number and the turbulent quantities.
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Abbreviations
- gi :
-
Gravitational acceleration
- Gk :
-
Buoyancy generation term
- H:
-
Height of the cavity
- h:
-
Heat transfer coefficient
- k:
-
Turbulent kinetic energy
- kf :
-
Conductivity of fluid
- L:
-
Width of the cavity
- ni :
-
i-th component of normal vector at the wall
- Nu:
-
Nusselt number
- p:
-
Pressure
- Pk :
-
Generation term of turbulent kinetic energy
- Pθ :
-
Generation term of temperature variance
- Pr:
-
Prandtl number
- Prθ :
-
Turbulent Prandtl number
- Ra:
-
Rayleigh number
- RT :
-
Turbulent Reynolds number\(\left( { = \frac{{\rho k^2 }}{{\mu \varepsilon }}} \right)\)
- t:
-
Time
- T:
-
Time scale
- Ui :
-
Cartesian velocity components
- \(\overline {u_i u_j } \) :
-
Reynolds stresses
- Uτ :
-
Wall friction velocity\(\left( { = \left( {\frac{\mu }{\rho }\left| {\frac{{\partial U_P }}{{\partial x_n }}} \right|_w } \right)^{1/2} } \right)\)
- Xi :
-
Cartesian Coordinates
- xn :
-
Normal distance from the wall
- x + x :
-
Dimensionless normal distance from the\(\left( { = \frac{{\rho U_\tau x_n }}{\mu }} \right)\)
- β:
-
Gas expansion coefficient
- Δn :
-
Normal distance from the wall
- ε:
-
Dissipation rate of turbulent kinetic energy
- εθ:
-
Dissipation rate of temperature fluctuation
- γ:
-
Dynamic viscosity
- γM ij :
-
Pseudo eddy-viscosity for momentum equations
- γT j :
-
Pseudo eddy-viscosity for energy equation
- γT :
-
Turbulent eddy viscosity
- υ:
-
Kinematic viscosity
- ρ:
-
Density
- Θ:
-
Temperature
- \(\overline {\theta u_i } \) :
-
Turbulent heat fluxes
- \(\overline {\theta ^2 } \) :
-
Temperature variance
- H:
-
Pertaining to hot wall
- ε:
-
Pertaining to dissipation rate of turbulent kinetic energy
- θ:
-
Pertaining to temperature
- N-1 :
-
Pertaining to previous iteration level
- M:
-
Pertaining to momentum equation
- T:
-
Pertaining to energy equation
References
Ampofo, F. and Karayiannis, T. G., 2003, “Experimental Benchmark Data for Turbulent Natural Convection in an Air Filled Square Cavity,”Int. J. Heat Mass Transfer, Vol. 46, pp. 3551–3572.
Betts, P. L. and Bokhari, I. H., 2000, “Experiments on Turbulent Natural Convection in an Enclosed Tall Cavity,”Int. J. Heat Fluid Flow, Vol.21, pp. 675–683.
Boudjemadi, R., Maupu, V., Laurence, D., Quere and P. Le, 1997, “Budgets of Turbulent Stresses and Fluxes in a Vertical Slot Natural Convection Flow at Rayleigh Ra=105 and 5.4x 105,”Int. J. Heat Fluid Flow, Vol. 18, pp. 70–79.
Cheesewright, R., King, K. J. and Ziai, S., 1986, “Experimental Data for the Validation of Computer Codes for the Prediction of Two-Dimensional Buoyant Cavity Flows,”Proceeding of ASME Meeting, HTD, Vol. 60, pp. 75–81.
Chen, H. C. and Patel, V. C., 1988, “Near-Wall Turbulence Models for Complex Flows Including Separation,”AIAA J., Vol. 26, pp. 641–648.
Choi, S. K., 2003, “Evaluation of Turbulence Models for Natural Convection,”KAERI Internal Report, FS200-AR-01-R0-03, (in Korean).
Choi, S. K., Kim, E. K. and Kim, S. O., 2004, “Computation of Turbulent Natural Convection in a Rectangular Cavity with the\(k - \varepsilon - \overline {v^2 } - f\) 2-f Model,”Numer. Heat Transfer, Part B, Vol. 45, pp. 159–179.
Davidson, L. 1990, “Calculation of the Turbulent Buoyancy-Driven Flow in a Rectangular Cavity Using an Efficient Solver and Two Different Low Reynolds Numberk-ε Turbulence Model,”Numer. Heat Transfer, Part A, Vol. 18, pp. 129–147.
Dol, H. S. and Hanjalic, K., 2001, “Computational Study of Turbulent Natural Convection in a Side-Heated Near-Cubic enclosure at a High Rayleigh Number,”Int. J. Heat Mass Transfer, Vol. 44, pp. 2323–2344.
Dol, H. S., Hanjalic, K. and Kenjeres, S., 1997, “A Comparative Assessment of the Second-Moment Differential and Algebraic Models in Turbulent Natural Convection,”Int. J. Heat Fluid Flow, Vol. 18, pp. 4–14.
Dol, H. S. Opstelten I. J., and Hanjalic, K., 2000, “Turbulent Natural Convection in a Side- Heated Near-Cubic Enclosure: Experiments and Model Computations,”Technical report APTFR/ 00-02, Thermal and Fluids Science Section, Department of Applied Physics, Delft University of Technology, Delft, The Netherlands.
Hanjalic, K., 2002, “One-Point Closure Models for Buoyancy-Driven Turbulent Flows,”Annu. Rev. Fluid Mech. Vol. 34, pp. 321–347.
Henkes, R. A. W. M. and Hoodendoorn, C. J., 1995, “Comparison Exercise for Computations of Turbulent Natural Convection in Enclosures,”Numer. Heat Transfer, Part B, Vol. 28, pp. 59–78.
Henkes, R. A. W. M., Van Der Vlugt and F. F. Hoodendoorn, C. J., 1991, “Natural-Convection Flow in a Square Cavity Calculated with Low- Reynolds-Number Turbulence Models,”Int. J. Heat Mass Transfer, Vol. 34, pp. 377–388.
Hsieh, K. J. and Lien, F. S., 2004, “Numerical Modeling of Buoyancy-Driven Turbulent Flows in Enclosures,”Int. J. Heat Fluid Flow, in press.
Ince, N. Z. and Launder, B. E., 1989, “On the Computation of Buoyancy-Driven Turbulent Flows in Rectangular Enclosures,”Int. J. Heat Fluid Flow, Vol. 10, pp. 110–117.
Ince, N. Z. and Launder, B. E., 1995, “Three- Dimensional and Heat-Loss Effects on Turbulent Flow in a Nominally Two-Dimensional Cavity,”Int. J. Heat Fluid Flow, Vol. 16, pp. 171–177.
Kenjeres, S., 1998, “NumericalModelling of Complex Buoyancy-Driven Flows,” Ph. D Thesis, Delft University of Technology, The Netherlands.
Kenjeres, S., and Hanjalic, K., 1995, “Prediction of Turbulent Thermal Convection in Concentric and Eccentric Annuli,”Int. J. Heat Fluid Flow, Vol. 16, pp. 429–439.
King, K.J., 1989, “TurbulentNatural Convection in Rectangular Air Cavities,” Ph. D Thesis, Queen Mary College, University of London, U. K.
Janssen, R. J. A., 1994, ”Instabilitiesin Natural- Convection flows in Cavities,” Ph. D thesis, Delft University of Technology, Delft, The Netherlands.
Lai, Y. G., and So, R. M. C., 1990, “Near-Wall Modeling of Turbulent Heat Fluxes,”Int. J. Heat Mass Transfer, Vol. 33, pp. 1429–1440.
Launder, B. E. and Sharma, B. I., 1974, “Application of the Energy Dissipation Model of Turbulence to the Calculation of Flow Near Spinning Disc,”Lett. In Heat and Mass Transfer, Vol. 1, pp. 131–138.
Lien, F. S., and Leschziner, M. A., 1991, “Second-Moment Modelling of Recirculating Flow with a Non-orthogonal Collocated Finite-Volume Algorithm,”Turbulent Shear Flows, Vol. 8, pp. 205–222.
Medic, G. and Durbin, P. A., 2002, “Toward Improved Prediction of Heat Transfer on Turbine Blades,”J. Turbomachinery, Vol. 124, pp. 187- 192.
Menter, F. R., 1994, “Two-Equation Eddy- Viscosity Turbulence Models for Engineering Applications,”AIAA Journal, Vol. 32, No. 8, pp. 1598–1604.
Opstelten, I. J., 1994, “ExperimentalStudy on Transition Characteristics of Natural- Convection Flow,” Ph. D thesis, Delft University of Technology, Delft, The Netherlands.
Patankar, S. V., 1980, “NumericalHeat Transfer and Fluid Flow” Hemisphere, New York, USA.
Peeters, T. W. J. and Henkes, R. A. W. M., 1992, “The Reynolds-Stress Model of Turbulence Applied to the Natural-Convection Boundary Layer along a Heated Vertical Plate,”Int. J. Heat Mass Transfer, Vol. 35, pp. 403–420.
Peng, S. H. and Davidson, L., 2001, “Large Eddy Simulation of Turbulent Buoyant Flow in a Confined Cavity,”Int. J. Heat Fluid Flow, Vol. 22, pp. 323–331.
Shikazo, N. and Kasagi, N., 1996, “Second Moment Closure for Turbulent Scalar Transport at Various Prandtl Numbers,”Int. J. Heat Mass Transfer, Vol. 39, pp. 2977–2987.
Shin, J. K., An, J. S. and Choi, Y. D. 2004, “Near Wall Modelling of Turbulent Heat Fluxes by Elliptic Equation.”Transactions of the Korean Society of Mechanical Engineers, Part B. Vol. 28, pp. 526–534.
Shin, J. K., Choi, Y. D. and Lee, G. H., 1993, “A Low-reynolds Number Second Moment Closure for Turbulent Heat Fluxes,”Transactions of the Korean Society of Mechanical Engineers, Part B. Vol. 17, pp. 3196–3207.
Tian, Y. S. and Karayiannis T. G., 2000, “Low Turbulence Natural Convection in an Air Filled Square Cavity part I: The Thermal and Fluid Flow Fields,”Int. J. Heat Mass Transfer, Vol. 43, pp. 849–866.
Tieszen, S., Ooi, P., Durbin, P. A. and Behnia, M., 1998, “Modeling of Natural Convection Heat Transfer,”Proc. Summer Program, Center of Turbulence Research, Stanford University, Stanford, CA, U. S. A., pp. 287–302.
Tsuji, T and Nagano, Y., 1987, “Turbulence Measurements in a Natural Convection Boundary Layer along a Vertical Flat Plate,”Int. J. Heat Mass Transfer, Vol. 31, pp. 2101–2111.
Van Leer, B., 1974, “Towards the Ultimate Conservative Difference Scheme: Monotonicity and Conservation Combined in a Second Order Scheme,”J. Comput. Phy., Vol. 14, pp. 361–370.
Versteegh, T.A.M. and Nieuwstat, F. T. M., 1998, “Turbulence Budgets of Natural Convection in an Infinite, Differentially Heated, Vertical Wall,”Int. J. Heat Fluid Flow, Vol. 19, pp. 135–149.
Zhu, J., 1991, “A Low-Diffusive and Oscillation Free Convection Scheme,”Comm. Appl. Numer. Methods, Vol. 7, pp. 225–232.
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Choi, SK., Kim, EK., Wi, MH. et al. Computation of a turbulent natural convection in a rectangular cavity with the low-reynolds-number differential stress and flux model. KSME International Journal 18, 1782–1798 (2004). https://doi.org/10.1007/BF02984327
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DOI: https://doi.org/10.1007/BF02984327