Optimization study and heat transfer comparison of staggered circular and elliptic tubes in forced convection

Abstract In this study, a two-dimensional (2-D) heat transfer analysis was performed in circular and elliptic tube heat exchangers. The finite element method was used to discretize the fluid flow and heat transfer governing equations and a 2-D isoparametric, four-noded, linear element was implemented for the finite element analysis program, FEAP (O.C. Zienkiewicz, R.L. Taylor, The Finite Element Method, vol. 1, McGraw-Hill, London, 1989, Chapter 15). The numerical results for the equilateral triangle staggering configuration, obtained with the new element were then validated qualitatively by means of direct comparison to previously published experimental results for circular tubes heat exchangers (G. Stanescu, A.J. Fowler, A. Bejan, Int. J. Heat Mass Transfer 39 (2) (1996) 311–317). Next, a numerical geometric optimization was conducted to maximize the total heat transfer rate between the given volume and the given external flow both for circular and elliptic arrangements, for general staggering configurations. The results are reported for air in the range 300⩽ReL⩽800, where L is the swept length of the fixed volume. Circular and elliptical arrangements with the same flow obstruction cross-sectional area were compared on the basis of maximum total heat transfer. The effect of ellipses eccentricity was also investigated. A relative heat transfer gain of up to 13% is observed in the optimal elliptical arrangement, as compared to the optimal circular one. The heat transfer gain, combined with the relative pressure drop reduction of up to 25% observed in previous studies (H. Brauer, Chem. Process Eng., August (1964) 451–460; S.N. Bordalo, F.E.M. Saboya, Determinacao experimental dos coeficientes de perda de carga em trocadores de calor de tubos circulares e elipticos aletados, in: Proceedings of the 13th COBEM, Congresso Brasileiro de Engenharia Mec a nica (in Portuguese), Belo Horizonte, Brasil, 1995) show that the elliptical arrangement has the potential for a considerably better overall performance than the traditional circular one.

[1]  A. Bejan Convection Heat Transfer , 1984 .

[2]  Adrian Bejan,et al.  Forced convection in banks of inclined cylinders at low Reynolds numbers , 1994 .

[3]  A. Bejan,et al.  The optimal spacing of cylinders in free-stream cross-flow forced convection , 1996 .

[4]  Adrian Bejan,et al.  Optimal geometric arrangement of staggered plates in forced convection , 1997 .

[5]  Roy W. Knight,et al.  Optimal Thermal Design of Forced Convection Heat Sinks-Analytical , 1991 .

[6]  Adrian Bejan,et al.  Optimal Spacing Between Pin Fins With Impinging Flow , 1996 .

[7]  A. Bejan,et al.  The optimal spacing of parallel plates cooled by forced convection , 1992 .

[8]  W. Rohsenow,et al.  Thermally Optimum Spacing of Vertical, Natural Convection Cooled, Parallel Plates , 1984 .

[9]  Thomas J. R. Hughes,et al.  A simple scheme for developing ‘upwind’ finite elements , 1978 .

[10]  Leroy S. Fletcher,et al.  Free Convection Between Series of Vertical Parallel Plates With Embedded Line Heat Sources , 1991 .

[11]  Adrian Bejan,et al.  Optimal Arrays of Pin Fins and Plate Fins in Laminar Forced Convection , 1993 .

[12]  F. Saboya,et al.  Performance of one- and two-row tube and plate fin heat exchangers , 1984 .

[13]  J. Reddy,et al.  The Finite Element Method in Heat Transfer and Fluid Dynamics , 1994 .

[14]  Ephraim M Sparrow,et al.  Experiments on a Three-Row Fin and Tube Heat Exchanger , 1976 .

[15]  J. Z. Zhu,et al.  The finite element method , 1977 .

[16]  Roy W. Knight,et al.  Optimal thermal design of air cooled forced convection finned heat sinks-experimental verification , 1992 .

[17]  Leroy S. Fletcher,et al.  The Effect of Plate Spacing on Free Convection Between Heated Parallel Plates , 1992 .

[18]  Luiz Alberto Oliveira Rocha,et al.  A comparative study of elliptical and circular sections in one- and two-row tubes and plate fin heat exchangers , 1997 .

[19]  Adrian Bejan,et al.  The optimal spacing between horizontal cylinders in a fixed volume cooled by natural convection , 1995 .

[20]  Wing Kam Liu,et al.  Finite Element Analysis of Incompressible Viscous Flows by the Penalty Function Formulation , 1979 .