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TECHNICAL PAPERS: Heat Transfer Enhancement

Three-Dimensional Simulations of Enhanced Heat Transfer in a Flat Passage Downstream From a Grooved Channel

[+] Author and Article Information
M. Greiner

University of Nevada, Reno, Nevada 89557e-mail: greiner@unr.edu

P. F. Fischer, H. M. Tufo

Mathematics and Computer Science Division, Argonne National Laboratory, Argonne, IL 60637

R. A. Wirtz

University of Nevada, Reno, Nevada 89557

J. Heat Transfer 124(1), 169-176 (Jun 15, 2001) (8 pages) doi:10.1115/1.1418371 History: Received May 17, 2000; Revised June 15, 2001
Copyright © 2002 by ASME
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References

Webb, R. L., 1994, Principles of Enhanced Heat Transfer, John Wiley & Sons, New York.
Ghaddar,  N. K., Korczak,  K., Mikic,  B. B., and Patera,  A. T., 1986, “Numerical Investigation of Incompressible Flow in Grooved Channels: Part 1—Stability and Self-Sustained Oscillations,” J. Fluid Mech., 168, pp. 541–567.
Greiner,  M., 1991, “An Experimental Investigation of Resonant Heat Transfer Enhancement in Grooved Channels,” Int. J. Heat Mass Transf., 24, pp. 1383–1391.
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Karniadakis,  G. E., Mikic,  B. B., and Patera,  A. T., 1988, “Minimum-Dissipation Transport Enhancement by Flow Destabilization: Reynolds Analogy Revisited,” J. Fluid Mech., 192, pp. 365–391.
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Greiner,  M., Chen,  R.-F., and Wirtz,  R. A., 1989, “Heat Transfer Augmentation Through Wall-Shaped-Induced Flow Destabilization,” ASME J. Heat Transfer, 112, pp. 336–341.
Greiner,  M., Chen,  R.-F., and Wirtz,  R. A., 1991, “Enhanced Heat Transfer/Pressure Drop Measured From a Flat Surface in a Grooved Channel,” ASME J. Heat Transfer, 113, pp. 498–500.
Wirtz,  R. A., Huang,  F., and Greiner,  M., 1999, “Correlation of Fully Developed Heat Transfer and Pressure Drop in a Symmetrically Grooved Channel,” ASME J. Heat Transfer, 121, pp. 236–239.
Greiner,  M., Spencer,  G., and Fischer,  P. F., 1998, “Direct Numerical Simulation of Three-Dimensional Flow and Augmented Heat Transfer in a Grooved Channel,” ASME J. Heat Transfer, 120, pp. 717–723.
Greiner,  M., Faulkner,  R. J., Van,  V. T., Tufo,  H. M., and Fischer,  P. F., 2000, “Simulations of Three-Dimensional Flow and Augmented Heat Transfer in a Symmetrically Grooved Channel,” ASME J. Heat Transfer, 122, pp. 653–660.
Blair,  M. F., 1983, “Influence of Free-Stream Turbulence on Turbulent Boundary Layer Heat Transfer and Mean Profile Development: Part I—Experimental Data; Part II—Analysis of Results,” ASME J. Heat Transfer, 105, pp. 33–47.
Maciejewski,  P. K., and Moffat,  R. J., 1992, “Heat Transfer with Very High Free-Stream Turbulence: Part I—Experimental Data; Part II—Analysis of Results,” ASME J. Heat Transfer, 114, pp. 827–839.
Greiner,  M., Chen,  R.-F., and Wirtz,  R. A., 1995, “Augmented Heat Transfer in a Recovery Passage Downstream From a Grooved Section: An Example of Uncoupled Heat/Momentum Transport,” ASME J. Heat Transfer, 117, pp. 303–308.
Huang, F., 1998, “Experimental Investigation of Fully-Developed Augmented Convection in a Symmetrically Grooved Channel,” Masters of Science Degree thesis, University of Nevada, Reno.
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Fischer,  P. F., 1997, “An Overlapping Schwarz Method for Spectral Element Solution of the Incompressible Navier-Stokes Equations,” J. Comput. Phys., 133, pp. 84–101.
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Figures

Grahic Jump Location
Regionally averaged pressure gradient versus Reynolds number and location
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Regionally averaged Nusselt number versus pumping power
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Spectral element mesh. (a) Periodic groove domain. (b) Groove/flat domain. The z-direction width of both domains is W.
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Surfaces of v-velocity at y=H/2. (a) Re=405. (b) Re=509. (c) Re=640. (d) Re=764.
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Centerline unsteady velocity versus location and Reynolds number.
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Centerline velocity versus axial location and Reynolds number
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Centerline Nusselt number versus axial location
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Bulk Nusselt number versus axial location
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Regionally averaged Nusselt number versus Reynolds number and location
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Local dimensionless pressure gradient versus axial location and Reynolds number

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