Enhanced heat transfer due to curvature-induced lateral vortices in laminar flows in sinusoidal corrugated-plate channels

• Published in: International journal of heat and mass transfer Vol. 47; no. 10; pp. 2283 - 2292
• Main Authors: Metwally, H.M., Manglik, R.M.
• Format: Journal Article
• Language: English
• Published: Oxford Elsevier Ltd 01.05.2004; Elsevier
• Subjects: Applied sciences; Devices using thermal energy; Energy; Energy. Thermal use of fuels; Exact sciences and technology; Heat exchangers (included heat transformers, condensers, cooling towers); Temperature distribution; Forced convection; Nusselt number; Pipe flow; Laminar flow; Pressure drop; Heat exchanger; Compact heat exchanger; Numerical simulation; Wavy wall; Stream line; Vortex; Curvature; Heat transfer; Finite difference method; Parallel plate
• ISSN: 0017-9310; 1879-2189
• DOI: 10.1016/j.ijheatmasstransfer.2003.11.019

Laminar periodically developed forced convection in sinusoidal corrugated-plate channels with uniform wall temperature, and single-phase constant property flows is considered. Numerical solutions are obtained using the control-volume finite-difference method for a wide range of channel corrugation aspect ratios (0⩽ γ⩽1), and flow rates (10⩽ Re⩽1000) of viscous liquids ( Pr=5, 35, and 150). The flow field is found to be strongly influenced by γ and Re, and it displays two distinct regimes: a low Re or γ undisturbed laminar-flow regime, and a high Re or γ swirl-flow regime. In the no-swirl regime, the flow behavior is very similar to that in fully developed straight-duct flows with no cross-stream disturbance. In the swirl regime, flow separation and reattachment in the corrugation troughs generates transverse vortex cells that grow spatially with Re and γ, and the transition to this regime also depends on Re and γ. The mixing produced by these self-sustained transverse vortices is found to significantly enhance the heat transfer, depending upon γ, Re, and Pr, with a relatively small friction factor penalty. The consequent exchanger compactness and heat transfer enhancement effectiveness ( j/ f) is up to 5.5 times that for parallel-plate channels.