Abstract
This study investigates the turbulent free convection in a tank of water with the bottom surface being a smooth or a grooved surface and the top of the water surface exposed to ambient. The experiments for smooth surface was done with four values of AR, 3, 2, 1 and 0.5, whereas for grooved surface, values of AR are 3, 2 and 1. Here AR is the aspect ratio (=width of fluid layer/height of fluid layer). Heat flux at the bottom surface was from electrical heating. Experiments have been carried out for modified Rayleigh number in the range of \(2.5 \times 10^{8}\le Ra\le 3 \times 10^{12}\). The experimental results indicate that AR has significant effect on heat transport and hence sensitive to the nature and structures of the large scale mean flows of the system.
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Abbreviations
- \(A_{p}\) :
-
Cross-sectional area of the plates
- \(AR\) :
-
Aspect ratio = width of the water layer/height of the water layer
- \(D\) :
-
Height of the water layer
- \(g\) :
-
Acceleration due to gravity
- \(h_{R}\) :
-
Groove height
- \(k\) :
-
Thermal conductivity of water layer
- \(Q_{h}\) :
-
Heat input from heater
- \(q_{h}\) :
-
Heat flux from heater
- \(Q_{b}\) :
-
Heat output to the water
- \(q_{b}\) :
-
Heat flux entering the cell \(=Q_{b}/A_{p}\)
- \(Ra\) :
-
Rayleigh number based on water layer height\(\,=g\beta \Delta {T}D^{3}/\nu \alpha\).
- \(Ra^{*}\) :
-
Modified Rayleigh number \(=g\beta q_{b} D^{4}/(\nu \alpha k)\).
- \(Nu\) :
-
Nusselt number \(=D/\delta _{T}\)
- \(T_{b}\) :
-
Temperature of the plate next to the water
- \(T_{0}\) :
-
Temperature of core of the water layer
- \(\alpha\) :
-
Thermal diffusivity
- \(\beta\) :
-
Isobaric thermal expansion coefficient
- \(\delta _{T}\) :
-
Thermal boundary layer thickness
- \(\delta _{u}\) :
-
Viscous boundary layer thickness
- \(\lambda _{R}\) :
-
Groove spacing
- \(\nu\) :
-
Kinematic viscosity
- \(\Delta {T}\) :
-
Temperature difference between the bottom plate and core of the water layer \(=(T_{b}-T_{0})\)
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Kumar, L.G.K., Kumar, S.R. & Subudhi, S. Experimental study of the turbulent free convection over horizontal smooth or grooved surfaces in an open cavity. Heat Mass Transfer 52, 245–253 (2016). https://doi.org/10.1007/s00231-015-1559-6
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DOI: https://doi.org/10.1007/s00231-015-1559-6