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A numerical and experimental study on turbulent natural convection in a differentially heated cavity

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Figure

Figure 1: Schematic representation of the cavity
Figure 2: Comparison of velocity and temperature profile at RaH = 6.4 · 108
Figure 3: Comparison of velocity and temperature profile at RaH = 1010
Figure 4: Local Nusselt number along the heated wall, RaH = 6.4 · 108
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