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Modelling Turbulent Heat Transfer in a Natural Convection Flow

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Figure

Figure 1. Left: Configuration of the computational test case. Right: Computational mesh resolu- tion with (180 180××270)=8,748,000 cells
Figure 2. Instantaneous temperature (left) and vertical velocity (right) profile between the heated walls, linear temperature condition
Figure 4. Time-averaged profile of the local Nusselt number along the heated walls. Top: Adiabatic bc
Figure 5. Time-averaged vertical velocity profile at the xy-midplane, at x = 0.75 m, z = 0.75 m and different heights
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