Comparison of the Finite Volume and Lattice Boltzmann Methods for Solving Natural Convection Heat Transfer Problems inside Cavities and Enclosures

Figure 6

Nusselt number profile at hot wall.

(a) 0.00≤𝑌≤1.00

(b) 0.00≤𝑌≤0.20

(c) 0.20≤𝑌≤0.30

(d) 0.30≤𝑌≤0.80

(e) 0.80≤𝑌≤1.00