Hot combustion gases of a furnace are flowing through a concrete chimney
\((k=1.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) of rectangular cross
section. The flow section of the chimney is $20 \mathrm{~cm} \times 40
\mathrm{~cm}\(, and the thickness of the wall is \)10 \mathrm{~cm}$. The average
temperature of the hot gases in the chimney is \(T_{i}=280^{\circ} \mathrm{C}\),
and the average convection heat transfer coefficient inside the chimney is
\(h_{l}=75 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The chimney is
losing heat from its outer surface to the ambient air at $T_{0}=15^{\circ}
\mathrm{C}\( by convection with a heat transfer coefficient of \)h_{o}=18
\mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ and to the sky by radiation.
The emissivity of the outer surface of the wall is \(\varepsilon=0.9\), and the
effective sky temperature is estimated to be \(250 \mathrm{~K}\).
Using the finite difference method with \(\Delta x=\Delta y=10 \mathrm{~cm}\)
and taking full advantage of symmetry, \((a)\) obtain the finite difference
formulation of this problem for steady two-dimensional heat transfer, (b)
determine the temperatures at the nodal points of a cross section, and \((c)\)
evaluate the rate of heat loss for a \(1-m\)-long section of the chimney.