In a one-shell and eight-tube pass heat exchanger, the temperature of water
flowing at rate of \(50,000 \mathrm{lbm} / \mathrm{h}\) is raised from
\(70^{\circ} \mathrm{F}\) to \(150^{\circ} \mathrm{F}\). Hot air \(\left(c_{p}=0.25
\mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right)\) that flows on
the tube side enters the heat exchanger at \(600^{\circ} \mathrm{F}\) and exits
at \(300^{\circ} \mathrm{F}\). If the convection heat transfer coefficient on
the outer surface of the tubes is \(30 \mathrm{Btu} / \mathrm{h} \cdot
\mathrm{ft}^{2}{ }^{\circ} \mathrm{F}\), determine the surface area of the heat
exchanger using both LMTD and \(\varepsilon-\mathrm{NTU}\) methods. Account for
the possible fouling resistance of \(0.0015\) and \(0.001 \mathrm{~h} \cdot
\mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F} /\) Btu on water and air side,
respectively.