Consider the flow of saturated steam at \(270.1 \mathrm{kPa}\) that flows
through the shell side of a shell-and-tube heat exchanger while the water
flows through 4 tubes of diameter \(1.25 \mathrm{~cm}\) at a rate of \(0.25
\mathrm{~kg} / \mathrm{s}\) through each tube. The water enters the tubes of
heat exchanger at \(20^{\circ} \mathrm{C}\) and exits at \(60^{\circ}
\mathrm{C}\). Due to the heat exchange with the cold fluid, steam is condensed
on the tubes external surface. The convection heat transfer coefficient on the
steam side is \(1500 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), while the
fouling resistance for the steam and water may be taken as \(0.00015\) and
\(0.0001 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\), respectively. Using
the NTU method, determine \((a)\) effectiveness of the heat exchanger, \((b)\)
length of the tube, and \((c)\) rate of steam condensation.