A counter-flow heat exchanger is stated to have an overall heat transfer
coefficient of \(284 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) when
operating at design and clean conditions. Hot fluid enters the tube side at
\(93^{\circ} \mathrm{C}\) and exits at \(71^{\circ} \mathrm{C}\), while cold fluid
enters the shell side at \(27^{\circ} \mathrm{C}\) and exits at \(38^{\circ}
\mathrm{C}\). After a period of use, built-up scale in the heat exchanger gives
a fouling factor of \(0.0004 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\). If
the surface area is \(93 \mathrm{~m}^{2}\), determine \((a)\) the rate of heat
transfer in the heat exchanger and \((b)\) the mass flow rates of both hot and
cold fluids. Assume both hot and cold fluids have a specific heat of \(4.2
\mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\).