Consider a cogeneration system operating as illustrated in Fig. 8.14. The steam generator provides a $10^{6} \mathrm{~kg} / \mathrm{h}$ of steam at $8 \mathrm{MPa}, 480^{\circ} \mathrm{C}$, of which $4 \times 10^{5} \mathrm{~kg} / \mathrm{h}$ is extracted between the first and second turbine stages at $1 \mathrm{MPa}$ and diverted to a process heating load. Condensate returns from the process heating load at $0.95 \mathrm{MPa}, 120^{\circ} \mathrm{C}$ and is mixed with liquid exiting the lower-pressure pump at $0.95 \mathrm{MPa}$. The entire flow is then pumped to the steam generator pressure. Saturated liquid at $8 \mathrm{kPa}$ leaves the condenser. The turbine stages and the pumps operate with isentropic efficiencies of 86 and $80 \%$, respectively. Determine
(a) the heating load, in $\mathrm{kJ} / \mathrm{h}$.
(b) the power developed by the turbine, in $\mathrm{kW}$. (c) the rate of heat transfer to the working fluid passing through the steam generator, in $\mathrm{kJ} / \mathrm{h}$.