Consider the surge drum in the figure. Initially, the system is at steady state with a hold-up \( \bar{V} = 5 \, \text{m}^3 \), which is \( 50\% \) of full tank capacity, \( V_{\text{full}} \), and volumetric flow rates \( F_{\text{in}} = F_{\text{out}} = 1 \, \text{m}^3/\text{h} \). The high hold-up alarm limit \( V_{\text{high}} = 0.8 V_{\text{full}} \) while the low hold-up alarm limit \( V_{\text{low}} = 0.2 V_{\text{full}} \). A proportional (P-only) controller manipulates the outflow to regulate the hold-up as \( F_{\text{out}} = K_c (V - \bar{V}) + F_{\text{out} \). At \( t = 0 \), \( F_{\text{in}} \) increases as a step from \( 1 \, \text{m}^3/\text{h} \) to \( 2 \, \text{m}^3/\text{h} \). Assume linear control valves and instantaneous valve dynamics. Let \( K_c^{\text{min}} \) be the minimum controller gain that ensures \( V \) never exceeds \( V_{\text{high}} \). The value of \( K_c^{\text{min}} \), in \( \text{h}^{-1} \), rounded off to 2 decimal places, is:}
\includegraphics[width=0.5\linewidth]{q63 CE.PNG}