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Instrumentation and Process Control Question on Measurement of process variables

Consider the surge drum in the figure. Initially, the system is at steady state with a hold-up V=5V = 5 m³, which is 50% of the full tank capacity, VfullV_{\text{full}}, and volumetric flow rates Fin=Fout=1\vec{F}_{\text{in}} = \vec{F}_{\text{out}} = 1 m³/h. The high hold-up alarm limit Vhigh=0.8VfullV_{\text{high}} = 0.8 V_{\text{full}} while the low hold-up alarm limit Vlow=0.2VfullV_{\text{low}} = 0.2 V_{\text{full}}. A proportional (P-only) controller manipulates the outflow to regulate the hold-up VV as Fout=Kc(VV)+Fout\vec{F}_{\text{out}} = K_c (V - \vec{V}) + \vec{F}_{\text{out}}. At t=0t = 0, Fin\vec{F}_{\text{in}} increases as a step from 1 m³/h to 2 m³/h. Assume linear control valves and instantaneous valve dynamics. Let KcminK_c^{\text{min}} be the minimum controller gain that ensures VV never exceeds VhighV_{\text{high}}. The value of KcminK_c^{\text{min}}, in h1^{-1}, rounded off to 2 decimal places, is _____.
surge drum

Answer

The correct Answers is :0.32 or 0.34 Approx