Using a generic PI transfer function and the transfer functions for the process, the control valve and the measuring device as determined in Tutorial 5.
Problem 2.Consider the stirred tank vessel from Problem 1 of Tutorial 5.Up to time 0 the process is at steady state. At time 0 there is a step change in the influent flow rate, i.e. 𝐹𝑖(𝑡)increases by 0.001 m3/s.Using Simulink for the simulations, carry out the following:a)Build in Simulinkthe closed loop block-diagram for the controlled […]