Solve it by MATLAB SIMULINK please.

Project Requirements

Draw a block diagram for the above process.

Simulate open loop response for the above process subjected to step change of

magnitude $2.$

From the open loop response, Identify FOPTD models using $63\mathrm{.}2\%$ and fraction

incomplete methods.

Compare the real response and response from the approximated FOPTD model.

Design a PI and PID controller using Ziegler$-$Nichols $($Z$-$N$)$ and Tyreus$-$Luyben $($T$-$L$)$ tuning

methods. The ultimate gain should be determined using the Routh Array method. As

Routh Array method requires the use of Pade approximation, the ultimate gain identified

using this method should be taken as an estimate $($initial guess$).$ The actual ultimate gain

and ultimate period should be found by performing closed$-$loop tests on the identified

model $($and not on the real plant$).$

Compare the performance of the PI and PID controller and comment on what happens

when derivative action is added to the controller.

Compare the performance of Z$-$N and T$-$L methods subjected to step change and

disturbance in steam pressure. Explain and justify the performance of the controller

designed by two methods using the knowledge of process control you learned in this

course.

Design a PI controller using Skogestad's IMC rules. Compare its performance with that of

the controller designed using the Z$-$N and T$-$L tuning methods.

Use your knowledge about PID controller to fine tune PID parameters to come up with

your own PID controller parameters, which gives very good performance $($minimum

overshoot and reasonably fast response$).$

tau$\_(1)=5,$tau$\_(2)=3,$tau$\_(3)=2,$tau$\_(4)=10$