Consider the continuous stirred tank heater shown below, Tin Tout min Steam With, 1.2e -105 8p(s) = 0.9e -105 (60s +1)/5

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Consider The Continuous Stirred Tank Heater Shown Below Tin Tout Min Steam With 1 2e 105 8p S 0 9e 105 60s 1 5 1 (72.78 KiB) Viewed 75 times

Consider the continuous stirred tank heater shown below, Tin Tout min Steam With, 1.2e -105 8p(s) = 0.9e -105 (60s +1)/5s +1) igd(s)= 60s +1 Here, &p(s) and ga(s) are the transfer functions between the steam and the inlet temperature with the reactor temperature, respectively. For this process: 1. Draw the feedback control loop on the process schematic (i.e. P&ID) and develop the feedback control loop in a block diagram 2. Using the direct substitution method, design a Ziegler Nichols controller with P, PI and PID tuning values