Consider the following empirical model of a pilot-scale distillation column (Wood and Berry, 1973)
\left[ \begin{matrix} X_{D}(s) \\ X_{B}(s) \end{matrix}\right] = \begin{bmatrix} \frac{12.8e^{-s} }{16.7s+1} & \frac{-18.9e^{-3s} }{21s+1} \\ \frac{6.6e^{-7s} }{10.9s+1} & \frac{-19.4e^{-3s} }{14.4s+1} \end{bmatrix} \left[ \begin{matrix} R(s) \\ S(s) \end{matrix}\right] (18-12)where the notation is defined in Fig. 18.1b. Suppose that a multiloop control system consisting of two PI controllers is used. Compare the closed-loop set-point changes that result if the X_{D}-R/X_{B} -S pairing is selected and
(a) A set-point change is made in each loop with the other loop in manual
(b) The set-point changes are made with both controllers in automatic Assume that the controller settings are based on the ITAE tuning method for set-point changes in Chapter 12.