Dynamic process and disturbance models are identified for the 2x2 dist
illation column described in the summary paper by Cott. Process models
are identified using both classical least squares and the newer AUDI
identification algorithm developed at the University of Alberta. The i
dentified models are validated and gain-adjusted in the frequency doma
in by comparing the magnitude spectrum of the models, \G(e(-i omega))\
, versus the spectrum obtained by fast Fourier transformation of the o
riginal plant I/O time series. The noise/disturbance models are identi
fied using standard time series tools and all models are verified by s
howing that the filtered residuals (measured process output minus mode
l based estimate of the output) are essentially white noise. The estim
ated SISO models are all first-order and very close to the actual proc
ess whether compared on the basis of step-response coefficients, model
parameters or frequency domain plots. The control problem is so simpl
e that two standard PID feedback loops with one-way (lead/lag) interac
tion compensation produce results that are essentially identical to a
2X2 multivariable, model-based (GPC) controller.