| Creating and Manipulating Models | ![]() |
Distillation Column Example
This example is adapted from [2] and illustrates the use of I/O delays in process modeling. The process of interest is the distillation column depicted by the figure below. This column is used to separate a mix of methanol and water (the feed) into bottom products (mostly water) and a methanol-saturated distillate.
Figure 1-2: Distillation Column
Schematically, the distillation process functions as follows:
The regulated output variables are:
The goal is to maximize
by adjusting the reflux flow rate
and the steam flow rate
in the reboiler.
To obtain a linearized model around the steady-state operating conditions, the transient responses to pulses in steam and reflux flow are fitted by first-order plus delay models. The resulting transfer function model is
Note the different time delays for each input/output pair.
You can specify this MIMO transfer function by typing
H = tf({12.8 -18.9;6.6 -19.4},... {[16.7 1] [21 1];[10.9 1] [14.4 1]},... 'iodelay',[1 3;7 3],... 'inputname',{'R' , 'S'},... 'outputname',{'Xd' , 'Xb'})
The resulting TF model is displayed as
Transfer function from input "R" to output... 12.8 Xd: exp(-1*s) * ---------- 16.7 s + 1 6.6 Xb: exp(-7*s) * ---------- 10.9 s + 1 Transfer function from input "S" to output... -18.9 Xd: exp(-3*s) * -------- 21 s + 1 -19.4 Xb: exp(-3*s) * ---------- 14.4 s + 1
| Specifying Input/Output Delays | Specifying Delays on the Inputs or Outputs | ![]() |
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