[ Team LiB ] Previous Section Next Section

M10.4 Numerical Example

Consider a surge vessel that has a diameter of 1 m, and a maximum height of 2 m, with low- and high-level alarms set at 20% and 80%. Also, assume that the height setpoint is 1 meter, and the steady-state flow rate is 0.5 m3/min. The constant cross-sectional area is then 0.785 m2. Since the steady-state flow rate is 0.5 m3/min, assume that the inlet flow rate can vary between 0 and 1 m3/min.

You should show that the process and load disturbance transfer functions are

graphics/m10equ07a.gif


Since the physical variable minimum and maximum alarm heights are 0.4 and 1.6 m, respectively, in terms of deviation variables, the minimum and maximum heights are

graphics/m10equ07b.gif


So, DH = 0.6 m. The minimum and maximum manipulated variable values are

graphics/m10equ07c.gif


So, DL = 0.5 m3/min. From Equations (M10.5) and (M10.7), we find kc = -0.833 m2/min and kc0 = -1.389 m/min.

Step Disturbances

Compare the step responses of the linear and nonlinear controllers to a small step disturbance of 0.05 m3/min and a large step disturbance of 0.5 m3/min. For a small step change in the load disturbance (inlet flow rate), the linear and nonlinear controllers are shown in Figure M10-2. Notice that the manipulated input changes more slowly for the nonlinear controller. The minor disadvantage is that the offset is larger for the nonlinear controller, as designed. This is not a real problem, as the offset is small compared with the capacity of the vessel.

Figure M10-2. Response to a small step in inlet flow rate (0.05 m3/min).

graphics/m10fig02.gif

Responses to a large step in the inlet flow rate are compared in Figure M10-3. For this case, these responses are similar and there is not much incentive to use the nonlinear strategy.

Figure M10-3. Response to a large step in inlet flow rate (0.5 m3/min).

graphics/m10fig03.gif

Sinusoidal Disturbances

Consider a sinusoidal disturbance with an amplitude of 0.05 m3/min and a frequency of 1/min. The linear and nonlinear strategies are compared in Figure M10-4. Clearly, there is an incentive for nonlinear control, since the manipulated variable does not change nearly as much for the nonlinear case as for the linear case.

Figure M10-4. Response to a small amplitude (0.05 m3/min) sinusoidal inlet flow rate disturbance.

graphics/m10fig04.gif

The responses to large-magnitude sinusoidal disturbance with an amplitude of 0.5 m3/min and a frequency of 1/min is shown in Figure M10-5. In this case, there is not much incentive for the nonlinear control strategy.

Figure M10-5. Response to a large-amplitude (0.5 m3/min) sinusoidal inlet flow rate disturbance.

graphics/m10fig05.gif

You should show that a high-frequency disturbance is rejected very well by the nonlinear strategy.

Additional Simulations

Consider the large-magnitude sinusoidal disturbance shown in Figure M10-5. Show that doubling the amplitude of the disturbance leads to saturation of the manipulated variable, and to violation of the high- and low-level alarms.

    [ Team LiB ] Previous Section Next Section