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8.7 The IMC Structure

The IMC structure is shown in Figure 8-12. The distinguishing characteristic of this structure is the process model, which is in parallel with the actual process (plant). Note that (~) is generally used to represent signals associated with the model. Other literature sources may use a subscript (such as m) to represent the model. Figure 8-13 illustrates that both the controller and model exist as computer computations; it is convenient to treat them separately for design and analysis.

Figure 8-12. The internal model control structure.

graphics/08fig12.gif

Figure 8-13. The IMC strategy. The dotted line indicates the calculations performed by the model-based controller.

graphics/08fig13.gif

A list of transfer function variables shown in the IMC block diagram are given below.

d(s)=

disturbance

graphics/dtildes.gif=

estimated disturbance

gp(s)=

process

graphics/gtildes.gif=

process model

q(s)=

internal model controller

r(s)=

setpoint

graphics/rtildes.gif=

modified setpoint (corrects for model error and disturbances)

u(s)=

manipulated input (controller output)

y(s)=

measured process output

graphics/ytildes1.gif=

model output

Notice that the feedback signal is

Equation 8.36

graphics/08equ36.gif


The signal to the controller is

Equation 8.37

graphics/08equ37.gif


Consider now some limiting cases.

Perfect Model, No Disturbances

If the model is perfect graphics/08inequ07.gif and there are no disturbances (d(s) = 0), then the feedback signal is zero. The relationship between r(s) and y(s) is then

Equation 8.38

graphics/08equ38.gif


Notice that this is the same relationship that we get for an open-loop control system design.

Why is this nice? If the controller, q(s), is stable and the process, gp(s), is stable, then the closed-loop system is stable. We developed a design procedure that yields a stable, physically realizable controller in Section 8.3.

Recall that a standard feedback controller could actually destabilize a process if we did not correctly choose the tuning parameters. An analysis of the poles of the closed-loop transfer function must be performed to determine the stability of standard feedback controllers.

Perfect Model, Disturbance Effect

If the model is perfect graphics/08inequ07.gif and there is a disturbance, then the feedback signal is

graphics/08equ38a.gif


This illustrates that feedback is needed because of unmeasured disturbances entering a process.

Model Uncertainty, No Disturbances

If there are no disturbances [d(s) = 0] but there is model uncertainty graphics/08inequ17.gif, which is always the case in the real world, then the feedback signal is

graphics/08equ38b.gif


This illustrates that feedback is needed because of model uncertainty.

The closed-loop relationship is

graphics/08equ38c.gif


Recapitulating, the reasons for feedback control include the following:

  • Unmeasured disturbances

  • Model uncertainty

  • Faster response than the open-loop system (with a static controller)

  • Closed-loop stability of open-loop unstable system

The primary disadvantage of IMC is that it does not guarantee stability of open-loop unstable systems. The procedure detailed in Chapter 9 handles these systems.

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