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4.3 Integrator + Dead Time

An integrator + dead-time process has the input-output transfer function relationship

Equation 4.3

graphics/04equ03.gif


and the output response to a step input

Equation 4.4

graphics/04equ04.gif


with the response shown in Figure 4-5. The gain, k, can be found from the slope by solving

graphics/04equ04a.gif


Figure 4-5. Estimating parameters for an integrator + time-delay model from a step input test.

graphics/04fig05.gif

and the time delay is clearly identified by the time required for a change in output.

Integrator + dead-time models are good for describing the behavior of "integrating processes," such as vessel liquid levels or gas drum pressures. They can provide a good short-term approximation to the step response behavior of a first-order + dead-time process. Consider the step response of a distillation column, which has a fairly long time constant. We see from Figure 4-6 that it takes roughly 5–6 hours to obtain good estimates for a FODT model.

Figure 4-6. Distillation column overhead composition response to a step change of 0.01 kmol/min in reflux rate at t = 10 minutes.

graphics/04fig06.gif

The reader should be able to show that the transfer function is approximately

graphics/04equ04b.gif


where the gain has units of mol%/(kmol/min) and the time unit is minutes.

The initial response of Figure 4-6 is "blown-up" in Figure 4-7. Notice that fewer than 20 minutes (the step change is made at t = 10 minutes) is required to obtain a satisfactory integrator + time-delay model. Clearly, plant operators (and managers) will be much more willing to tolerate a 20-minute test than a 4- to 5-hour test.

Figure 4-7. Distillation column overhead composition response to a step change of 0.01 kmol/min in reflux rate at t = 10 minutes. Focus is on the short-term response.

graphics/04fig07.gif

The reader should be able to show that the estimated transfer function is approximately

graphics/04equ04c.gif


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