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Some chemical processes, such as a distillation column, can be modeled as a series of first-order processes with the same time constant. For the process with transfer function

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design a digital proportional controller with a sampling period T = 0.1 by applying the tangent method and the Ziegler-Nichols rules (see Sections 5.5 and 6.3.4). Use the circle criterion to show that the closed-loop system with actuator saturation nonlinearity of slope unity is asymptotically stable. Obtain the step response of the closed-loop system to verify the stability of the closed-loop system with actuator saturation.

Computer Engineering, Engineering

  • Category:- Computer Engineering
  • Reference No.:- M92025984

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