Abstract
This work presents a comparison among three different control strategies for multivariable processes. The techniques were implemented in a pilot plant with coupled control loops, where all steps used to design the controllers were described allowing to establish a trade-off between algorithm complexity, information needed from the process and achieved performance. Two data-driven control techniques are used: multivariable ultimate point method to design a decentralized PID controller and virtual reference feedback tuning to design a centralized PID controller. A mathematical model of the process is obtained and used to design a model-based generalized predictive controller. Experimental results allow us to evaluate the performance achieved for each method, as well as to infer on their advantages and disadvantages.
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Notes
For PID controller parameters see Campestrini et al. (2009).
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E. Boeira, V. Bordignon, D. Eckhard and L. Campestrini are supported by CNPq.
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Boeira, E., Bordignon, V., Eckhard, D. et al. Comparing MIMO Process Control Methods on a Pilot Plant. J Control Autom Electr Syst 29, 411–425 (2018). https://doi.org/10.1007/s40313-018-0387-6
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DOI: https://doi.org/10.1007/s40313-018-0387-6