Comparison PID and MPC Control, Applied to a Binary Distillation Column
Anderson Rigoberto Cuenca S1, Jose Leonardo Benavides M2, Manuel Augusto Pesantez G.3

1Anderson Cuenca S, Electromechanics, University National of Loja, Loja, Ecuador.
2Leonardo Benavides M., Electromechanics, University National of Loja, Loja, Ecuador.
3Manuel Pesantez G., Electromechanics, University National of Loja, Loja, Ecuador.

Manuscript received on 13 August 2016 | Revised Manuscript received on 20 August 2016 | Manuscript Published on 30 August 2016 | PP: 99-103 | Volume-5 Issue-6, August 2016 | Retrieval Number: F4665085616/16©BEIESP
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Abstract: Using binary distillation column in the industry is currently imperative, the reason why the control parameters that are highly nonlinear necessary to apply classic strategies as advanced control and raised here. These techniques are the PID controller and the MPC; the data that are to perform the calculations are of IFAC event whose mixture is alcohol with water. Finally with the help of software MATLAB® / Simulink simulations for comparing which of the two drivers is the best delivery results when controlling the composition on the bottom, top and pressure in binary distillation column performed.
Keywords: Chemical Industry, Distillation Columns, MPC (Predictive Control Method), PID Control.

Scope of the Article: Bio-Science and Bio-Technology