LINEAR ALGEBRA AND OPTIMIZATION BASED CONTROLLER DESIGN FOR TRAJECTORY TRACKING OF TYPICAL CHEMICAL PROCESS

Authors

  • M. E. SERRANO
  • G. J. E. SCAGLIA
  • P. ABALLAY
  • O. A. ORTIZ
  • V. MUT

DOI:

https://doi.org/10.52292/j.laar.2014.468

Keywords:

Control System Design, Nonlinear Model, Tracking Trajectory Control, Numerical Methods, Typical Chemical Process

Abstract

This paper presents a new controller design to tracking trajectory of a typical chemical process. The plant model is represented by numerical methods and, from this approach; the control actions for an optimal operation of the system are obtained. Its main advantage is that the condition for the tracking error tends to zero and the calculation of control actions, are obtained solving a system of linear equations. The proofs of convergence to zero of the tracking error are presented. Simulation results show the good performance of the proposed control system.

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Published

2014-10-31

Issue

Vol. 44 No. 4 (2014): Latin American Applied Research

Section

Control and Information Processing

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