An Approach to linear state Signal Shaping by quadratic Model Predictive Control

Author(s):  
Carlos Cateriano Yanez ◽  
Georg Pangalos ◽  
Gerwald Lichtenberg
2017 ◽  
Vol 62 (6) ◽  
pp. 3068-3075 ◽  
Author(s):  
Ricardo P. Aguilera ◽  
Gabriel Urrutia ◽  
Ramon A. Delgado ◽  
Daniel Dolz ◽  
Juan C. Aguero

2012 ◽  
Vol 2012 ◽  
pp. 1-11 ◽  
Author(s):  
Fabian Jarmolowitz ◽  
Christopher Groß-Weege ◽  
Thomas Lammersen ◽  
Dirk Abel

This work investigates the active control of an unstable Rijke tube using robust output model predictive control (RMPC). As internal model a polytopic linear system with constraints is assumed to account for uncertainties. For guaranteed stability, a linear state feedback controller is designed using linear matrix inequalities and used within a feedback formulation of the model predictive controller. For state estimation a robust gain-scheduled observer is developed. It is shown that the proposed RMPC ensures robust stability under constraints over the considered operating range.


2020 ◽  
Vol 53 (2) ◽  
pp. 6937-6942
Author(s):  
Kathrin Weihe ◽  
Carlos Cateriano Yáñez ◽  
Georg Pangalos ◽  
Gerwald Lichtenberg

2013 ◽  
Vol 846-847 ◽  
pp. 73-76 ◽  
Author(s):  
Shi Li ◽  
Yan Hu ◽  
Xi Ju Zong

This paper is concerns with the study of model predictive control of a circulating fluidized bed coal combustor. A nonlinear mechanical model is proposed based on a pilot plant and representative of the main combustion phenomena. The nonlinear model is linearized at the steady-state point, linear state-space model is obtained. Model predictive control (MPC) strategy is applied using linear model. Simulation results are presented and discussed.


2017 ◽  
Vol 27 (4) ◽  
pp. 595-615 ◽  
Author(s):  
Piotr Tatjewski

AbstractOffset-free model predictive control (MPC) algorithms for nonlinear state-space process models, with modeling errors and under asymptotically constant external disturbances, is the subject of the paper. The main result of the paper is the presentation of a novel technique based on constant state disturbance prediction. It was introduced originally by the author for linear state-space models and is generalized to the nonlinear case in the paper. First the case with measured state is considered, in this case the technique allows to avoid disturbance estimation at all. For the cases with process outputs measured only and thus the necessity of state estimation, the technique allows the process state estimation only - as opposed to conventional approach of extended process-and-disturbance state estimation. This leads to simpler design with state observer/filter of lower order and, moreover, without the need of a decision of disturbance placement in the model (under certain restrictions), as in the conventional approach. A theoretical analysis of the proposed algorithm is provided, under applicability conditions which are weaker than in the conventional approach. The presented theory is illustrated by simulation results of nonlinear processes, showing competitiveness of the proposed algorithms.


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