2017
DOI: 10.1002/asjc.1603
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Robust Constrained Model Predictive Control for Discrete‐Time Uncertain System in Takagi‐Sugeno's Form

Abstract: In this paper, we investigate a robust constrained model predictive control synthesis approach for discrete-time Takagi-Sugeno's (T-S) fuzzy system with structured uncertainty. The key idea is to determine, at each sampling time, a state feedback fuzzy predictive controller that minimizes the performance objective function in the infinite time horizon by solving a class of linear matrix inequalities (LMIs) optimization problem. To do this, the fuzzy predictive controller is designed on the basis of non-paralle… Show more

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Cited by 16 publications
(21 citation statements)
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“…where u (k) is the control input,ū ∈ ℜ m denotes the saturation level function. In the saturation function (5), each component of the vector (k) can be represented as:…”
Section: Control Design With Actuator Saturationmentioning
confidence: 99%
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“…where u (k) is the control input,ū ∈ ℜ m denotes the saturation level function. In the saturation function (5), each component of the vector (k) can be represented as:…”
Section: Control Design With Actuator Saturationmentioning
confidence: 99%
“…To avoid this drawback and enlarge the feasibility set of solutions, extended Lyapunov functions have been investigated such as: piecewise Lyapunov functions (PLF) [8] and fuzzy weighting-dependent Lyapunov functions (FWDLF) [9][10][11][12][13][14][15]. Moreover, for nonlinear systems subjected to model uncertainties, robust stability analysis methods for T-S fuzzy systems with uncertainties have been developed in recent years [5,8,[15][16][17][18][19][20][21]. The control of T-S models generally uses the so-called state feedback parallel distributed compensation (PDC) scheme.…”
Section: Introductionmentioning
confidence: 99%
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“…In this example, a CSTR for an exothermic, irreversible reaction A → B with constant liquid volume is considered to highlight the quality of the control that can be achieved by ItMPC when both the set point and the optimal trajectory of the states to the set point are within the tighter state constraints obtained by the procedure of tightening the state constraints. The continuous time model is derived from the mass and energy balances and it is given by . dCAdt=qV()CAfCAk0eE/italicRTCAdTdt=qV()TfT+normalΔHρCpk0eE/italicRTCA+UAitalicVρCp()TcT where C A is the concentration of A in the reactor, T is the reactor temperature, and T C is the temperature of the coolant stream.…”
Section: Illustrative Examplesmentioning
confidence: 99%
“…In this example, a CSTR for an exothermic, irreversible reaction A → B with constant liquid volume is considered to highlight the quality of the control that can be achieved by ItMPC when both the set point and the optimal trajectory of the states to the set point are within the tighter state constraints obtained by the procedure of tightening the state constraints. The continuous time model is derived from the mass and energy balances and it is given by [20,25].…”
Section: Cstr Modelmentioning
confidence: 99%