International audienceIn this paper, a new constrained nonlinear predictive control scheme is proposed for maximizing the production in polymerization processes. The key features of the proposed feedback strategy are its ability to rigorously handle the process constraints (input saturation, maximum allowed heat production, maximal temperature values and rate of change) as well as its real time implementability due to the low dimensional control parametrization being used. Simulations are proposed to show the efficiency of the proposed feedback as well as its robustness to model uncertainties.The controller performance is also validated experimentally on a laboratory scale reactor to control the emulsion polymerization of styrene
Abstract: A large-scale set of differential and algebraic equations (DAEs) is used to model and cont...
The control of a gas phase propylene polymerization model in a fluidized bed reactor was studied, wh...
This paper addresses the optimization of batch polymerization systems, using a feasible path approac...
International audienceIn this paper, a new constrained nonlinear predictive control scheme is propos...
The aim of this thesis was to develop an advanced two-layer control structure for the semi-batch pol...
A general method for the synthesis of continuous- and discrete-time feedback control systems for sin...
A nonlinear control system integrating an off-line optimizer and a nonlinear model-based controller ...
This work studies the experimental application of the globally linearizing control (GLC) method to a...
The objective of this work is to develop a strategy of nonlinear model predictive control for indust...
International audienceA multivariable control strategy is developed to control the polymer molecular...
The main focus of this thesis is the development of continuous and discrete-time nonlinear model bas...
A nonlinear model predictive control scheme based on the second-order Volterra model is presented. F...
A nonlinear model predictive control (NMPC) is applied to a slurry polymerization stirred tank react...
The performance of two advanced model based non-linear controllers is analyzed for the optimal setpo...
Nonlinear model predictive control (NMPC) is one of the few methods that can handle multivariate non...
Abstract: A large-scale set of differential and algebraic equations (DAEs) is used to model and cont...
The control of a gas phase propylene polymerization model in a fluidized bed reactor was studied, wh...
This paper addresses the optimization of batch polymerization systems, using a feasible path approac...
International audienceIn this paper, a new constrained nonlinear predictive control scheme is propos...
The aim of this thesis was to develop an advanced two-layer control structure for the semi-batch pol...
A general method for the synthesis of continuous- and discrete-time feedback control systems for sin...
A nonlinear control system integrating an off-line optimizer and a nonlinear model-based controller ...
This work studies the experimental application of the globally linearizing control (GLC) method to a...
The objective of this work is to develop a strategy of nonlinear model predictive control for indust...
International audienceA multivariable control strategy is developed to control the polymer molecular...
The main focus of this thesis is the development of continuous and discrete-time nonlinear model bas...
A nonlinear model predictive control scheme based on the second-order Volterra model is presented. F...
A nonlinear model predictive control (NMPC) is applied to a slurry polymerization stirred tank react...
The performance of two advanced model based non-linear controllers is analyzed for the optimal setpo...
Nonlinear model predictive control (NMPC) is one of the few methods that can handle multivariate non...
Abstract: A large-scale set of differential and algebraic equations (DAEs) is used to model and cont...
The control of a gas phase propylene polymerization model in a fluidized bed reactor was studied, wh...
This paper addresses the optimization of batch polymerization systems, using a feasible path approac...