Profile control in distributed parameter systems using lexicographic optimization based MPC

Abstract Process equipment that exhibits significant spatial variation of system properties, such as temperature or concentration in a fixed bed reactor, are typically modeled as distributed parameter systems. While some properties of the final product exiting the equipment may depend on the states concerning the endpoint, others may be a function of the history of processing within the equipment. In such instances, control of the spatial property profile may be beneficial. In this work, we explore the idea of profile control using extended MPC and outline the additional challenges that must be addressed in this context. In case that the target profile is unachievable, we present an MPC formulation that uses lexicographic optimization to prioritize the different sections of the profile. Simulation of a simple representative system namely a hypothetical plug flow reactor is used to demonstrate that the lexicographic optimization based MPC provides a systematic approach to profile control and spans between the endpoint control strategy and the whole profile control strategy. The benefits of lexicographic optimization based MPC were also demonstrated on a large-scale distributed parameter system of industrial size, namely the continuous pulp digester.

[1]  Veikko Jääskeläinen Linear Programming and Budgeting , 1981 .

[2]  Panagiotis D. Christofides,et al.  Model-Based Control of Particulate Processes , 2002 .

[3]  Hanif D. Sherali,et al.  Equivalent weights for lexicographic multi-objective programs: Characterizations and computations , 1982 .

[4]  Y. Hwang,et al.  Nonlinear wave theory for dynamics of binary distillation columns , 1991 .

[5]  Yng-Long Hwang,et al.  Dynamics of continuous countercurrent mass-transfer processes—II. Single-component systems with nonlinear equilibria , 1988 .

[6]  Achim Kienle,et al.  Nonlinear control of a reactive distillation column , 2003 .

[7]  Roger M. Y. Ho,et al.  Goal programming and extensions , 1976 .

[8]  Sunwon Park,et al.  Control of high‐purity distillation column using a nonlinear wave theory , 1992 .

[9]  Francis J. Doyle,et al.  Hierarchical multiobjective strategy for particle‐size distribution control , 2003 .

[10]  Saibal Ganguly,et al.  Observer-based control algorithms for a distillation column , 2006 .

[11]  Jay H. Lee,et al.  Subspace identification based inferential control applied to a continuous pulp digester , 1999 .

[12]  Francis J. Doyle,et al.  Control structure selection and model predictive control of the Weyerhaeuser digester problem , 1998 .

[13]  Wolfgang Marquardt NONLINEAR MODEL REDUCTION FOR BINARY DISTILLATION , 1986 .

[14]  Francis J. Doyle,et al.  Reaction profile control of the continuous pulp digester , 1999 .

[15]  W. Harmon Ray,et al.  A control scheme for packed bed reactors having a changing catalyst activity profile. I: On-line parameter estimation and feedback control , 1992 .

[16]  R. Curtain Finite-dimensional compensator design for parabolic distributed systems with point sensors and boundary input , 1982 .

[17]  John F. MacGregor,et al.  Application of LQ and IMC controllers to a packed‐bed reactor , 1987 .

[18]  Francis J. Doyle,et al.  Nonlinear inferential multi-rate control of Kappa number at multiple locations in a continuous pulp digester , 2006 .

[19]  Coleman B. Brosilow,et al.  The modular multivariable controller: I: Steady‐state properties , 1992 .

[20]  R. Temam Infinite Dimensional Dynamical Systems in Mechanics and Physics Springer Verlag , 1993 .

[21]  A. Soyster,et al.  Preemptive and nonpreemptive multi-objective programming: Relationship and counterexamples , 1983 .

[22]  William L. Luyben Profile position control of distillation columns with sharp temperature profiles , 1972 .

[23]  Francis J. Doyle,et al.  Model-based predictive control studies for a continuous pulp digester , 2001, IEEE Trans. Control. Syst. Technol..

[24]  Evanghelos Zafiriou,et al.  Model based process control : proceedings of the IFAC Workshop, Atlanta, Georgia, USA, 13-14 June 1988 , 1989 .

[25]  R. Braatz,et al.  Particle Size and Shape Control in Crystallization Processes , 2002 .

[26]  Tor Arne Johansen,et al.  Linear MPC with optimal prioritized infeasibility handling: application, computational issues and stability , 2001, Autom..

[27]  Francis J. Doyle,et al.  Mathematical Model Predictions of a Plugging Phenomenon in an Industrial Single-Vessel Pulp Digester , 2004 .

[28]  Mark J. Balas,et al.  Finite-dimensional control of distributed parameter systems by Galerkin approximation of infinite dimensional controllers☆ , 1986 .

[29]  W. Ray,et al.  Identification and control of distributed parameter systems by means of the singular value decomposition , 1995 .

[30]  Jiongmin Yong,et al.  Optimal control for a class of distributed parameter systems , 1990, 29th IEEE Conference on Decision and Control.

[31]  Masatoshi Yoshida,et al.  Control of Axial Temperature Distribution in a Packed-Bed Reactor , 1998 .

[32]  Pascal Dufour,et al.  On nonlinear distributed parameter model predictive control strategy: on-line calculation time reduction and application to an experimental drying process , 2003, Comput. Chem. Eng..

[33]  Costas J. Spanos,et al.  Advanced process control , 1989 .

[34]  James P. Ignizio,et al.  Linear Programming in Single- and Multiple-Objective Systems , 1984 .

[35]  J. Rawlings,et al.  Model identification and control of solution crystallization processes: a review , 1993 .

[36]  Francis J. Doyle,et al.  Fundamental continuous-pulp-digester model for simulation and control , 1997 .

[37]  Manfred Morari,et al.  Linearizing controller design for a packed-bed reactor using a low-order wave propagation model , 1996 .