Parametric uncertainty and disturbance attenuation in the suboptimal control of a non‐linear electrochemical process

The optimal control of the hydrogen evolution reactions is attempted for the regulation and change of set-point problems, taking into account that model parameters are uncertain and I/O signals are corrupted by noise. Bilinear approximations are constructed, and their dimension eventually increased to meet accuracy requirements with respect to the trajectories of the original plant. The current approximate model is used to evaluate the optimal feedback through integration of the Hamiltonian equations. The initial value for the costate is found by solving a state-dependent algebraic Riccati equation, and the resulting control is then suboptimal for the electrochemical process. The bilinear model allows for an optimal Kalman–Bucy filter application to reduce external noise. The filtered output is reprocessed through a non-linear observer in order to obtain a state-estimation as independent as possible from the bilinear model. Uncertainties on parameters are attenuated through an adaptive control strategy that exploits sensitivity functions in a novel fashion. The whole approach to this control problem can be applied to a fairly general class of non-linear continuous systems subject to analogous stochastic perturbations. All calculations can be handled on-line by standard ordinary differential equations integration software. Copyright © 2007 John Wiley & Sons, Ltd.

[1]  J. L. Hudson,et al.  Electrochemical Reaction Dynamics - A Review , 1994 .

[2]  H. Sussmann Semigroup Representations, Bilinear Approximation of Input-Output Maps, and Generalized Inputs , 1976 .

[3]  A. C. Chialvo,et al.  Kinetics of hydrogen evolution reaction with Frumkin adsorption : re-examination of the Volmer-Heyrovsky and Volmer-Tafel routes , 1998 .

[4]  C. D'Attellis,et al.  Trajectory tracking in nonlinear systems via nonlinear reduced-order observers , 1995 .

[5]  D. Britz,et al.  Kinetics of the deuterium and hydrogen evolution reactions at palladium in alkaline solution , 1996 .

[6]  S. Pyun,et al.  An investigation of the hydrogen absorption reaction into, and the hydrogen evolution reaction from, , 1996 .

[7]  Arthur J. Krener,et al.  Bilinear and Nonlinear Realizations of Input-Output Maps , 1975 .

[8]  W. Fleming,et al.  Deterministic and Stochastic Optimal Control , 1975 .

[9]  T. Edgar,et al.  Controllability and observability covariance matrices for the analysis and order reduction of stable nonlinear systems , 2003 .

[10]  Mats Ekman,et al.  Suboptimal control for the bilinear quadratic regulator problem: application to the activated sludge process , 2005, IEEE Transactions on Control Systems Technology.

[11]  B. Conway,et al.  Kinetic theory of the open-circuit potential decay method for evaluation of behaviour of adsorbed intermediates. Analysis for the case of the H2 evolution reaction , 1987 .

[12]  Hong Wang,et al.  Suboptimal mean controllers for bounded and dynamic stochastic distributions , 2002 .

[13]  C. Marozzi,et al.  Analysis of the use of voltammetric results as a steady state approximation to evaluate kinetic parameters of the hydrogen evolution reaction , 2005 .

[14]  Daniel R. Lewin,et al.  Model-based Control of Fuel Cells: (1) Regulatory Control , 2004 .

[15]  Ioannis G. Kevrekidis,et al.  The dynamic response of PEM fuel cells to changes in load , 2005 .

[16]  István Z. Kiss,et al.  Controlling Electrochemical Chaos in the Copper-Phosphoric Acid System , 1997 .

[17]  C. Neuman,et al.  Optimal control of non‐linear chemical reactors via an initial‐value Hamiltonian problem , 2006 .

[18]  V. Costanza A variational approach to the control of electrochemical hydrogen reactions , 2005 .

[19]  P. Hartman Ordinary Differential Equations , 1965 .

[20]  C. Neuman,et al.  An adaptive control strategy for nonlinear processes , 1995 .