Publication

Nonlinear model predictive control for hydrogen production in an ethanol steam reformer with membrane separation

Conference Article

Conference

IEEE Multi-Conference on Systems and Control (MSC)

Edition

2016

Pages

1155-1160

Doc link

http://dx.doi.org/10.1109/CCA.2016.7587962

File

Download the digital copy of the doc pdf document

Abstract

This paper presents a new Nonlinear Model Predictive Control (NMPC) design for an Ethanol Steam Reformer with Pd-Ag membrane separation stage. The reformer is used to produce pure hydrogen able to feed a Proton Exchange Membrane Fuel Cell. Mass and energy balances are used to obtain the nonlinear dynamic model of both the reforming and the separation stages. Constraints, system nonlinearities and flexible cost function are the main reasons to select an NMPC controller, which is tested against the ordinary differential equations as simulation model, and has an internal model based on the sample data technique.

Categories

automation, control theory, optimisation.

Author keywords

Ethanol reformers, model predictive control, nonlinear systems, hydrogen-based technologies

Scientific reference

E. Pérez, M. Serra, C. Ocampo-Martínez and J. Llorca. Nonlinear model predictive control for hydrogen production in an ethanol steam reformer with membrane separation, 2016 IEEE Multi-Conference on Systems and Control, 2016, Buenos Aires, Argentina, pp. 1155-1160.