Model predictive supervisory control for multi-stack electrolyzers using multilinear modeling

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Autorschaft

Externe Organisationen

  • Fraunhofer-Institut für Windenergiesysteme (IWES)
  • Hochschule für Angewandte Wissenschaften Hamburg
Forschungs-netzwerk anzeigen

Details

OriginalspracheEnglisch
Aufsatznummer151847
FachzeitschriftInternational Journal of Hydrogen Energy
Jahrgang185
Frühes Online-Datum15 Okt. 2025
PublikationsstatusVeröffentlicht - 5 Nov. 2025

Abstract

Offshore green hydrogen production lacks of flexible and scalable supervisory control approaches for multi-stack electrolyzers, raising the need for extendable and high-performance solutions. This work presents a two-stage nonlinear model predictive control (MPC) method. First, an MPC stage generates a discrete on-off electrolyzer switching decision through algebraic relaxation of a Boolean signal. The second MPC stage receives the stack's on-off operation decision and optimizes hydrogen production. This is a novel approach for solving a mixed-integer nonlinear program (MINP) in multi-stack electrolyzer control applications. In order to realize the MPC, the advantages of the implicit multilinear time-invariant (iMTI) model class are exploited for the first time for proton exchange membrane (PEM) electrolyzer models. A modular, flexible, and scalable framework in MATLAB is built. The tensor based iMTI model, in canonical polyadic (CP) decomposed form, breaks the curse of dimensionality and enables effective model composition for electrolyzers. Simulation results show an appropriate multilinear model representation of the nonlinear system dynamics in the operation region. A sensitivity analysis identified three numeric factors as decisive for the effectiveness of the MPC approach. The classic rule-based control methods Daisy Chain and Equal serve as reference. Over two weeks and under a wind power input profile, the MPC strategy performs better regarding the objective of hydrogen production compared to the Daisy Chain (4.60 %) and Equal (0.43 %) power distribution controllers. As a side effect of the optimization, a convergence of the degradation states is observed.

ASJC Scopus Sachgebiete

Ziele für nachhaltige Entwicklung

Zitieren

Model predictive supervisory control for multi-stack electrolyzers using multilinear modeling. / Luxa, Aline; Hanke-Rauschenbach, Richard; Lichtenberg, Gerwald.
in: International Journal of Hydrogen Energy, Jahrgang 185, 151847, 05.11.2025.

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Download
@article{696c8e4c0eaf447e97f8656b0f3e651d,
title = "Model predictive supervisory control for multi-stack electrolyzers using multilinear modeling",
abstract = "Offshore green hydrogen production lacks of flexible and scalable supervisory control approaches for multi-stack electrolyzers, raising the need for extendable and high-performance solutions. This work presents a two-stage nonlinear model predictive control (MPC) method. First, an MPC stage generates a discrete on-off electrolyzer switching decision through algebraic relaxation of a Boolean signal. The second MPC stage receives the stack's on-off operation decision and optimizes hydrogen production. This is a novel approach for solving a mixed-integer nonlinear program (MINP) in multi-stack electrolyzer control applications. In order to realize the MPC, the advantages of the implicit multilinear time-invariant (iMTI) model class are exploited for the first time for proton exchange membrane (PEM) electrolyzer models. A modular, flexible, and scalable framework in MATLAB is built. The tensor based iMTI model, in canonical polyadic (CP) decomposed form, breaks the curse of dimensionality and enables effective model composition for electrolyzers. Simulation results show an appropriate multilinear model representation of the nonlinear system dynamics in the operation region. A sensitivity analysis identified three numeric factors as decisive for the effectiveness of the MPC approach. The classic rule-based control methods Daisy Chain and Equal serve as reference. Over two weeks and under a wind power input profile, the MPC strategy performs better regarding the objective of hydrogen production compared to the Daisy Chain (4.60 %) and Equal (0.43 %) power distribution controllers. As a side effect of the optimization, a convergence of the degradation states is observed.",
keywords = "Implicit modeling, Model predictive control, Multi-stack, Multilinear, Off-grid operation, PEM electrolyzer, Supervisory control, Wind energy",
author = "Aline Luxa and Richard Hanke-Rauschenbach and Gerwald Lichtenberg",
note = "Publisher Copyright: {\textcopyright} 2025 The Author(s)",
year = "2025",
month = nov,
day = "5",
doi = "10.1016/j.ijhydene.2025.151847",
language = "English",
volume = "185",
journal = "International Journal of Hydrogen Energy",
issn = "0360-3199",
publisher = "Elsevier Ltd.",

}

Download

TY - JOUR

T1 - Model predictive supervisory control for multi-stack electrolyzers using multilinear modeling

AU - Luxa, Aline

AU - Hanke-Rauschenbach, Richard

AU - Lichtenberg, Gerwald

N1 - Publisher Copyright: © 2025 The Author(s)

PY - 2025/11/5

Y1 - 2025/11/5

N2 - Offshore green hydrogen production lacks of flexible and scalable supervisory control approaches for multi-stack electrolyzers, raising the need for extendable and high-performance solutions. This work presents a two-stage nonlinear model predictive control (MPC) method. First, an MPC stage generates a discrete on-off electrolyzer switching decision through algebraic relaxation of a Boolean signal. The second MPC stage receives the stack's on-off operation decision and optimizes hydrogen production. This is a novel approach for solving a mixed-integer nonlinear program (MINP) in multi-stack electrolyzer control applications. In order to realize the MPC, the advantages of the implicit multilinear time-invariant (iMTI) model class are exploited for the first time for proton exchange membrane (PEM) electrolyzer models. A modular, flexible, and scalable framework in MATLAB is built. The tensor based iMTI model, in canonical polyadic (CP) decomposed form, breaks the curse of dimensionality and enables effective model composition for electrolyzers. Simulation results show an appropriate multilinear model representation of the nonlinear system dynamics in the operation region. A sensitivity analysis identified three numeric factors as decisive for the effectiveness of the MPC approach. The classic rule-based control methods Daisy Chain and Equal serve as reference. Over two weeks and under a wind power input profile, the MPC strategy performs better regarding the objective of hydrogen production compared to the Daisy Chain (4.60 %) and Equal (0.43 %) power distribution controllers. As a side effect of the optimization, a convergence of the degradation states is observed.

AB - Offshore green hydrogen production lacks of flexible and scalable supervisory control approaches for multi-stack electrolyzers, raising the need for extendable and high-performance solutions. This work presents a two-stage nonlinear model predictive control (MPC) method. First, an MPC stage generates a discrete on-off electrolyzer switching decision through algebraic relaxation of a Boolean signal. The second MPC stage receives the stack's on-off operation decision and optimizes hydrogen production. This is a novel approach for solving a mixed-integer nonlinear program (MINP) in multi-stack electrolyzer control applications. In order to realize the MPC, the advantages of the implicit multilinear time-invariant (iMTI) model class are exploited for the first time for proton exchange membrane (PEM) electrolyzer models. A modular, flexible, and scalable framework in MATLAB is built. The tensor based iMTI model, in canonical polyadic (CP) decomposed form, breaks the curse of dimensionality and enables effective model composition for electrolyzers. Simulation results show an appropriate multilinear model representation of the nonlinear system dynamics in the operation region. A sensitivity analysis identified three numeric factors as decisive for the effectiveness of the MPC approach. The classic rule-based control methods Daisy Chain and Equal serve as reference. Over two weeks and under a wind power input profile, the MPC strategy performs better regarding the objective of hydrogen production compared to the Daisy Chain (4.60 %) and Equal (0.43 %) power distribution controllers. As a side effect of the optimization, a convergence of the degradation states is observed.

KW - Implicit modeling

KW - Model predictive control

KW - Multi-stack

KW - Multilinear

KW - Off-grid operation

KW - PEM electrolyzer

KW - Supervisory control

KW - Wind energy

UR - http://www.scopus.com/inward/record.url?scp=105018667373&partnerID=8YFLogxK

U2 - 10.1016/j.ijhydene.2025.151847

DO - 10.1016/j.ijhydene.2025.151847

M3 - Article

AN - SCOPUS:105018667373

VL - 185

JO - International Journal of Hydrogen Energy

JF - International Journal of Hydrogen Energy

SN - 0360-3199

M1 - 151847

ER -

Von denselben Autoren