Details
| Originalsprache | Englisch |
|---|---|
| Aufsatznummer | 151847 |
| Fachzeitschrift | International Journal of Hydrogen Energy |
| Jahrgang | 185 |
| Frühes Online-Datum | 15 Okt. 2025 |
| Publikationsstatus | Veröffentlicht - 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
- Energie (insg.)
- Erneuerbare Energien, Nachhaltigkeit und Umwelt
- Energie (insg.)
- Feuerungstechnik
- Physik und Astronomie (insg.)
- Physik der kondensierten Materie
- Energie (insg.)
- Energieanlagenbau und Kraftwerkstechnik
Ziele für nachhaltige Entwicklung
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in: International Journal of Hydrogen Energy, Jahrgang 185, 151847, 05.11.2025.
Publikation: Beitrag in Fachzeitschrift › Artikel › Forschung › Peer-Review
}
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 -