Exploring Tradeoffs in Syngas Production With Solid‐Oxide Electrolysis via Multi‐Objective Optimization

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Autori principali: Gbenga Jerome, Victor Selmert, An Phuc Dam, Nicolas Kruse, Leandros Paschalidis, Remzi Can Samsun, Rüdiger‐A. Eichel
Natura: Artículo Open Access
Pubblicazione: Wiley 2026
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author Gbenga Jerome
Victor Selmert
An Phuc Dam
Nicolas Kruse
Leandros Paschalidis
Remzi Can Samsun
Rüdiger‐A. Eichel
author_facet Gbenga Jerome
Victor Selmert
An Phuc Dam
Nicolas Kruse
Leandros Paschalidis
Remzi Can Samsun
Rüdiger‐A. Eichel
Gbenga Jerome
Victor Selmert
An Phuc Dam
Nicolas Kruse
Leandros Paschalidis
Remzi Can Samsun
Rüdiger‐A. Eichel
collection Wiley Open Access
contents Exploring Tradeoffs in Syngas Production With Solid‐Oxide Electrolysis via Multi‐Objective Optimization Gbenga Jerome Victor Selmert An Phuc Dam Nicolas Kruse Leandros Paschalidis Remzi Can Samsun Rüdiger‐A. Eichel Chemie Ingenieur Technik ABSTRACT Syngas is an important intermediate with a wide range of applications. Recent efforts at Forschungszentrum Jülich focus on the electrolytic production of syngas from water and carbon dioxide through high‐temperature solid‐oxide cell electrolysis cells (SOECs) for use in methanol synthesis in the context of the DryHy project. In this work, an ASPEN Plus model is developed and used to explore the trade‐offs between different objectives in syngas production using solid‐oxide electrolysis cells. Two different system designs are investigated: a low‐ and a high‐utilization design. Four key objectives related to syngas composition and SOEC system performance are considered: energy efficiency, stoichiometric number, carbon oxide ratio, and the inlet water‐to‐carbon dioxide ratio. The trade‐offs between these objectives are analyzed to gain insights into the operation of SOEC systems in co‐electrolysis mode. A comparison of the two designs reveals that the high‐utilization design consistently outperforms the low‐utilization design for the considered objectives. In addition, it is observed that a significant difference in the inlet water‐to‐carbon dioxide ratio required to achieve the stoichiometric number needed for methanol synthesis exists. 10.1002/cite.70113 http://creativecommons.org/licenses/by/4.0/
doi_str_mv 10.1002/cite.70113
format Artículo Open Access
id wiley_oa_10_1002_cite_70113
institution Wiley Open Access
license_str_mv http://creativecommons.org/licenses/by/4.0/
publishDate 2026
publisher Wiley
record_format wiley_oa
spellingShingle Exploring Tradeoffs in Syngas Production With Solid‐Oxide Electrolysis via Multi‐Objective Optimization
Gbenga Jerome
Victor Selmert
An Phuc Dam
Nicolas Kruse
Leandros Paschalidis
Remzi Can Samsun
Rüdiger‐A. Eichel
Chemie Ingenieur Technik
Exploring Tradeoffs in Syngas Production With Solid‐Oxide Electrolysis via Multi‐Objective Optimization Gbenga Jerome Victor Selmert An Phuc Dam Nicolas Kruse Leandros Paschalidis Remzi Can Samsun Rüdiger‐A. Eichel Chemie Ingenieur Technik ABSTRACT Syngas is an important intermediate with a wide range of applications. Recent efforts at Forschungszentrum Jülich focus on the electrolytic production of syngas from water and carbon dioxide through high‐temperature solid‐oxide cell electrolysis cells (SOECs) for use in methanol synthesis in the context of the DryHy project. In this work, an ASPEN Plus model is developed and used to explore the trade‐offs between different objectives in syngas production using solid‐oxide electrolysis cells. Two different system designs are investigated: a low‐ and a high‐utilization design. Four key objectives related to syngas composition and SOEC system performance are considered: energy efficiency, stoichiometric number, carbon oxide ratio, and the inlet water‐to‐carbon dioxide ratio. The trade‐offs between these objectives are analyzed to gain insights into the operation of SOEC systems in co‐electrolysis mode. A comparison of the two designs reveals that the high‐utilization design consistently outperforms the low‐utilization design for the considered objectives. In addition, it is observed that a significant difference in the inlet water‐to‐carbon dioxide ratio required to achieve the stoichiometric number needed for methanol synthesis exists. 10.1002/cite.70113 http://creativecommons.org/licenses/by/4.0/
title Exploring Tradeoffs in Syngas Production With Solid‐Oxide Electrolysis via Multi‐Objective Optimization
topic Chemie Ingenieur Technik
url https://onlinelibrary.wiley.com/doi/10.1002/cite.70113