001049774 001__ 1049774
001049774 005__ 20251217202232.0
001049774 037__ $$aFZJ-2025-05558
001049774 041__ $$aEnglish
001049774 1001_ $$0P:(DE-Juel1)198866$$aJerome, Gbenga$$b0$$eCorresponding author$$ufzj
001049774 1112_ $$aSOC Große Runde$$cJülich$$d2025-07-01 - 2025-07-01$$wGermany
001049774 245__ $$aExploring Tradeoffs in Syngas production with Solid Oxide Electrolysis via Multi-objective Optimization
001049774 260__ $$c2025
001049774 3367_ $$033$$2EndNote$$aConference Paper
001049774 3367_ $$2DataCite$$aOther
001049774 3367_ $$2BibTeX$$aINPROCEEDINGS
001049774 3367_ $$2ORCID$$aLECTURE_SPEECH
001049774 3367_ $$0PUB:(DE-HGF)31$$2PUB:(DE-HGF)$$aTalk (non-conference)$$btalk$$mtalk$$s1765993030_31382$$xOther
001049774 3367_ $$2DINI$$aOther
001049774 520__ $$aSyngas 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 (SOEC) for use in methanol synthesis in the context of the DryHy project. This presentation discusses finding from an article “Exploring Tradeoffs in Syngas Production with Solid-Oxide Electrolysis via Multi-Objective Optimization” currently under review. An ASPEN Plus model is developed to investigate tradeoffs between competing objectives in SOEC-based syngas production. Two system configurations were examined: low utilization and high utilization designs. Four key performance metrics were evaluated: energy efficiency, stoichiometric number (SN), carbon oxide ratio, and inlet H₂O/CO₂ ratio.By comparing both designs, the high utilization design outperforms the low utilization design and a significant difference in the inlet H₂O/CO₂ ratio required for the same stoichiometry number exist.
001049774 536__ $$0G:(DE-HGF)POF4-1232$$a1232 - Power-based Fuels and Chemicals (POF4-123)$$cPOF4-123$$fPOF IV$$x0
001049774 536__ $$0G:(DE-Juel1)BMBF-03SF0716$$aBMBF-03SF0716A - Verbundvorhaben DryHy: Wasserbewusste Erzeugung von Wasserstoff und e-Fuels in trockenen Regionen (Phase 1), Teilvorhaben: Vorbereitung der Demonstationsphase durch Untersuchung und Entwicklung der Einzeltechnologien (BMBF-03SF0716)$$cBMBF-03SF0716$$x1
001049774 909CO $$ooai:juser.fz-juelich.de:1049774$$pVDB
001049774 9101_ $$0I:(DE-588b)5008462-8$$6P:(DE-Juel1)198866$$aForschungszentrum Jülich$$b0$$kFZJ
001049774 9101_ $$0I:(DE-588b)36225-6$$6P:(DE-Juel1)198866$$aRWTH Aachen$$b0$$kRWTH
001049774 9131_ $$0G:(DE-HGF)POF4-123$$1G:(DE-HGF)POF4-120$$2G:(DE-HGF)POF4-100$$3G:(DE-HGF)POF4$$4G:(DE-HGF)POF$$9G:(DE-HGF)POF4-1232$$aDE-HGF$$bForschungsbereich Energie$$lMaterialien und Technologien für die Energiewende (MTET)$$vChemische Energieträger$$x0
001049774 9141_ $$y2025
001049774 920__ $$lyes
001049774 9201_ $$0I:(DE-Juel1)IET-1-20110218$$kIET-1$$lGrundlagen der Elektrochemie$$x0
001049774 980__ $$atalk
001049774 980__ $$aVDB
001049774 980__ $$aI:(DE-Juel1)IET-1-20110218
001049774 980__ $$aUNRESTRICTED