Full metadata record

DC Field Value Language
dc.contributor.authorBaik, Chaekyung-
dc.contributor.authorChoi, Jihyun-
dc.contributor.authorKwon, Dayoung-
dc.contributor.authorYang, Chaeyeon-
dc.contributor.authorLee, Suji-
dc.contributor.authorSung, Yung-Eun-
dc.contributor.authorKim, Wooyul-
dc.contributor.authorPark, Hyun S.-
dc.date.accessioned2026-05-11T09:30:13Z-
dc.date.available2026-05-11T09:30:13Z-
dc.date.created2026-05-07-
dc.date.issued2026-05-
dc.identifier.issn1385-8947-
dc.identifier.urihttps://pubs.kist.re.kr/handle/201004/154737-
dc.description.abstractLow-temperature NH3 electrolysis has emerged as a promising method for carbon-free H2 production, utilizing NH3 as a cost-effective H2 carrier. While most research has focused on NH3 oxidation catalysts, the efficiency, stability, and scalability of NH3 dehydrogenation devices remain underexplored. Here, low-temperature NH3 electrolyzers achieving peak current densities over 1.5 A cm−2 are demonstrated with high efficiency and stability. Electrochemical and chemical regeneration protocols were developed to enhance coulombic efficiency and durability. Using these protocols, ∼90% coulombic efficiency was sustained at 0.67 A cm−2 for 50 min without degradation. Surface poisoning behaviors under different protocols were examined by combining in-situ ATR-SEIRAS (attenuated total reflectance surface-enhanced infrared absorption spectroscopy) with electrochemical analysis. Finally, a 40 W NH3 electrolyzer stack with a 25 cm2, 3-cell configuration showed stable operation at 0.72 A cm−2 for 200 min, with a degradation rate of 75.7 μA cm−2 min−1 under voltage swing operation. This work establishes a systematic approach to low-temperature NH3 electrolysis, enabling stable and efficient intermittent H2 production.-
dc.languageEnglish-
dc.publisherElsevier BV-
dc.titleEfficient and stable 40 W-class low-temperature NH3 electrolyzers for intermittent H2 production-
dc.typeArticle-
dc.identifier.doi10.1016/j.cej.2026.175681-
dc.description.journalClass1-
dc.identifier.bibliographicCitationChemical Engineering Journal, v.536-
dc.citation.titleChemical Engineering Journal-
dc.citation.volume536-
dc.description.isOpenAccessN-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.identifier.wosid001742366600001-
dc.relation.journalWebOfScienceCategoryEngineering, Environmental-
dc.relation.journalWebOfScienceCategoryEngineering, Chemical-
dc.relation.journalResearchAreaEngineering-
dc.type.docTypeArticle-
dc.subject.keywordPlusADSORPTION-
dc.subject.keywordPlusELECTRODE-
dc.subject.keywordPlusSURFACE-
dc.subject.keywordPlusNO-
dc.subject.keywordPlusELECTROCHEMICAL AMMONIA OXIDATION-
dc.subject.keywordPlusHYDROGEN-PRODUCTION-
dc.subject.keywordPlusNITRIC-OXIDE-
dc.subject.keywordPlusTHIN-FILMS-
dc.subject.keywordPlusPT(100)-
dc.subject.keywordPlusELECTROCATALYSIS-
dc.subject.keywordAuthorAmmonia electrolysis-
dc.subject.keywordAuthorammonia oxidation reaction-
dc.subject.keywordAuthorSurface regeneration-
dc.subject.keywordAuthorVoltage swing operation-
dc.subject.keywordAuthorammonia electrolyzer stack-
Appears in Collections:
KIST Article > 2026
Export
RIS (EndNote)
XLS (Excel)
XML

qrcode

Items in DSpace are protected by copyright, with all rights reserved, unless otherwise indicated.

BROWSE