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Lim, Hankwon
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dc.citation.startPage 154405 -
dc.citation.title INTERNATIONAL JOURNAL OF HYDROGEN ENERGY -
dc.citation.volume 225 -
dc.contributor.author Gu, Jiwon -
dc.contributor.author Kim, Youngmin -
dc.contributor.author Im, Younghwan -
dc.contributor.author Kim, Min Sik -
dc.contributor.author Ni, Aleksey -
dc.contributor.author Chae, Ho-Jeong -
dc.contributor.author Lim, Hankwon -
dc.date.accessioned 2026-04-13T09:30:24Z -
dc.date.available 2026-04-13T09:30:24Z -
dc.date.created 2026-03-30 -
dc.date.issued 2026-04 -
dc.description.abstract As hydrogen demand increases in the transition toward a carbon-neutral society, solutions for hydrogen storage and transportation are necessary. Among the various options, ammonia is a promising hydrogen carrier due to its high volumetric density, and ammonia cracking process is indispensable to regenerate hydrogen. However, because ammonia cracking is energy-intensive, the development of large-scale ammonia cracking reactors with energy efficient heat management system is essential to ensure reliable hydrogen supply to satisfy hydrogen demand. In this work, a numerical model of shell-and-tube ammonia cracking reactor suitable for both centralized and distributed type plants is developed, employing molten salt as the heat transfer fluid to achieve uniform and efficient heat supply. When the ammonia temperature is sufficiently raised, conversion exceeding 75% and 83.1% of energy efficiency are achieved, while the molten salt exhibited only 22.6% temperature drop compared with the corresponding gas flow temperature rise. The reactor performances for various tube lengths or diameters yield conversion rates from 65 to 88%, indicating that a molten salt-heated shell-and-tube ammonia cracker can be designed as a compact reactor. Furthermore, sensitivity analyses of key parameters, including inlet temperatures, pressure, and space velocity, are found to have strong influence on temperature profiles and reaction progress, and the small multi-tubular model remains the performance well similar for the singular tube system. This study demonstrates for the first time via a CFD conceptual design of ammonia cracker, that molten salt heating is viable for maintaining uniform temperature gradients (<40 degrees C) and achieve >65% NH(3 )conversion rate in compact ammonia cracking reactor under industrial-grade gas hourly sapce velocity (GHSV), providing a viable design pathway for demonstration of large-scale ammonia crackers and contributing to the realization of an integrated hydrogen value chain. -
dc.identifier.bibliographicCitation INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, v.225, pp.154405 -
dc.identifier.doi 10.1016/j.ijhydene.2026.154405 -
dc.identifier.issn 0360-3199 -
dc.identifier.uri https://scholarworks.unist.ac.kr/handle/201301/91331 -
dc.identifier.url https://www.sciencedirect.com/science/article/pii/S0360319926010426?pes=vor&utm_source=clarivate&getft_integrator=clarivate -
dc.identifier.wosid 001718806900001 -
dc.language 영어 -
dc.publisher PERGAMON-ELSEVIER SCIENCE LTD -
dc.title Conceptual CFD design of a molten salt-heated ammonia cracking reactor for efficient hydrogen production -
dc.type Article -
dc.description.isOpenAccess FALSE -
dc.relation.journalWebOfScienceCategory Chemistry, Physical; Electrochemistry; Energy & Fuels -
dc.relation.journalResearchArea Chemistry; Electrochemistry; Energy & Fuels -
dc.type.docType Article -
dc.description.journalRegisteredClass scie -
dc.description.journalRegisteredClass scopus -
dc.subject.keywordAuthor Ammonia cracking -
dc.subject.keywordAuthor Computation fluid dynamics -
dc.subject.keywordAuthor Molten salt -
dc.subject.keywordAuthor Shell-and-tube reactor -
dc.subject.keywordPlus ENERGY -
dc.subject.keywordPlus COMMERCIAL RU/AL2O3 CATALYST -
dc.subject.keywordPlus DECOMPOSITION -

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