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Hydrogen production by SI process, with electrodialysis stack embedded in HI decomposition

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dc.contributor.authorKang, Kyoung-Soo-
dc.contributor.authorKim, Chang-Hee-
dc.contributor.authorKim, Jong-Won-
dc.contributor.authorCho, Won-Chul-
dc.contributor.authorJeong, Seong-Uk-
dc.contributor.authorPark, Chu-Sik-
dc.contributor.authorPark, Byung-Heung-
dc.contributor.authorKang, Jeong-Won-
dc.contributor.authorBae, Ki-Kwang-
dc.date.accessioned2021-09-04T01:55:46Z-
dc.date.available2021-09-04T01:55:46Z-
dc.date.created2021-06-17-
dc.date.issued2016-03-02-
dc.identifier.issn0360-3199-
dc.identifier.urihttps://scholar.korea.ac.kr/handle/2021.sw.korea/89245-
dc.description.abstractHydrogen production by the sulfur-iodine (SI) process, with an electrodialysis (ED) stack embedded in the HI decomposition section (SEC3) to concentrate HI in the HIx solution and overcome the pseudo-azeotrope, was conducted under pressurized conditions. The HIx solution of H2O/HI = 5.63-6.13 and I-2/HI = 0.57-1.97 was supplied to the SEC3. HI gas was concentrated in a packed distillation column and decomposed over Pt/Al2O3. The experimental results of distillation column operation under different feed rates and HIx compositions are reported. The raffinate from the column showed a pseudo-azeotropic Hlx mixture, as predicted in previous research. The dynamic responses of the ED stack were examined during the start-up period according to the HIx feed composition at the anode inlet. The ED voltage changed with the I-2 concentration in the inlet flow. The proton transport number (t(+)) and electro-osmosis coefficient (beta) were estimated for the ED stack during the operations. Hydrogen production ranged from 18.3 to 50 L/h, depending on the operating conditions and HIx feed composition. Copyright (c) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.-
dc.languageEnglish-
dc.language.isoen-
dc.publisherPERGAMON-ELSEVIER SCIENCE LTD-
dc.subjectIODINE THERMOCHEMICAL CYCLE-
dc.subjectELECTRO-ELECTRODIALYSIS-
dc.subjectHI-I-2-H2O MIXTURE-
dc.subjectLIQUID-EQUILIBRIA-
dc.subjectEFFICIENCY-
dc.subjectSYSTEM-
dc.titleHydrogen production by SI process, with electrodialysis stack embedded in HI decomposition-
dc.typeArticle-
dc.contributor.affiliatedAuthorKang, Jeong-Won-
dc.identifier.doi10.1016/j.ijhydene.2015.12.101-
dc.identifier.scopusid2-s2.0-85027942943-
dc.identifier.wosid000372563000005-
dc.identifier.bibliographicCitationINTERNATIONAL JOURNAL OF HYDROGEN ENERGY, v.41, no.8, pp.4560 - 4569-
dc.relation.isPartOfINTERNATIONAL JOURNAL OF HYDROGEN ENERGY-
dc.citation.titleINTERNATIONAL JOURNAL OF HYDROGEN ENERGY-
dc.citation.volume41-
dc.citation.number8-
dc.citation.startPage4560-
dc.citation.endPage4569-
dc.type.rimsART-
dc.type.docTypeArticle-
dc.description.journalClass1-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.relation.journalResearchAreaChemistry-
dc.relation.journalResearchAreaElectrochemistry-
dc.relation.journalResearchAreaEnergy & Fuels-
dc.relation.journalWebOfScienceCategoryChemistry, Physical-
dc.relation.journalWebOfScienceCategoryElectrochemistry-
dc.relation.journalWebOfScienceCategoryEnergy & Fuels-
dc.subject.keywordPlusIODINE THERMOCHEMICAL CYCLE-
dc.subject.keywordPlusELECTRO-ELECTRODIALYSIS-
dc.subject.keywordPlusHI-I-2-H2O MIXTURE-
dc.subject.keywordPlusLIQUID-EQUILIBRIA-
dc.subject.keywordPlusEFFICIENCY-
dc.subject.keywordPlusSYSTEM-
dc.subject.keywordAuthorSulfur-iodine process-
dc.subject.keywordAuthorElectrodialysis-
dc.subject.keywordAuthorNuclear hydrogen-
dc.subject.keywordAuthorThermochemical cycle-
dc.subject.keywordAuthorWater splitting-
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