Hydrogen production in fluidized bed by chemical-looping cycle

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dc.contributor.authorJin, Gyoung Taeko
dc.contributor.authorRyu, Ho-Jungko
dc.contributor.authorJo, Sung-Hoko
dc.contributor.authorLee, Seung-Yongko
dc.contributor.authorSon, Sung Realko
dc.contributor.authorKim, Sang Doneko
dc.date.accessioned2008-05-09T09:14:08Z-
dc.date.available2008-05-09T09:14:08Z-
dc.date.created2012-02-06-
dc.date.created2012-02-06-
dc.date.issued2007-05-
dc.identifier.citationKOREAN JOURNAL OF CHEMICAL ENGINEERING, v.24, no.3, pp.542 - 546-
dc.identifier.issn0256-1115-
dc.identifier.urihttp://hdl.handle.net/10203/4481-
dc.descriptionThis work was presented at the 6th Korea-China Workshop on Clean Energy Technology held at Busan, Korea, July 4-7, 2006.en
dc.description.abstractTo investigate the feasibility of a chemical-looping hydrogen generation system, we investigated the reduction and water splitting reaction characteristics for three mediators and two reducing gas in a bubbling fluidized bed reactor (0.02 in I.D.). For three oxygen carrier particles (NiO/bentonite, Fe2O3/bentonite, (NiO: Fe2O3)/bentonite), hydrogen was used as a reduction gas and water was used as an oxidation gas. For (NiO : Fe2O3)/bentonite particle, carbon monoxide, which is the main component in the syngas from coal or heavy residue, was used as a reducing gas to check reactivity for the carbon containing fuels and carbon deposition characteristics. Based on the reactivity tests, (NiO : Fe2O3)/bentonite particle was selected as the best mediator for the chemical-looping hydrogen generation system to achieve stable continuous operation.-
dc.description.sponsorshipThis work was supported by Ministry of Commerce, Industry and Energy (MOCIE) and Korea Research Council of Public Science & Technology (KORP).en
dc.languageEnglish-
dc.language.isoen_USen
dc.publisherSpringer-
dc.subjectOXYGEN CARRIER PARTICLES-
dc.subjectCO2 CAPTURE-
dc.subjectREACTIVITY-
dc.titleHydrogen production in fluidized bed by chemical-looping cycle-
dc.typeArticle-
dc.identifier.wosid000247263200031-
dc.identifier.scopusid2-s2.0-36949018449-
dc.type.rimsART-
dc.citation.volume24-
dc.citation.issue3-
dc.citation.beginningpage542-
dc.citation.endingpage546-
dc.citation.publicationnameKOREAN JOURNAL OF CHEMICAL ENGINEERING-
dc.embargo.liftdate9999-12-31-
dc.embargo.terms9999-12-31-
dc.contributor.localauthorKim, Sang Done-
dc.contributor.nonIdAuthorJin, Gyoung Tae-
dc.contributor.nonIdAuthorRyu, Ho-Jung-
dc.contributor.nonIdAuthorJo, Sung-Ho-
dc.contributor.nonIdAuthorLee, Seung-Yong-
dc.contributor.nonIdAuthorSon, Sung Real-
dc.type.journalArticleArticle; Proceedings Paper-
dc.subject.keywordAuthorchemical-looping cycle-
dc.subject.keywordAuthorhydrogen production-
dc.subject.keywordAuthorinherent CO2-
dc.subject.keywordAuthorcapture-
dc.subject.keywordAuthorredox-
dc.subject.keywordAuthormediator-
dc.subject.keywordPlusOXYGEN CARRIER PARTICLES-
dc.subject.keywordPlusCO2 CAPTURE-
dc.subject.keywordPlusREACTIVITY-
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