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dc.contributor.authorLee, Ki Yong-
dc.contributor.authorKim, Hoon Sik-
dc.contributor.authorKim, Chang Soo-
dc.contributor.authorJung, Kwang-Deog-
dc.date.accessioned2024-01-20T18:32:47Z-
dc.date.available2024-01-20T18:32:47Z-
dc.date.created2021-09-04-
dc.date.issued2010-10-
dc.identifier.issn0360-3199-
dc.identifier.urihttps://pubs.kist.re.kr/handle/201004/131083-
dc.description.abstractThe solubility behavior of SO2 in 1-butyl-3-methylimidazolium acetate ([BMIm][OAc]) was investigated. The solubility of SO2 in [BMIm][OAc] was measured to be 0.6 in mole fraction at 50 degrees C in a stream of SO2 gas. The desorption of SO2 from [BMIm][OAc] was never completed, until the temperature was raised to 170 degrees C in a stream of N-2, indicating that the absorption of SO2 is irreversible at the experimental condition. An in-situ IR study showed that acetate anion in [BMIm][OAc] transformed into acetic acid during the SO2 absorption. After removing acetic acid at 170 degrees C by evacuation, the bands at 1210, 1045 and 850 cm(-1) appeared in IR spectra. The bands at 1210 and 1047 cm(-1) were assigned to S-O stretching mode of HOSO2- (an isomer of HSO3-) and the band at 885 cm(-1) was assigned to the symmetric stretching mode of HO-S. FT-IR study suggested that acetic acid and most plausibly [BMIm][HOSO2] were generated from the interactions of [BMIm][OAc] with SO2 and adventitious water in feed gas and/or [BMIm][OAc] during absorption-desorption process. [BMIm][HOSO2] recovered after removing acetic acid was found to be a new and reversible SO2 absorbent with the SO2 absorption capacity of 0.55 in mole fraction. (C) 2010 Professor T. Nejat Veziroglu. Published by Elsevier Ltd. All rights reserved.-
dc.languageEnglish-
dc.publisherPERGAMON-ELSEVIER SCIENCE LTD-
dc.subjectWATER-SPLITTING CYCLE-
dc.subjectIONIC LIQUIDS-
dc.subjectSULFUR-DIOXIDE-
dc.subjectFLUE-GAS-
dc.subjectINFRARED-SPECTROSCOPY-
dc.subjectSOLUBILITY-
dc.titleBehaviors of SO2 absorption in [BMIm][OAc] as an absorbent to recover SO2 in thermochemical processes to produce hydrogen-
dc.typeArticle-
dc.identifier.doi10.1016/j.ijhydene.2010.07.128-
dc.description.journalClass1-
dc.identifier.bibliographicCitationINTERNATIONAL JOURNAL OF HYDROGEN ENERGY, v.35, no.19, pp.10173 - 10178-
dc.citation.titleINTERNATIONAL JOURNAL OF HYDROGEN ENERGY-
dc.citation.volume35-
dc.citation.number19-
dc.citation.startPage10173-
dc.citation.endPage10178-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.identifier.wosid000283977100018-
dc.identifier.scopusid2-s2.0-77957283202-
dc.relation.journalWebOfScienceCategoryChemistry, Physical-
dc.relation.journalWebOfScienceCategoryElectrochemistry-
dc.relation.journalWebOfScienceCategoryEnergy & Fuels-
dc.relation.journalResearchAreaChemistry-
dc.relation.journalResearchAreaElectrochemistry-
dc.relation.journalResearchAreaEnergy & Fuels-
dc.type.docTypeArticle-
dc.subject.keywordPlusWATER-SPLITTING CYCLE-
dc.subject.keywordPlusIONIC LIQUIDS-
dc.subject.keywordPlusSULFUR-DIOXIDE-
dc.subject.keywordPlusFLUE-GAS-
dc.subject.keywordPlusINFRARED-SPECTROSCOPY-
dc.subject.keywordPlusSOLUBILITY-
dc.subject.keywordAuthorThermochemical water splitting cycle-
dc.subject.keywordAuthorSulfur dioxide absorbent-
dc.subject.keywordAuthorSulfur dioxide separation-
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