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dc.contributor.authorJo, Hoyong-
dc.contributor.authorLee, Min-Gu-
dc.contributor.authorPark, Jinwon-
dc.contributor.authorJung, Kwang-Deog-
dc.date.accessioned2024-01-20T02:04:03Z-
dc.date.available2024-01-20T02:04:03Z-
dc.date.created2021-09-01-
dc.date.issued2017-02-01-
dc.identifier.issn0360-5442-
dc.identifier.urihttps://pubs.kist.re.kr/handle/201004/123086-
dc.description.abstractIndirect carbonation is a suitable method for carbon dioxide (CO2) removal from the environment, and it requires an acid to dissolve the calcium ions and a base to precipitate the formed calcium carbonate (CaCO3). We herein report a new method to produce high-purity nano-CaCO3 (nCaCO(3)) from steel slag using hydrochloric acid (HCl) and sodium hydroxide (NaOH). The rate equation for the dissolution of calcium (Ca) in the slag was derived using a range of variables, such as temperatures, solid -to -liquid (S/L) ratio, and HCI concentration. The purified calcium hydroxide (Ca(OH)(2)) was converted into nCaCO(3) (size: 80-120 nm, purity: 98.5%) by carbonation with CO2, after impurities, such as iron (Fe), aluminum (Al), and Mg, were completely removed. An efficiency of 73% was obtained for the dissolution and precipitation steps when 0.50 M HCI and 1.0 M NaOH were employed to produce 1 ton/h of nano-CaCO3 with a purity of 98.5 wt%. Recently, a sodium chloride (NaCI) electrolysis system with low energy requirement was proposed to simultaneously produce HCl and NaOH. Assuming 90% faradic efficiency in the aforementioned NaCI electrolysis, process energies of 916 kWh/tCaCO(3) and 1462 kWh/tCaCO(3) were obtained at potentials of 0.83 V and 1.50 V, respectively. (C) 2016 Elsevier Ltd. All rights reserved.-
dc.languageEnglish-
dc.publisherPERGAMON-ELSEVIER SCIENCE LTD-
dc.subjectLAYERED DOUBLE HYDROXIDES-
dc.subjectCO2 MINERAL CARBONATION-
dc.subjectELECTROCHEMICAL-CELL-
dc.subjectSEQUESTRATION-
dc.subjectDISSOLUTION-
dc.subjectFIXATION-
dc.subjectDIOXIDE-
dc.subjectALKALI-
dc.subjectACID-
dc.subjectSERPENTINITE-
dc.titlePreparation of high-purity nano-CaCO3 from steel slag-
dc.typeArticle-
dc.identifier.doi10.1016/j.energy.2016.11.140-
dc.description.journalClass1-
dc.identifier.bibliographicCitationENERGY, v.120, pp.884 - 894-
dc.citation.titleENERGY-
dc.citation.volume120-
dc.citation.startPage884-
dc.citation.endPage894-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.identifier.wosid000395953000076-
dc.identifier.scopusid2-s2.0-85007496573-
dc.relation.journalWebOfScienceCategoryThermodynamics-
dc.relation.journalWebOfScienceCategoryEnergy & Fuels-
dc.relation.journalResearchAreaThermodynamics-
dc.relation.journalResearchAreaEnergy & Fuels-
dc.type.docTypeArticle-
dc.subject.keywordPlusLAYERED DOUBLE HYDROXIDES-
dc.subject.keywordPlusCO2 MINERAL CARBONATION-
dc.subject.keywordPlusELECTROCHEMICAL-CELL-
dc.subject.keywordPlusSEQUESTRATION-
dc.subject.keywordPlusDISSOLUTION-
dc.subject.keywordPlusFIXATION-
dc.subject.keywordPlusDIOXIDE-
dc.subject.keywordPlusALKALI-
dc.subject.keywordPlusACID-
dc.subject.keywordPlusSERPENTINITE-
dc.subject.keywordAuthorSteel slag-
dc.subject.keywordAuthorAlkali metal ion dissolution-
dc.subject.keywordAuthorMineral carbonation-
dc.subject.keywordAuthorNano-CaCO3-
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