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dc.contributor.authorSon, Jeong-Woo-
dc.contributor.authorKim, Jae-Hyun-
dc.contributor.authorKang, Jin-Kyu-
dc.contributor.authorKim, Song-Bae-
dc.contributor.authorPark, Jeong-Ann-
dc.contributor.authorLee, Chang-Gu-
dc.contributor.authorChoi, Jae-Woo-
dc.contributor.authorLee, Sang-Hyup-
dc.date.accessioned2024-01-20T03:34:42Z-
dc.date.available2024-01-20T03:34:42Z-
dc.date.created2021-09-03-
dc.date.issued2016-08-
dc.identifier.issn1944-3994-
dc.identifier.urihttps://pubs.kist.re.kr/handle/201004/123855-
dc.description.abstractIn this study, phosphate (P) removal from aqueous solutions by hydrocalumite was investigated using batch experiments and model analyses. The maximum phosphate removal capacity was determined to be 127.53mgP/g under the given experimental conditions (hydrocalumite dose=0.05g/L, initial P concentration=2-20mgP/L, reaction time=24h). Model analyses showed that the Elovich model was most suitable for describing the kinetic data, whereas the Redlich-Peterson model provided the best fits to the equilibrium data. Furthermore, phosphate removal by hydrocalumite was not sensitive to pH changes between 4.0 and 11.0. A thermodynamic analysis indicated that phosphate removal by hydrocalumite increased with a rise in temperature from 15 to 45 degrees C, suggesting that the removal process was spontaneous and endothermic (H degrees=32.05kJ/mol, S degrees=112.86J/K/mol, G degrees=-0.47 to -3.86kJ/mol). The phosphate removal capacity in stream water (5.40-17.25mgP/g) was also lower than that in a synthetic P solution (6.86-27.51mgP/g) under the given experimental conditions (initial P concentration=2mgP/L, hydrocalumite dose=0.05-0.3g/L, reaction time=24h). Such a result could possibly be ascribed to the presence of carbonate ions (CO32-) in the stream water, which could interfere with phosphate removal by hydrocalumite through the precipitation of calcium carbonate (CaCO3).-
dc.languageEnglish-
dc.publisherDESALINATION PUBL-
dc.titleAnalysis of phosphate removal from aqueous solutions by hydrocalumite-
dc.typeArticle-
dc.identifier.doi10.1080/19443994.2015.1119759-
dc.description.journalClass1-
dc.identifier.bibliographicCitationDESALINATION AND WATER TREATMENT, v.57, no.45, pp.21476 - 21486-
dc.citation.titleDESALINATION AND WATER TREATMENT-
dc.citation.volume57-
dc.citation.number45-
dc.citation.startPage21476-
dc.citation.endPage21486-
dc.description.isOpenAccessN-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.identifier.wosid000383400800030-
dc.identifier.scopusid2-s2.0-84948168024-
dc.relation.journalWebOfScienceCategoryEngineering, Chemical-
dc.relation.journalWebOfScienceCategoryWater Resources-
dc.relation.journalResearchAreaEngineering-
dc.relation.journalResearchAreaWater Resources-
dc.type.docTypeArticle-
dc.subject.keywordPlusLAYERED DOUBLE HYDROXIDES-
dc.subject.keywordPlusREGRESSION-ANALYSIS-
dc.subject.keywordPlusWASTE-WATER-
dc.subject.keywordPlusSORPTION-
dc.subject.keywordPlusKINETICS-
dc.subject.keywordPlusMG-
dc.subject.keywordPlusPHOSPHORUS-
dc.subject.keywordPlusEQUILIBRIUM-
dc.subject.keywordPlusADSORPTION-
dc.subject.keywordPlusDESORPTION-
dc.subject.keywordAuthorHydrocalumite-
dc.subject.keywordAuthorHydroxyapatite-
dc.subject.keywordAuthorLayered double hydroxide-
dc.subject.keywordAuthorPhosphate removal-
dc.subject.keywordAuthorPrecipitation-
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