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dc.contributor.authorPark, Jeong-Ann-
dc.contributor.authorJung, Sung-Mok-
dc.contributor.authorChoi, Jae-Woo-
dc.contributor.authorKim, Jae-Hyun-
dc.contributor.authorHong, Seungkwan-
dc.contributor.authorLee, Sang-Hyup-
dc.date.accessioned2024-01-19T23:32:16Z-
dc.date.available2024-01-19T23:32:16Z-
dc.date.created2021-09-03-
dc.date.issued2018-02-
dc.identifier.issn0045-6535-
dc.identifier.urihttps://pubs.kist.re.kr/handle/201004/121762-
dc.description.abstractMicrocystin-LR (MC-LR) is a growing issue as it is toxic and difficult to remove in drinking water treatment plants (DWTPs). Mesoporous carbon (MC) is evaluated as an alternative adsorbent for MC-LR removal and compared with three widely-used powdered activated carbons (PACs). MC was more favorable for MC-LR removal than PACs. MC-LR adsorption on MC was a rapid process (k(2) = 1.02 x 10(-4) g/mu g/min) that completed within 15 min, while adsorption on PACs took 60 min. The maximum adsorption capacity of MC-LR was 18,008 mu g/g (MC), which was higher than that of the PACs. Two mechanisms were associated with adsorption: the small hydro-dynamic diameter of MC in an aqueous solution increased the instantaneous attraction of MC-LR to its surface, and the numerous mesopores enhanced pore diffusion. The MC could remove MC-LR to meet the drinking water guidance level (1 mu g/L) from an the MC-LR concentration range of 5-20 mu g/L. in drinking water sources, and 10 min of treatment was sufficient to meet this level (MC dose = 20 mg/L). The field-scale DWTP was operated by adding 1 or 5 mg/L MC to the mixing basin, and 49.49% and 74.50% of MC-LR was removed, respectively. Geosmin and 2-methylisoborneol were slightly reduced when 5 mg/L of MC was applied. (C) 2017 Elsevier Ltd. All rights reserved.-
dc.languageEnglish-
dc.publisherPERGAMON-ELSEVIER SCIENCE LTD-
dc.titleMesoporous carbon for efficient removal of microcystin-LR in drinking water sources, Nak-Dong River, South Korea: Application to a field-scale drinking water treatment plant-
dc.typeArticle-
dc.identifier.doi10.1016/j.chemosphere.2017.11.092-
dc.description.journalClass1-
dc.identifier.bibliographicCitationCHEMOSPHERE, v.193, pp.883 - 891-
dc.citation.titleCHEMOSPHERE-
dc.citation.volume193-
dc.citation.startPage883-
dc.citation.endPage891-
dc.description.isOpenAccessN-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.identifier.wosid000423890500104-
dc.identifier.scopusid2-s2.0-85034857583-
dc.relation.journalWebOfScienceCategoryEnvironmental Sciences-
dc.relation.journalResearchAreaEnvironmental Sciences & Ecology-
dc.type.docTypeArticle-
dc.subject.keywordPlusPOWDERED ACTIVATED CARBON-
dc.subject.keywordPlusADVANCED OXIDATION PROCESSES-
dc.subject.keywordPlusPHOTOCATALYTIC DESTRUCTION-
dc.subject.keywordPlusAQUEOUS-SOLUTIONS-
dc.subject.keywordPlusADSORPTION-
dc.subject.keywordPlusCYANOBACTERIA-
dc.subject.keywordPlusDEGRADATION-
dc.subject.keywordPlusCYANOTOXINS-
dc.subject.keywordPlusTOXIN-
dc.subject.keywordPlusPRODUCTS-
dc.subject.keywordAuthorMesoporous carbon-
dc.subject.keywordAuthorCyanobacterial bloom-
dc.subject.keywordAuthorMicrocystin-LR-
dc.subject.keywordAuthorPore diffusion-
dc.subject.keywordAuthorDrinking water treatment plant-
dc.subject.keywordAuthorField-scale study-
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