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Development and performance investigation of a novel ultrasonic-assisted non-contact membrane distillation process to prevent membrane fouling

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dc.contributor.authorMyagmarsukh, Zolboo-
dc.contributor.authorKim, Yu-Bin-
dc.contributor.authorHam, Min-Gyu-
dc.contributor.authorJi, Ho-
dc.contributor.authorKim, Young-Deuk-
dc.date.accessioned2025-01-08T06:30:24Z-
dc.date.available2025-01-08T06:30:24Z-
dc.date.issued2024-12-
dc.identifier.issn0011-9164-
dc.identifier.issn1873-4464-
dc.identifier.urihttps://www.kriso.re.kr/sciwatch/handle/2021.sw.kriso/10634-
dc.description.abstractA novel non-contact membrane distillation (NCMD) process is proposed that prevents membrane fouling by preventing direct physical contact between the feed and membrane. The feed channel of the NCMD module is equipped with an ultrasonic transducer that provides high-frequency mechanical oscillations to the feed film, which forms a fine mist of droplets and water column. Experiments are conducted to determine the feed height required to maximize the evaporation rate, and the effects of feed temperature, flow rate, and ultrasonic power on the permeation flux. The results reveal that the highest permeation flux occurs at a feed height of 20 mm, and an increase in the feed height and flow rate decreases the ultrasonic cavitation effect, while a higher feed temperature and ultrasonic power significantly increases the permeation flux. At the feed temperature of 60 degrees C, feed flow rate of 1.0 L/min, and ultrasonic current of 600 mA, the permeation flux is 6.3 kg/m(2)h, which is 8.4 times greater than that of the NCMD process without ultrasonic treatment. The corresponding specific energy consumptions with and without the ultrasonication are 647 and 6028 kWh/m(3), respectively. Moreover, the long-term experimental results indicate that the proposed system is unaffected by high feed concentrations.-
dc.language영어-
dc.language.isoENG-
dc.publisherELSEVIER-
dc.titleDevelopment and performance investigation of a novel ultrasonic-assisted non-contact membrane distillation process to prevent membrane fouling-
dc.typeArticle-
dc.publisher.location네덜란드-
dc.identifier.doi10.1016/j.desal.2024.118108-
dc.identifier.scopusid2-s2.0-85204084494-
dc.identifier.wosid001322295600001-
dc.identifier.bibliographicCitationDESALINATION, v.592-
dc.citation.titleDESALINATION-
dc.citation.volume592-
dc.type.docTypeArticle-
dc.description.isOpenAccessN-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.relation.journalResearchAreaEngineering-
dc.relation.journalResearchAreaWater Resources-
dc.relation.journalWebOfScienceCategoryEngineering, Chemical-
dc.relation.journalWebOfScienceCategoryWater Resources-
dc.subject.keywordPlusDIRECT-CONTACT MEMBRANE-
dc.subject.keywordPlusCONCENTRATION POLARIZATION-
dc.subject.keywordPlusHEAT-TRANSFER-
dc.subject.keywordPlusFREQUENCY-
dc.subject.keywordPlusTEMPERATURE-
dc.subject.keywordPlusEVAPORATION-
dc.subject.keywordPlusMITIGATION-
dc.subject.keywordPlusCONFIGURATIONS-
dc.subject.keywordPlusSONOCHEMISTRY-
dc.subject.keywordPlusCONDENSATION-
dc.subject.keywordAuthorNon-contact membrane distillation-
dc.subject.keywordAuthorMass and heat transfer-
dc.subject.keywordAuthorUltrasonic-
dc.subject.keywordAuthorMembrane fouling-
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친환경해양개발연구본부 (해수에너지연구센터)
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