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dc.contributor.authorTun, Lat Lat-
dc.contributor.authorJeong, Dawoon-
dc.contributor.authorJeong, Seongpil-
dc.contributor.authorCho, Kyungjin-
dc.contributor.authorLee, Seockheon-
dc.contributor.authorBae, Hyokwan-
dc.date.accessioned2024-01-20T03:34:24Z-
dc.date.available2024-01-20T03:34:24Z-
dc.date.created2021-09-04-
dc.date.issued2016-08-
dc.identifier.issn0376-7388-
dc.identifier.urihttps://pubs.kist.re.kr/handle/201004/123837-
dc.description.abstractThe nitrogen content of a synthetic ammonia wastewater was concentrated using direct contact membrane distillation (DCMD). The ratio of transferred ammonia to water (i.e., specific ammonia transfer: SAT) was controlled by operational conditions. With 20 degrees C on the permeate side, and a high temperature of 70 degrees C on the feed side, the process exhibited low SAT values for PTFE/PP (PTF045LD0A), PTFE/PP (TF-450), and PVDF (HVHP-14250) membranes. This was because the increase in water flux ( >24 L/m(2) h) was greater than that of ammonia transfer. A positive relationship between SAT and free ammonia concentration was identified under different total ammoniacal nitrogen concentration and pH. The acidification pretreatment to pH 5 led to further reduction in the SAT value (as low as 6.91 x 10(-5) g-N/g-H2O). As a practical application, the dewatering process of source-separated human urine by DCMD required an additional filtration step to prevent fouling, but the filtration had an insignificant effect on the SAT. For the acidified and filtered source-separated human urine, total ammoniacal nitrogen was successfully concentrated with a low SAT value ( < 2.06 x 10(-3) g-N/g-H2O). (C) 2016 Elsevier B.V. All rights reserved.-
dc.languageEnglish-
dc.publisherElsevier BV-
dc.titleDewatering of source-separated human urine for nitrogen recovery by membrane distillation-
dc.typeArticle-
dc.identifier.doi10.1016/j.memsci.2016.04.004-
dc.description.journalClass1-
dc.identifier.bibliographicCitationJournal of Membrane Science, v.512, pp.13 - 20-
dc.citation.titleJournal of Membrane Science-
dc.citation.volume512-
dc.citation.startPage13-
dc.citation.endPage20-
dc.description.isOpenAccessN-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.identifier.wosid000375421000002-
dc.identifier.scopusid2-s2.0-84962815343-
dc.relation.journalWebOfScienceCategoryEngineering, Chemical-
dc.relation.journalWebOfScienceCategoryPolymer Science-
dc.relation.journalResearchAreaEngineering-
dc.relation.journalResearchAreaPolymer Science-
dc.type.docTypeArticle-
dc.subject.keywordPlusECOLOGICAL SANITATION-
dc.subject.keywordPlusAMMONIA RECOVERY-
dc.subject.keywordPlusWASTE-WATER-
dc.subject.keywordPlusDESALINATION-
dc.subject.keywordPlusPRECIPITATION-
dc.subject.keywordPlusPERFORMANCE-
dc.subject.keywordPlusREMOVAL-
dc.subject.keywordPlusMODEL-
dc.subject.keywordPlusSCALE-
dc.subject.keywordAuthorHuman urine-
dc.subject.keywordAuthorAmmonia enrichment-
dc.subject.keywordAuthorMembrane distillation-
dc.subject.keywordAuthorAcidification-
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KIST Article > 2016
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