{"@context":{"@vocab":"https://cir.nii.ac.jp/schema/1.0/","rdfs":"http://www.w3.org/2000/01/rdf-schema#","dc":"http://purl.org/dc/elements/1.1/","dcterms":"http://purl.org/dc/terms/","foaf":"http://xmlns.com/foaf/0.1/","prism":"http://prismstandard.org/namespaces/basic/2.0/","cinii":"http://ci.nii.ac.jp/ns/1.0/","datacite":"https://schema.datacite.org/meta/kernel-4/","ndl":"http://ndl.go.jp/dcndl/terms/","jpcoar":"https://github.com/JPCOAR/schema/blob/master/2.0/"},"@id":"https://cir.nii.ac.jp/crid/1390014746557045504.json","@type":"Article","productIdentifier":[{"identifier":{"@type":"DOI","@value":"10.15261/serdj.30.159"}},{"identifier":{"@type":"NDL_BIB_ID","@value":"032987698"}},{"identifier":{"@type":"URI","@value":"http://id.ndl.go.jp/bib/032987698"}},{"identifier":{"@type":"URI","@value":"https://ndlsearch.ndl.go.jp/books/R000000004-I032987698"}},{"identifier":{"@type":"URI","@value":"https://www.jstage.jst.go.jp/article/serdj/30/2/30_159/_pdf"}}],"dc:title":[{"@language":"en","@value":"Flow Characteristics and Mass-Transfer in Droplet Layer Formed in an Emulsion-Flow Column by Using Extraction of Iodine from Organic Phase"}],"dc:language":"en","description":[{"type":"abstract","notation":[{"@language":"en","@value":"<p>The novel extraction method called \"emulsion-flow\" is characterized by using a layer of accumulated droplets in the column to supply both phases in the form of droplets. To clarify the flow behavior of both phases in the layer, extraction of iodine from organic to aqueous phase was carried out to enhance visibility of organic phase with the help of iodine. In addition, the mass-transfer in the organic phase was examined by extracting iodine from organic phase to aqueous Na<sub>2</sub>S<sub>2</sub>O<sub>3</sub> solution. The results indicated that two phases in the droplet layer were in the state of O/W/O emulsion where most of the water flows down in the form of film around the droplets. Also, progress of coalescence of organic-phase droplets during extraction of iodine from organic phase was observed. The height of droplet layer increased with the square of organic phase flow velocity. The trend was the same as that observed for extraction of iodine from the aqueous phase. The mass-transfer capacity coefficient of the organic phase increased linearly with the organic-phase flow velocity, with a small dependence on the aqueous-phase flow velocity. The trend of the distribution of iodine concentration in the column was predicted by solving the convection-diffusion equation with an appropriate setting of the Peclet number. </p>"}],"abstractLicenseFlag":"disallow"}],"creator":[{"@id":"https://cir.nii.ac.jp/crid/1410014746557045506","@type":"Researcher","foaf:name":[{"@language":"en","@value":"AKAHOSHI Kaoru"}],"jpcoar:affiliationName":[{"@language":"en","@value":"Department of Chemical Engineering, Kagoshima University"}]},{"@id":"https://cir.nii.ac.jp/crid/1410014746557045507","@type":"Researcher","foaf:name":[{"@language":"en","@value":"HIRAYAMA Mikiro"}],"jpcoar:affiliationName":[{"@language":"en","@value":"Department of Chemical Engineering, Nagoya University"}]},{"@id":"https://cir.nii.ac.jp/crid/1410014746557045509","@type":"Researcher","foaf:name":[{"@language":"en","@value":"ZHANG Ming"}],"jpcoar:affiliationName":[{"@language":"en","@value":"Department of Chemical Engineering, Kagoshima University"}]},{"@id":"https://cir.nii.ac.jp/crid/1410014746557045505","@type":"Researcher","foaf:name":[{"@language":"en","@value":"GOSHIMA Takashi"}],"jpcoar:affiliationName":[{"@language":"en","@value":"Department of Chemical Engineering, Kagoshima University"}]},{"@id":"https://cir.nii.ac.jp/crid/1410014746557045508","@type":"Researcher","foaf:name":[{"@language":"en","@value":"MIZUTA Kei"}],"jpcoar:affiliationName":[{"@language":"en","@value":"Department of Chemical Engineering, Kagoshima University"}]},{"@id":"https://cir.nii.ac.jp/crid/1410014746557045504","@type":"Researcher","foaf:name":[{"@language":"en","@value":"NII Susumu"}],"jpcoar:affiliationName":[{"@language":"en","@value":"Department of Chemical Engineering, Kagoshima University"}]}],"publication":{"publicationIdentifier":[{"@type":"PISSN","@value":"13417215"},{"@type":"LISSN","@value":"13417215"},{"@type":"EISSN","@value":"21884765"},{"@type":"NDL_BIB_ID","@value":"000000156123"},{"@type":"ISSN","@value":"13417215"},{"@type":"NCID","@value":"AA11114608"}],"prism:publicationName":[{"@language":"en","@value":"Solvent Extraction Research and Development, Japan"},{"@language":"ja","@value":"Solvent Extraction Research and Development, Japan"},{"@language":"en","@value":"SERDJ"},{"@language":"ja","@value":"抽出学会誌"}],"dc:publisher":[{"@language":"en","@value":"Japan Association of Solvent Extraction"},{"@language":"ja","@value":"日本溶媒抽出学会"}],"prism:publicationDate":"2023","prism:volume":"30","prism:number":"2","prism:startingPage":"159","prism:endingPage":"167"},"reviewed":"false","dcterms:accessRights":"http://purl.org/coar/access_right/c_abf2","url":[{"@id":"http://id.ndl.go.jp/bib/032987698"},{"@id":"https://ndlsearch.ndl.go.jp/books/R000000004-I032987698"},{"@id":"https://www.jstage.jst.go.jp/article/serdj/30/2/30_159/_pdf"}],"availableAt":"2023","foaf:topic":[{"@id":"https://cir.nii.ac.jp/all?q=General%20Chemical%20Engineering","dc:title":"General Chemical Engineering"},{"@id":"https://cir.nii.ac.jp/all?q=General%20Chemistry","dc:title":"General Chemistry"}],"relatedProduct":[{"@id":"https://cir.nii.ac.jp/crid/1360016867010612736","@type":"Article","relationType":["references"],"jpcoar:relatedTitle":[{"@value":"Mass transfer during drop formation on the nozzle: New flow expansion model"}]},{"@id":"https://cir.nii.ac.jp/crid/1360861292711350400","@type":"Article","relationType":["references"],"jpcoar:relatedTitle":[{"@value":"Mass Transfer to Drops"}]},{"@id":"https://cir.nii.ac.jp/crid/1363107370958012032","@type":"Article","relationType":["references"],"jpcoar:relatedTitle":[{"@value":"Study of drop coalescence behavior for liquid–liquid extraction operation"}]},{"@id":"https://cir.nii.ac.jp/crid/1363670320299700736","@type":"Article","relationType":["references"],"jpcoar:relatedTitle":[{"@value":"Mass transfer enhancement through Marangoni instabilities during single drop formation"}]},{"@id":"https://cir.nii.ac.jp/crid/1390001204508335872","@type":"Article","relationType":["references"],"jpcoar:relatedTitle":[{"@language":"en","@value":"Mass transfer coefficients in a flat type supported liquid membrane."},{"@value":"平膜含浸型液膜装置における物質移動係数"},{"@language":"ja-Kana","@value":"ヒラ マク ガンシンガタ エキマク ソウチ ニ オケル ブッシツ イドウ ケイ"}]},{"@id":"https://cir.nii.ac.jp/crid/1390001205185462272","@type":"Article","relationType":["references"],"jpcoar:relatedTitle":[{"@language":"en","@value":"Continuous Extraction of Uranium from Actual Uranium-Containing Liquid Wastes Using an “Emulsion Flow” Extractor"},{"@language":"ja","@value":"エマルションフロー法による人形峠ウラン廃液からのウランの連続抽出"},{"@language":"ja-Kana","@value":"エマルションフローホウ ニ ヨル ニンギョウトウゲ ウラン ハイエキ カラ ノ ウラン ノ レンゾク チュウシュツ"},{"@value":"Continuous Extraction of Uranium from Actual Uranium-Containing Liquid Wastes Using an ^|^ldquo;Emulsion Flow^|^rdquo; Extractor"}]},{"@id":"https://cir.nii.ac.jp/crid/1390001206419090560","@type":"Article","relationType":["references"],"jpcoar:relatedTitle":[{"@language":"en","@value":"The Size of Drops Formed from Single Nozzles in Liquid-Liquid Systems"},{"@value":"単一孔から生成する液滴の大きさについて"}]},{"@id":"https://cir.nii.ac.jp/crid/1390006817998385280","@type":"Article","relationType":["references"],"jpcoar:relatedTitle":[{"@language":"en","@value":"Axial Mixing in Emulsion-flow Column under Iodine Extraction"}]},{"@id":"https://cir.nii.ac.jp/crid/1390282679237125632","@type":"Article","resourceType":"学術雑誌論文(journal article)","relationType":["references"],"jpcoar:relatedTitle":[{"@language":"en","@value":"New Apparatus for Liquid-Liquid Extraction, \"Emulsion Flow\" Extractor"}]},{"@id":"https://cir.nii.ac.jp/crid/1390282679237654272","@type":"Article","resourceType":"学術雑誌論文(journal article)","relationType":["references"],"jpcoar:relatedTitle":[{"@language":"en","@value":"Counter Current \"Emulsion Flow\" Extractor for Continuous Liquid-Liquid Extraction from Suspended Solutions"}]},{"@id":"https://cir.nii.ac.jp/crid/1390282679638355840","@type":"Article","resourceType":"学術雑誌論文(journal article)","relationType":["references"],"jpcoar:relatedTitle":[{"@language":"ja","@value":"新しい液液抽出法\"エマルションフロー法\""},{"@language":"en","@value":"New Liquid-liquid Extraction Apparatus, \"Emulsion-flow\" Extractor"},{"@language":"ja-Kana","@value":"アタラシイエキエキ チュウシュツホウ\"エマルションフローホウ\""}]},{"@id":"https://cir.nii.ac.jp/crid/1390282680717860224","@type":"Article","relationType":["references"],"jpcoar:relatedTitle":[{"@language":"en","@value":"Continuous Liquid-Liquid Extraction of Nickel from Simulated Electroless Nickel Plating Liquid Wastes by Using a Counter Current Emulsion Flow Extractor"},{"@value":"Continuous Liquid-Liquid Extraction of Nickel from Simulated Electroless Nickel Plating Liquid Wastes by a Using Counter Current Emulsion flow Extractor"}]},{"@id":"https://cir.nii.ac.jp/crid/1390282752324873088","@type":"Article","resourceType":"学術雑誌論文(journal article)","relationType":["references"],"jpcoar:relatedTitle":[{"@language":"en","@value":"Size Distribution of Droplets in a Two Liquid-phase Mixture Compared between Liquid Spraying and Mechanical Stirring"}]},{"@id":"https://cir.nii.ac.jp/crid/1390568456335357824","@type":"Article","relationType":["references"],"jpcoar:relatedTitle":[{"@language":"en","@value":"Quantification of Iodine Mass Transfer and Height of Emulsion Phase in “Emulsion-flow” Column"}]},{"@id":"https://cir.nii.ac.jp/crid/1390584708066720512","@type":"Article","relationType":["isReferencedBy"],"jpcoar:relatedTitle":[{"@language":"en","@value":"Application of Queueing Theory and Foam Drainage Model to Enhance Understanding of Droplet Layer in Emulsion-flow Column Extractor"}]}],"dataSourceIdentifier":[{"@type":"JALC","@value":"oai:japanlinkcenter.org:2010638453"},{"@type":"NDL_SEARCH","@value":"oai:ndlsearch.ndl.go.jp:R000000004-I032987698"},{"@type":"CROSSREF","@value":"10.15261/serdj.30.159"},{"@type":"OPENAIRE","@value":"doi_________::9c008eba86057c906e7607d37c2e4a8c"},{"@type":"CROSSREF","@value":"10.15261/serdj.32.9_references_DOI_XgLSO74tSopYKtht7jz4I4NY1pP"}]}