{"@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/1363388844347224960.json","@type":"Article","productIdentifier":[{"identifier":{"@type":"DOI","@value":"10.1002/aic.690330907"}},{"identifier":{"@type":"URI","@value":"https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1002%2Faic.690330907"}},{"identifier":{"@type":"URI","@value":"https://aiche.onlinelibrary.wiley.com/doi/pdf/10.1002/aic.690330907"}}],"dc:title":[{"@value":"Organic liquids in a bubble column: Holdups and mass transfer coefficients"}],"description":[{"type":"abstract","notation":[{"@value":"<jats:title>Abstract</jats:title><jats:p>Gas holdups and volumetric mass transfer coefficients <jats:italic>k<jats:sub>L</jats:sub>a</jats:italic> are studied in a bubble column of 0.095 m dia. with 50 different gas‐liquid systems comprising pure and mixed organic liquids and various gases. The gas holdups measured in pure organic liquids can be represented by existing correlations but the values in liquid mixtures are high. On the other hand, all mass transfer coefficients can be correlated uniformly by a new dimensionless equation, with 13.3% mean error.</jats:p>"}]}],"creator":[{"@id":"https://cir.nii.ac.jp/crid/1383388844347224962","@type":"Researcher","foaf:name":[{"@value":"S. S. öztürk"}]},{"@id":"https://cir.nii.ac.jp/crid/1383388844347224960","@type":"Researcher","foaf:name":[{"@value":"A. Schumpe"}]},{"@id":"https://cir.nii.ac.jp/crid/1380298344891832320","@type":"Researcher","foaf:name":[{"@value":"W.‐D. Deckwer"}]}],"publication":{"publicationIdentifier":[{"@type":"PISSN","@value":"00011541"},{"@type":"EISSN","@value":"15475905"}],"prism:publicationName":[{"@value":"AIChE Journal"}],"dc:publisher":[{"@value":"Wiley"}],"prism:publicationDate":"1987-09","prism:volume":"33","prism:number":"9","prism:startingPage":"1473","prism:endingPage":"1480"},"reviewed":"false","dc:rights":["http://onlinelibrary.wiley.com/termsAndConditions#vor"],"url":[{"@id":"https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1002%2Faic.690330907"},{"@id":"https://aiche.onlinelibrary.wiley.com/doi/pdf/10.1002/aic.690330907"}],"createdAt":"2004-06-23","modifiedAt":"2025-10-07","relatedProduct":[{"@id":"https://cir.nii.ac.jp/crid/1390282679541414400","@type":"Article","relationType":["isReferencedBy"],"jpcoar:relatedTitle":[{"@language":"en","@value":"Design Parameters of Bubble Column Reactors With and Without Solid Suspensions."}]},{"@id":"https://cir.nii.ac.jp/crid/1390282679541678848","@type":"Article","relationType":["isReferencedBy"],"jpcoar:relatedTitle":[{"@language":"en","@value":"Gas and Liquid Holdups in Multi-Stage Bubble Columns for Gas-Liquid-Liquid-Solid Four-Phase System."},{"@language":"ja-Kana","@value":"Gas and Liquid Holdups in Multi-Stage B"}]},{"@id":"https://cir.nii.ac.jp/crid/1390282679546333952","@type":"Article","relationType":["isReferencedBy"],"jpcoar:relatedTitle":[{"@language":"en","@value":"A New Approach for the Prediction of Gas Holdup in Bubble Columns Operated under Various Pressures in the Homogeneous Regime"}]}],"dataSourceIdentifier":[{"@type":"CROSSREF","@value":"10.1002/aic.690330907"},{"@type":"CROSSREF","@value":"10.1252/jcej.08we005_references_DOI_21uo9ag9PneF1xKU5zFD3KrpRY4"},{"@type":"CROSSREF","@value":"10.1252/jcej.29.745_references_DOI_21uo9ag9PneF1xKU5zFD3KrpRY4"},{"@type":"CROSSREF","@value":"10.1252/jcej.31.813_references_DOI_21uo9ag9PneF1xKU5zFD3KrpRY4"}]}