Mass transfer in a short wetted-wall column. 2. Binary systems

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dc.contributor.authorNieuwoudt I.
dc.contributor.authorCrause J.C.
dc.date.accessioned2011-05-15T16:01:48Z
dc.date.available2011-05-15T16:01:48Z
dc.date.issued1999
dc.description.abstractMass-transfer coefficients were measured in a short wetted-wall column by evaporating binary liquid mixtures. These mass-transfer coefficients were compared with the gas-phase transfer coefficients reported in part 1 of this series. For the systems used in this study, enhanced mass transfer was observed when mixtures having large differences in pure component surface tensions were evaporated. For these systems, an increase in surface rippling was observed. This mass-transfer enhancement was not exhibited in binary systems with small differences in pure component surface tensions.
dc.description.versionArticle
dc.identifier.citationIndustrial and Engineering Chemistry Research
dc.identifier.citation38
dc.identifier.citation12
dc.identifier.issn8885885
dc.identifier.urihttp://hdl.handle.net/10019.1/12162
dc.subjectacetone
dc.subjectaniline
dc.subjectethylene glycol
dc.subjectmethanol
dc.subjectoctanol
dc.subjectwater
dc.subjectarticle
dc.subjectevaporation
dc.subjectliquid
dc.subjectsurface tension
dc.titleMass transfer in a short wetted-wall column. 2. Binary systems
dc.typeArticle
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