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Please use this identifier to cite or link to this item: http://hdl.handle.net/11375/18864
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dc.contributor.advisorBaird, M. H. I.-
dc.contributor.authorLane, Stephen-
dc.date.accessioned2016-02-11T16:10:01Z-
dc.date.available2016-02-11T16:10:01Z-
dc.date.issued1971-09-
dc.identifier.urihttp://hdl.handle.net/11375/18864-
dc.description.abstract<p> Drop sizes were measured photographically for water in kerosene and for water in methyl isobutyl ketone, at varying flow rates and levels of agitation. At high levels of agitation the data could be represented very approximately by the well known relationship of Hinze and others: d32= CONS(σ0.6)/ρ0.6E0.44) (where d32=mean drop diameter, σ= interfacial tension, p̂= mean density and E= power input per unit mass). However this equation was not satisfactory at low levels of agitation, and an alternative equation based on dimensional analysis and including effects of density difference and gravity has been proposed. Qualitative observations regarding drop formation, holdup and various operating phenomena are made. </p>en_US
dc.language.isoenen_US
dc.subjectdrop sizesen_US
dc.subjectreciprocated plate extractionen_US
dc.subjectflow rateen_US
dc.subjectagitation levelen_US
dc.titleDrop Sizes in a Reciprocated Plate Extraction Columnen_US
dc.contributor.departmentChemical Engineeringen_US
dc.description.degreetypeThesisen_US
dc.description.degreeMaster of Engineering (MEngr)en_US
Appears in Collections:Open Access Dissertations and Theses

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