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Variations in Mass Transfer with Dispersed Bubbles

dc.contributor.advisorMurphy, K. L.
dc.contributor.authorWilson, Arthur Warren
dc.contributor.departmentCivil Engineeringen_US
dc.date.accessioned2016-11-23T18:02:30Z
dc.date.available2016-11-23T18:02:30Z
dc.date.issued1967-10
dc.description.abstract<p> Using a single bubble suspended in a liquid flow regime, the effects of velocity, bubble size, and surfactant levels on the gas transfer process across the bubble interface were investigated. Mass transfer data reported in the literature for non-circulating carbon dioxide bubbles was verified. A mathematical model predicting the mass transfer process for the single bubble system used in this study was formulated and this model provided a reasonable fit for experimental data obtained for the dissolution of a carbon dioxide bubble into an aqueous solution of a second sparingly soluble gas. The fate of a hypothetical air bubble in an aerator was briefly considered.</p>en_US
dc.description.degreeMaster of Engineering (MEngr)en_US
dc.description.degreetypeThesisen_US
dc.identifier.urihttp://hdl.handle.net/11375/20831
dc.language.isoen_USen_US
dc.subjectmass transfer, dispersed bubbles, liquid flow regime, velocity, gas transfer, surfactant levelsen_US
dc.titleVariations in Mass Transfer with Dispersed Bubblesen_US
dc.typeThesisen_US

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