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Please use this identifier to cite or link to this item: http://hdl.handle.net/11375/18630
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DC FieldValueLanguage
dc.contributor.advisorJohnson, A.I.-
dc.contributor.advisorHamielec, A.E.-
dc.contributor.authorHoughton, William-
dc.date.accessioned2015-12-04T16:49:26Z-
dc.date.available2015-12-04T16:49:26Z-
dc.date.issued1966-10-
dc.identifier.urihttp://hdl.handle.net/11375/18630-
dc.description.abstract<p> Forced convection mass transfer rates from single gas bubbles, with accompanying chemical reaction, were determined experimentally in the intermediate Reynolds number range. The reacting system carbon dioxide-monoethanolaminc was chosen for this study. </p> <p> A mathematical model, describing forced convection mass transfer from a single sphere with accompanying first or second order reaction, was developed and solved using finite-difference techniques. Hydrodynamic conditions in the intermediate Reynolds number region were described using Kawaguti-type velocity profiles. </p> <p> The numerical solutions of the model have been compared with the experimental results of this study as well as with previous theoretical and experimental results. </p>en_US
dc.language.isoenen_US
dc.subjectmass transferen_US
dc.subjectchemical reactionen_US
dc.subjectforced convectionen_US
dc.subjectvelocity profilesen_US
dc.titleMass Transfer with Chemical Reaction From Single Spheresen_US
dc.contributor.departmentChemical Engineeringen_US
dc.description.degreetypeThesisen_US
dc.description.degreeDoctor of Philosophy (PhD)en_US
Appears in Collections:Open Access Dissertations and Theses

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