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http://hdl.handle.net/11375/18630
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DC Field | Value | Language |
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dc.contributor.advisor | Johnson, A.I. | - |
dc.contributor.advisor | Hamielec, A.E. | - |
dc.contributor.author | Houghton, William | - |
dc.date.accessioned | 2015-12-04T16:49:26Z | - |
dc.date.available | 2015-12-04T16:49:26Z | - |
dc.date.issued | 1966-10 | - |
dc.identifier.uri | http://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.iso | en | en_US |
dc.subject | mass transfer | en_US |
dc.subject | chemical reaction | en_US |
dc.subject | forced convection | en_US |
dc.subject | velocity profiles | en_US |
dc.title | Mass Transfer with Chemical Reaction From Single Spheres | en_US |
dc.contributor.department | Chemical Engineering | en_US |
dc.description.degreetype | Thesis | en_US |
dc.description.degree | Doctor of Philosophy (PhD) | en_US |
Appears in Collections: | Open Access Dissertations and Theses |
Files in This Item:
File | Description | Size | Format | |
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Houghton_William_T_1966_Phd.pdf | 6.24 MB | Adobe PDF | View/Open |
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