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http://hdl.handle.net/11375/18630
Title: | Mass Transfer with Chemical Reaction From Single Spheres |
Authors: | Houghton, William |
Advisor: | Johnson, A.I. Hamielec, A.E. |
Department: | Chemical Engineering |
Keywords: | mass transfer;chemical reaction;forced convection;velocity profiles |
Publication Date: | Oct-1966 |
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> |
URI: | http://hdl.handle.net/11375/18630 |
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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