Breakup and coalescence in turbulent two-phase flows

Many engineering processes involve a gas and a liquid or two immiscible liquids in turbulent flow. The turbulent flows present in two-phase systems will cause the bubbles or drops of a dispersion to undergo breakup and coalescence, and the resulting changes in the dispersion may significantly affect...

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Main Author: Hunt, William E.
Other Authors: Mechanical Engineering
Format: Others
Language:en
Published: Virginia Tech 2014
Subjects:
Online Access:http://hdl.handle.net/10919/40633
http://scholar.lib.vt.edu/theses/available/etd-01172009-063113/
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spelling ndltd-VTETD-oai-vtechworks.lib.vt.edu-10919-406332021-05-26T05:48:40Z Breakup and coalescence in turbulent two-phase flows Hunt, William E. Mechanical Engineering Kornhauser, Alan A. Vandsburger, Uri Davis, Richey M. turbulent flow LD5655.V855 1995.H8345 Many engineering processes involve a gas and a liquid or two immiscible liquids in turbulent flow. The turbulent flows present in two-phase systems will cause the bubbles or drops of a dispersion to undergo breakup and coalescence, and the resulting changes in the dispersion may significantly affect the engineering process under consideration. For this reason, many researchers have studied breakup and coalescence in turbulent two phase flows. Models that can be used to simulate changes in a dispersion over time have been proposed, but these models contain constants that change with experimental conditions and empirical equations that can only be considered valid for certain experimental setups. The goal of this study was to develop general models that could be used to predict changes in bubble or drop size distributions over time for turbulent flows in agitated vessels and pipes. <p>Computer programs were written to reproduce the results of three agitated vessel studies. These programs used existing population balance models to approximate the changes in a dispersion over time measured in previous experiments. A new model for breakup in agitated vessels was then developed and verified with existing experimental data. A new model for coalescence in agitated vessels was also developed and verified with existing experimental data. Both of these models are based on theory and are more readily extendible than previous breakup and coalescence models. The work for agitated vessels was then extended to turbulent two-phase pipe flow. Since there was only a limited amount of experimental data available for breakup and coalescence in pipes, the model for turbulent pipe flow could not be verified. Master of Science 2014-03-14T21:27:15Z 2014-03-14T21:27:15Z 1995-07-05 2009-01-17 2009-01-17 2009-01-17 Thesis Text etd-01172009-063113 http://hdl.handle.net/10919/40633 http://scholar.lib.vt.edu/theses/available/etd-01172009-063113/ en OCLC# 34381287 LD5655.V855_1995.H8345.pdf In Copyright http://rightsstatements.org/vocab/InC/1.0/ xviii, 212 leaves BTD application/pdf application/pdf Virginia Tech
collection NDLTD
language en
format Others
sources NDLTD
topic turbulent flow
LD5655.V855 1995.H8345
spellingShingle turbulent flow
LD5655.V855 1995.H8345
Hunt, William E.
Breakup and coalescence in turbulent two-phase flows
description Many engineering processes involve a gas and a liquid or two immiscible liquids in turbulent flow. The turbulent flows present in two-phase systems will cause the bubbles or drops of a dispersion to undergo breakup and coalescence, and the resulting changes in the dispersion may significantly affect the engineering process under consideration. For this reason, many researchers have studied breakup and coalescence in turbulent two phase flows. Models that can be used to simulate changes in a dispersion over time have been proposed, but these models contain constants that change with experimental conditions and empirical equations that can only be considered valid for certain experimental setups. The goal of this study was to develop general models that could be used to predict changes in bubble or drop size distributions over time for turbulent flows in agitated vessels and pipes. <p>Computer programs were written to reproduce the results of three agitated vessel studies. These programs used existing population balance models to approximate the changes in a dispersion over time measured in previous experiments. A new model for breakup in agitated vessels was then developed and verified with existing experimental data. A new model for coalescence in agitated vessels was also developed and verified with existing experimental data. Both of these models are based on theory and are more readily extendible than previous breakup and coalescence models. The work for agitated vessels was then extended to turbulent two-phase pipe flow. Since there was only a limited amount of experimental data available for breakup and coalescence in pipes, the model for turbulent pipe flow could not be verified. === Master of Science
author2 Mechanical Engineering
author_facet Mechanical Engineering
Hunt, William E.
author Hunt, William E.
author_sort Hunt, William E.
title Breakup and coalescence in turbulent two-phase flows
title_short Breakup and coalescence in turbulent two-phase flows
title_full Breakup and coalescence in turbulent two-phase flows
title_fullStr Breakup and coalescence in turbulent two-phase flows
title_full_unstemmed Breakup and coalescence in turbulent two-phase flows
title_sort breakup and coalescence in turbulent two-phase flows
publisher Virginia Tech
publishDate 2014
url http://hdl.handle.net/10919/40633
http://scholar.lib.vt.edu/theses/available/etd-01172009-063113/
work_keys_str_mv AT huntwilliame breakupandcoalescenceinturbulenttwophaseflows
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