The transition from two phase bubble flow to slug flow
The process of transition from bubble to slug flow in a vertical pipe has been studied analytically and experimentally. An equation is presented which gives the agglomeration time as a function of void fraction, channel diameter, initial bubble diameter and liquid purity. A dependent function which...
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Format: | Technical Report |
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Cambridge, Mass. : M.I.T. Division of Sponsored Research, [1962]
2011
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Online Access: | http://hdl.handle.net/1721.1/61460 |
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author | Radovcich, Nick A. Moissis, Raphael. |
author2 | Massachusetts Institute of Technology. Division of Sponsored Research. |
author_facet | Massachusetts Institute of Technology. Division of Sponsored Research. Radovcich, Nick A. Moissis, Raphael. |
author_sort | Radovcich, Nick A. |
collection | MIT |
description | The process of transition from bubble to slug flow in a vertical pipe has been studied analytically and experimentally. An equation is presented which gives the agglomeration time as a function of void fraction, channel diameter, initial bubble diameter and liquid purity. A dependent function which also appears in the equation has been evaluated using experimental data. A reasonably good correlation of the data has been achieved. |
first_indexed | 2024-09-23T10:31:21Z |
format | Technical Report |
id | mit-1721.1/61460 |
institution | Massachusetts Institute of Technology |
last_indexed | 2024-09-23T10:31:21Z |
publishDate | 2011 |
publisher | Cambridge, Mass. : M.I.T. Division of Sponsored Research, [1962] |
record_format | dspace |
spelling | mit-1721.1/614602019-04-10T18:06:07Z The transition from two phase bubble flow to slug flow Radovcich, Nick A. Moissis, Raphael. Massachusetts Institute of Technology. Division of Sponsored Research. Massachusetts Institute of Technology. Heat Transfer Laboratory. Pipe -- Fluid dynamics. Bubbles. The process of transition from bubble to slug flow in a vertical pipe has been studied analytically and experimentally. An equation is presented which gives the agglomeration time as a function of void fraction, channel diameter, initial bubble diameter and liquid purity. A dependent function which also appears in the equation has been evaluated using experimental data. A reasonably good correlation of the data has been achieved. Office of the Naval Research DSR 2011-03-04T23:30:41Z 2011-03-04T23:30:41Z 1962 Technical Report 14089526 http://hdl.handle.net/1721.1/61460 Technical report (Massachusetts Institute of Technology, Heat Transfer Laboratory) ; no. 22. [82] leaves in various pagings (some unnumbered) application/pdf Cambridge, Mass. : M.I.T. Division of Sponsored Research, [1962] |
spellingShingle | Pipe -- Fluid dynamics. Bubbles. Radovcich, Nick A. Moissis, Raphael. The transition from two phase bubble flow to slug flow |
title | The transition from two phase bubble flow to slug flow |
title_full | The transition from two phase bubble flow to slug flow |
title_fullStr | The transition from two phase bubble flow to slug flow |
title_full_unstemmed | The transition from two phase bubble flow to slug flow |
title_short | The transition from two phase bubble flow to slug flow |
title_sort | transition from two phase bubble flow to slug flow |
topic | Pipe -- Fluid dynamics. Bubbles. |
url | http://hdl.handle.net/1721.1/61460 |
work_keys_str_mv | AT radovcichnicka thetransitionfromtwophasebubbleflowtoslugflow AT moissisraphael thetransitionfromtwophasebubbleflowtoslugflow AT radovcichnicka transitionfromtwophasebubbleflowtoslugflow AT moissisraphael transitionfromtwophasebubbleflowtoslugflow |