dc.contributor.author | Wichterle, Kamil | |
dc.contributor.author | Wichterlová, Jana | |
dc.contributor.author | Kulhánková, Lenka | |
dc.date.accessioned | 2006-10-02T13:39:25Z | |
dc.date.available | 2006-10-02T13:39:25Z | |
dc.date.issued | 2005 | |
dc.identifier.citation | Chemical Engineering Communications. 2005, vol. 192, no. 5, p. 550-556. | en |
dc.identifier.issn | 0098-6445 | |
dc.identifier.issn | 1563-5201 | |
dc.identifier.uri | http://hdl.handle.net/10084/56734 | |
dc.description.abstract | The breakup rate of bubbles was studied by observing them rising in water and in glycerol solutions with µ = 1–32 mPas. A levitating technique was applied with bubbles seized in the downstream liquid flow of a diverging channel. Bubbles with volumes VB = 0.2–0.8 cm3 are generally spheroid but their shape pulsates. As they wobble they have a tendency to split. The exponential decay of the number of unbroken bubbles was found, which has been characterized quantitatively by a half-life, t1/2. The rate of breakup increased significantly with the original size of the bubble. By regression of experimental data, the proportionality t1/2 ~ VB-4 has been determined. There is a significant effect of surface tension, while the effect of viscosity on the process appeared to be negligible in the bubble Reynolds number range of 60–3000 that was investigated. | en |
dc.language.iso | en | en |
dc.publisher | Taylor & Francis | en |
dc.relation.ispartofseries | Chemical Engineering Communications | en |
dc.relation.uri | http://dx.doi.org/10.1080/00986440590495034 | en |
dc.subject | aeration | en |
dc.subject | bubble | en |
dc.subject | dispersion | en |
dc.subject | multiphase flow | en |
dc.subject | particle | en |
dc.subject | stability | en |
dc.title | Breakup of bubbles rising in liquids of low and moderate viscosity | en |
dc.type | article | en |
dc.identifier.location | Není ve fondu ÚK | en |
dc.identifier.doi | 10.1080/00986440590495034 | |
dc.identifier.wos | 000230022000001 | |