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dc.contributor.authorRadovcich, Nick A.en_US
dc.contributor.authorMoissis, Raphael.en_US
dc.contributor.otherMassachusetts Institute of Technology. Division of Sponsored Research.en_US
dc.contributor.otherMassachusetts Institute of Technology. Heat Transfer Laboratory.en_US
dc.date.accessioned2011-03-04T23:30:41Z
dc.date.available2011-03-04T23:30:41Z
dc.date.issued1962en_US
dc.identifier14089526en_US
dc.identifier.urihttp://hdl.handle.net/1721.1/61460
dc.description.abstractThe 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.en_US
dc.description.sponsorshipOffice of the Naval Research DSRen_US
dc.format.extent[82] leaves in various pagings (some unnumbered)en_US
dc.publisherCambridge, Mass. : M.I.T. Division of Sponsored Research, [1962]en_US
dc.relation.ispartofseriesTechnical report (Massachusetts Institute of Technology, Heat Transfer Laboratory) ; no. 22.en_US
dc.subjectPipe -- Fluid dynamics.en_US
dc.subjectBubbles.en_US
dc.titleThe transition from two phase bubble flow to slug flowen_US
dc.typeTechnical Reporten_US


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