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dc.contributor.authorYoder, Graydon L.en_US
dc.contributor.authorRohsenow, Warren M.en_US
dc.contributor.otherMassachusetts Institute of Technology. Division of Sponsored Research.en_US
dc.contributor.otherMassachusetts Institute of Technology. Dept. of Mechanical Engineering.en_US
dc.contributor.otherMassachusetts Institute of Technology. Heat Transfer Laboratory.en_US
dc.date.accessioned2011-03-04T23:39:25Z
dc.date.available2011-03-04T23:39:25Z
dc.date.issued1980en_US
dc.identifier10849100en_US
dc.description.abstractDispersed flow consists of small liquid droplets entrained in a flowing vapor. This flow regime can occur in cryogenic equipment, in steam generators, and during nuclear reactor loss of coolant accidents. A theoretical analysis of dispersed flow film boiling has been performed using mass, momentum and energy conservation equations for both phases. A numerical solution scheme, including wall-to-drop, vapor to drop, and wall-to-vapor heat transfer mechanisms was used to predict wall temperatures for constant heat flux, vertical upflow conditions. Wall temperature predictions were compared to liquid nitrogen, Freon-12 and water data of four separate investigators with reasonable results. A local conditions solution was developed by simplifying the governing equations, using conclusions from the numerical model. A non-dimensional group was found which solely determined the non-equilibrium with the flow, and allowed hand calculation of wall temperatures. The local conditions solution was compared to data taken by five investigators with good results.en_US
dc.description.sponsorshipSponsored by National Science Foundation DSR Projecten_US
dc.format.extent211 pen_US
dc.publisherCambridge, Mass. : Heat Transfer Laboratory, Dept. of Mechanical Engineering, Massachusetts Institute of Technology, [1980]en_US
dc.relation.ispartofseriesTechnical report (Massachusetts Institute of Technology, Heat Transfer Laboratory) ; no. 103.en_US
dc.titleDispersed flow film boilingen_US
dc.typeTechnical Reporten_US


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