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dc.contributor.authorKandlikar, Satish
dc.date.accessioned2008-12-01T19:45:55Z
dc.date.available2008-12-01T19:45:55Z
dc.date.issued1990-11
dc.identifier.urihttp://hdl.handle.net/1850/7569
dc.descriptionProceedings of the winter annual ASME meeting, November 1990. Please see www.asme.org for the complete proceedings.en_US
dc.descriptionRIT community members may access full-text via RIT Libraries licensed databases: http://library.rit.edu/databases/
dc.description.abstractA mechanistic model is presented for heat transfer in the wet wall region of saturated flow boiling inside circular tubes. Saturated flow boiling is postulated to be essentially -similar to partial subcooled boiling with the two modes of heat transfer, nucleate boiling and convective boiling, assumed to be additive. The contribution from each mechanism is examined on the basis of the available literature on heat transfer in thin films and on flow boiling inside circular tubes. The effects of film thickness and interfacial shear stress on the nucleate boiling component are analyzed. A comprehensive flow boiling plot is presented on q vs. AT coordinates to illustrate the influence of quality on flow boiling heat transfer.en_US
dc.language.isoen_USen_US
dc.publisherAmerican Society of Mechanical Engineers (ASME)en_US
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dc.titleA Mechanistic model for flow boiling heat transferen_US
dc.typeProceedingsen_US


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