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dc.contributor.authorBae, Soonhoonen_US
dc.contributor.authorMaulbetsch, John S.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.accessioned2011-03-04T23:33:41Z
dc.date.available2011-03-04T23:33:41Z
dc.date.issued1970en_US
dc.identifier14083454en_US
dc.identifier.urihttp://hdl.handle.net/1721.1/61472
dc.description.abstractHigh vapor velocity condensation inside a tube was studied theoretically. The heat transfer coefficients were calculated by the momentum and heat transfer analogy. The Von Karman universal velocity distribution was applied to the condensate flow. Pressure drop was calculated by the Lockhart-Martinelli method and the Zivi void fraction equation. Experimental data was obtained for the mass velocities from 150,000 to 555,000 lbm/ft2 hr for R-12 and R-22 condensing in a 0.493" I.D. 18 ft. long test section. The measured heat transfer coefficients agreed with the prediction within 10% except a few points in the very low quality region.en_US
dc.description.sponsorshipSponsored by Technical Committee 1.3, American Society of Heating, Refrigerating and Air Conditioning Engineers DSR Projecten_US
dc.format.extent41, [14] pen_US
dc.publisherCambridge, Mass. : M.I.T. Heat Transfer Laboratory, [1970]en_US
dc.relation.ispartofseriesTechnical report (Massachusetts Institute of Technology, Heat Transfer Laboratory) ; no. 71.en_US
dc.subjectTubes -- Fluid dynamics.en_US
dc.subjectHeat -- Transmission.en_US
dc.subjectCondensation.en_US
dc.subjectRefrigerants.en_US
dc.titleRefrigerant forced-convection condensation inside horizontal tubesen_US
dc.typeTechnical Reporten_US


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