作者: V.G. Rifert , V.I. Podberezny , Ju.V. Putilin , Ju.G. Nikitin , P.A. Barabash
DOI: 10.1016/0011-9164(89)85063-5
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摘要: Abstract Local and average heat-transfer coefficients in water film evaporation on horizontal profile tubes were measured. Dependences for calculating the heat transfer are presented. The studies conducted demonstrated that use of longitudinally-profile makes it possible to increase, with an account development heat-exchange surface, from wall flowing-down liquid by a factor 1.35–1.85, overall “vaporliquid” transfer, 1.3–1.5. This allows such be recommended desalination plant evaporators.