Heat Transfer Engineering · 2007 · 67 citations · 22 references
EngineeringMechanical EngineeringFluid DynamicsHeat TransferTransport PhenomenaBoiling Heat TransferHeat Transfer AnalysisHeat Transfer FundamentalsHeat Transfer In FluidsBoiling Heat Transfer CoefficientDryout PhenomenaHeat Transfer CoefficientsHot Water HeatingLiquid Film BehaviorNucleate BoilingReynolds NumberReynolds Number Effects
A new falling‑film test facility was built to measure local heat‑transfer coefficients on arrays of horizontal tubes with R‑134a, using a hot‑water heating method to evaluate a wide range of film Reynolds numbers across four tube types, multiple pitches, and heat‑flux levels, with additional nucleate pool boiling data collected for comparison. The results show that as film Reynolds number decreases, a sharp transition to partial dryout sharply reduces heat transfer, while above this transition heat‑transfer coefficients remain nearly constant due to vigorous nucleate boiling, yielding about 15,000 data points across varying heat flux, Reynolds number, tube spacing, and tube type.
A new falling film heat transfer test facility has been built for the measurement of local heat transfer coefficients on a vertical array of horizontal tubes, including flow visualization capabilities, for use with refrigerants. Presently, the facility has been used for evaporation tests on four types of tubes at three tube pitches and three nominal heat flux levels for R-134a at 5°C. A new method for determining local heat transfer coefficients using hot water heating has been applied, and test results for a wide range of liquid film Reynolds numbers have been measured for arrays made of plain, Turbo-BII HP, Gewa-B, and High-Flux tubes. The results show that there is a transition to partial dryout as the film Reynolds number is reduced, marked by a sharp falloff in heat transfer. Above this transition, the heat transfer coefficients are nearly insensitive to the film Reynolds number, apparently because vigorous nucleate boiling is always seen in the liquid film. The corresponding nucleate pool boiling data for the four types of tubes were also measured for direct comparison purposes. Overall, about 15,000 local heat transfer data points were obtained in this study as a function of heat flux, film Reynolds number, tube spacing, and type.
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95/03868 Convective boiling and condensation
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