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Subcooled boiling heat transfer to R 12 in an annular vertical channel
Author(s) -
Bräuer Holger,
Mayinger Franz
Publication year - 1988
Publication title -
chemical engineering and technology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.403
H-Index - 81
eISSN - 1521-4125
pISSN - 0930-7516
DOI - 10.1002/ceat.270110142
Subject(s) - subcooling , boiling , thermodynamics , nucleate boiling , heat transfer , chemistry , reynolds number , mechanics , materials science , heat flux , turbulence , physics
Abstract Detailed knowledge of the physical phenomena involved in subcooled boiling is of great importance for the design of liquid‐cooled heat generating systems with high heat fluxes. Experimental heat transfer data were obtained for forced convective boiling of dichloro‐difluoroethane (R 12). The flow is circulated upwards through a concentric annular vertical channel. The inner and outer diameters of the annulus are 0.016 m and 0.03 m respectively. The reduced pressures studied were 0.24 ≤ p/p crit ≤ 0.8, inlet subcooling varied from 10 to 75 K and mass fluxes from 500 to 3000 kg/m 2 s, which corresponds to Re numbers from 30000 to 3. The experiments, described in this study, demonstrate that liquid fluorocarbons show certain unusual boiling characteristics in the subcooled flow, such as hysteresis of the boiling curve. These characteristics are attributed to the properties of the fluid, mainly the Pr number and the very low surface tension. The pronounced boiling curve hysteresis can be explained by the fact that large nucleation sites may have been flooded prior to incipient boiling. A dimensionless regression formula is presented which predicts the onset of subcooled boiling as a function of reduced pressure ( p/p crit ), Boiling‐(Bo), Reynolds‐(Re), and a modified Jacob number (Ja), over the whole range of parameters studied, with a good accuracy, including water data from literature.