Abstract
A suitable universal model for boiling heat transfer has been pursued for a very long time. The present work is a significant step towards such a model by dealing with the inherent bubble dynamics. As in previous works the bubble growth and departure are shown to be coupled and are dealt with simultaneously. For departure, the force balance is relatively straightforward, depending on a suitable drag coefficient. However, for growth the thermal aspects and boiling dynamics are rather more complicated. The present study not only draws from a 1D energy balance, but explains the need for correction of the effective superheat, based on kinetic theory and consideration of the vapor Knudsen layer conditions (following Ytrehus and Ostmo, 1996). Thereby, the present study merges a traditional macro approach with a micro, near-interface viewpoint, thereby identifying L /ℜT as the most significant parameter, besides the superheat (Jakob number). This approach provides a new explanation for the additional pressure dependence found in bubble departure, and the transition in trend at high pressure. The present study also extends the range typically considered, to include 19 liquids/liquefied gases, up to near critical pressures, sub-millimeter to several centimeter bubbles and gravity levels down to 1/16th that of earth, providing good prediction over the entire range. This range is limited at the one end by the dominance of micro-layer evaporation and substrate conduction at lower superheats, and at the other by bubble interaction - thermal robbing and bubble coalescence.
Original language | English |
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Pages (from-to) | 15-31 |
Number of pages | 17 |
Journal | International Journal of Multiphase Flow |
Volume | 105 |
DOIs | |
State | Published - Aug 2018 |
Keywords
- Bubble departure
- Bubble growth
- Evaporation interface
- Kinetic theory
- Knudsen layer
- Nucleate boiling
All Science Journal Classification (ASJC) codes
- Mechanical Engineering
- Fluid Flow and Transfer Processes
- General Physics and Astronomy