Abstract
Liquid-solid contact in transition boiling is modelled by involving transient conduction, boiling incipience, macrolayer evaporation and vapour film boiling. The prediction of liquid contact duration and time fraction agrees reasonably well with experimental data, and the model is able to predict both of the boiling curve transitions-the critical and minimum heat fluxes. The study concludes that the liquid turbulence due to buoyancy forces and bubble agitation is an important parameter for transition boiling. It is found that surface coating (oxidation or deposition) tends to improve the transition boiling heat transfer and elevate the wall superheats at both the critical heat flux and the minimum film boiling points, which agree with the experimental observations.
| Original language | English |
|---|---|
| Pages (from-to) | 1337-1349 |
| Journal | International Journal of Heat and Mass Transfer |
| Volume | 32 |
| Issue number | 7 |
| DOIs | |
| Publication status | Published - Jul 1989 |
| Externally published | Yes |
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