Faculty Presentation - Peter.ppt
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This document discusses phase changes in heat transfer, specifically boiling. It begins by defining boiling as a liquid-to-vapor phase change process that occurs at the solid-liquid interface. It then discusses the various regions of the pool boiling curve for water: natural convection, nucleate boiling, transition boiling, and film boiling. Nucleate boiling provides the highest heat transfer rates due to liquid entrainment and evaporation, reaching a maximum at the critical heat flux point. Transition and film boiling have lower heat transfer due to vapor film formation between the heater and liquid. Applications of boiling include nuclear reactors, petroleum transportation, and electronics cooling.
Faculty Presentation - Peter.ppt
- 1. PHASE CHANGES IN HEAT TRANSFER Presented by Mr. J. PETER FERNANDES Assistant Professor Department Mechanical Engineering St. Joseph’s College of Engineering and Technology Phase Changes in Heat Transfer 1 Mr. J.PETER FERNANDES
- 2. 2 Mr. J.PETER FERNANDES Phase Changes in Heat Transfer •Boiling: Boiling is a liquid-to-vapor phase changing process. Boiling occurs at the solid–liquid interface
- 3. Application of Boiling 3 Mr. J.PETER FERNANDES Phase Changes in Heat Transfer • Core and steam generators in nuclear reactors. • Petroleum transportation. • Electronic cooling and various types of chemical reactors.
- 4. Pool boiling curves for water 4 Mr. J.PETER FERNANDES Phase Changes in Heat Transfer
- 5. Natural Convection ( Point A on the Boiling Curve) • Bubbles do not form on the heating surface until the liquid is heated a few degrees above the saturation temperature (about 2 to 6°C for water) the liquid is slightly superheated in this case (meta stable state). • The fluid motion in this mode of boiling is governed by natural convection currents. • Heat transfer from the heating surface to the fluid is by natural convection. Mr. J.PETER FERNANDES Phase Changes in Heat Transfer 5
- 6. Nucleate Boiling • The bubbles form at an increasing rate at an increasing number of nucleation sites as we move along the boiling curve toward point C • Region A–B ─isolated bubbles. • Region B–C ─ numerous continuous columns of vapor in the liquid. Mr. J.PETER FERNANDES Phase Changes in Heat Transfer 6
- 7. Nucleate Boiling • In region A–B the stirring and agitation caused by the entrainment of the liquid to the heater surface is primarily responsible for the increased heat transfer coefficient. • In region A–B the large heat fluxes obtainable in this region are caused by the combined effect of liquid entrainment and evaporation. After point B the heat flux increases at a lower rate with increasing DT excess, and reaches a maximum at point C. • The heat flux at this point is called the critical (or maximum) heat flux, and is of prime engineering importance. Mr. J.PETER FERNANDES Phase Changes in Heat Transfer 7
- 8. Transition Boiling When ΔT excess is increased past point C, the heat flux decreases. This is because a large fraction of the heater surface is covered by a vapor film, which acts as an insulation. In the transition boiling regime, both nucleate and film boiling partially occur. Mr. J.PETER FERNANDES Phase Changes in Heat Transfer 8
- 9. Film Boiling • Beyond Point D the heater surface is completely covered by a continuous stable vapor film. • Point D, where the heat flux reaches a minimum is called the Leiden frost point. The presence of a vapor film between the heater surface and the liquid is responsible for the low heat transfer rates in the film boiling region. The heat transfer rate increases with increasing excess temperature due to radiation to the liquid. Mr. J.PETER FERNANDES Phase Changes in Heat Transfer 9
- 10. Pool boiling curves for water-Animation Mr. J.PETER FERNANDES Phase Changes in Heat Transfer 10
- 11. Thank you Phase Changes in Heat Transfer 11 Mr. J.PETER FERNANDES