Chapter: Mechanical : Heat and Mass Transfer : Phase Change Heat Transfer and Heat Exchangers

Boiling Curve - Operating Constraints

The boiling curve, shown in Fig. 11.5, is based on the assumption that the temperature of the heated surface can be maintained at the desired value.

Boiling Curve - Operating Constraints

The boiling curve, shown in Fig. , is based on the assumption that the temperature of the heated surface can be maintained at the desired value. In that case, it would be possible to operate the vapour producing system at the point of maximum flux with nucleate boiling. If the heat flux instead of the surface temperature, is the independent variable and it IS desired to operate the system at the point of maximum flux, it is just possible that a slight increase in the heat flux will increase the surface temperature substantially. And, the equilibrium will be established at point F. If the material of the heating element has its melting point temperature lower than the temperature at the equilibrium point F, the heating element will melt.

Factors Affecting Nucleate Boiling

Since high heat transfer rates and convection coefficients are associated with small values of the excess temperature, it is desirable that many engineering devices operate in the nucleate boiling regime. It is possible to get heat transfer coefficients in excess of 10⁴ W/m² in nucleate boiling regime and these values are substantially larger than those normally obtained in convection processes with no phase change.

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Mechanical : Heat and Mass Transfer : Phase Change Heat Transfer and Heat Exchangers : Boiling Curve - Operating Constraints |