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Heat Transfer During Boiling of Pure Substances in Free Convection

  • Chapter
Heat Transfer in Condensation and Boiling

Part of the book series: International Series in Heat and Mass Transfer ((HEAT))

Abstract

We shall next deal with boiling in free convection. The dimensions of the container in which the vapor is formed should be large in comparison to the vapor bubbles. A flow should result only by means of the buoyancy of the produced bubbles and by the differences in density. This is referred to simply as pool boiling. The two phase flow in a narrow evaporator tube, even if it is caused in a vertical tube only by the buoyancy of the vapor, will not be investigated. As already explained at the beginning of Chap. 9, there is evaporation in the region of small superheating of the heating wall. Heat is transferred only by free convection, curve a in Fig. 9.3. Nucleate boiling sets in only at a definite superheating of the wall. We will consider here the common case of a liquid at saturation temperature.

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  1. Institut für Technische Thermodynamik und Thermische Verfahrenstechnik, Universität Stuttgart, Pfaffenwaldring 9, W-7000, Stuttgart 80, Germany

    Professor Dr. Karl Stephan

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  1. Professor Dr. Karl Stephan
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© 1992 Springer-Verlag Berlin Heidelberg

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Stephan, K. (1992). Heat Transfer During Boiling of Pure Substances in Free Convection. In: Heat Transfer in Condensation and Boiling. International Series in Heat and Mass Transfer. Springer, Berlin, Heidelberg. https://doi.org/10.1007/978-3-642-52457-8_11

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  • DOI: https://doi.org/10.1007/978-3-642-52457-8_11

  • Publisher Name: Springer, Berlin, Heidelberg

  • Print ISBN: 978-3-642-52459-2

  • Online ISBN: 978-3-642-52457-8

  • eBook Packages: Springer Book Archive

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