Multiphase Science and Technology A Quarterly

ISSN for PRINT: 0276-1459

For Online Access

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1987, Volume3

Issue 1-4

508 pages

Issue price - $560.00

Dieter Steiner
Institut fur Thermische Verfahrenstechnik, Universitat Karlsruhe (T. H.), Germany

Perimeter-averaged heat transfer coefficients are investigated during flows of R12 in horizontal tube. The experimental data show that heat transfer is affected by the parameters in a different manner depending on the boiling region. The convective boiling region is mainly determined by mass velocity and flow quality, whereas the nucleate boiling is dominantly affected by heat flux. In particular in the developed nucleate region, the heat transfer coefficient is shown to have no dependence on the flow quality.

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