1990
DOI: 10.1016/0142-727x(90)90010-9
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Pool film boiling from spheres to saturated and subcooled liquids of Freon-12 and Freon-22

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Cited by 15 publications
(4 citation statements)
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“…E.A.6 in the Electronic Annex). We calculated the vapor film thickness around the sphere during film boiling using the analytical model of Tso et al (1990), and found that the film thickness at the bottom of the sphere is quite comparable with the length scale of the nanoparticle deposits. Therefore, the thin vapor film could be disturbed by such deposits.…”
Section: Data Interpretationmentioning
confidence: 98%
“…E.A.6 in the Electronic Annex). We calculated the vapor film thickness around the sphere during film boiling using the analytical model of Tso et al (1990), and found that the film thickness at the bottom of the sphere is quite comparable with the length scale of the nanoparticle deposits. Therefore, the thin vapor film could be disturbed by such deposits.…”
Section: Data Interpretationmentioning
confidence: 98%
“…As a result, they are provided with a levitation force by the generated vapor layer. This solid-liquid film boiling (or liquid-liquid film boiling) is usually caused by a huge temperature distinction between adjacent substances (3)(4)(5)(6)(7). Film boiling, also referred to as the Leidenfrost effect, generally impedes the heat transfer between neighboring materials due to the big thermal resistance induced by evaporated vapor layer (8,9).…”
mentioning
confidence: 99%
“…The authors tentatively propose this method for film boiling around a vertical finite-length cylinder with a convex hemispherical bottom as the effect of diameter and length of the test cylinder are not included in the correction. Incidentally, Tso et al [4] have reported that it is necessary to multiply the analytical solution by a Fig. 10.…”
Section: Comparison Of Predicted With Experimental Resultsmentioning
confidence: 98%
“…where both h A1 is given by Tso et al [4] for the saturated and subcooled film boiling from a sphere where the two-phase boundary layer theory is adopted and the average heat transfer coefficient on the side surface h _ A2 is given by Nishikawa et al [5] based on the two-phase boundary layer theory. The heat transfer coefficient for the wavy vapor-liquid interface on the part of the upper end h _ B is estimated by referring to a vapor-film-unit model proposed by Nishio and Ohtake [3] and h _ C by the Hamill-Baumeister correlation [6] using the method proposed by the authors [2].…”
Section: Estimation Of Wall Heat Fluxmentioning
confidence: 99%