2007
DOI: 10.1016/j.ijthermalsci.2006.07.001
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Two-phase modelling of laminar film condensation from vapour–gas mixtures in declining parallel-plate channels

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Cited by 36 publications
(18 citation statements)
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“…͑5a͒-͑5e͒ with ⌼ 1 = ⌼ 2 = ⌼ 3 = ⌼ 4 = ⌼ 5 = 0 and boundary conditions ͑8a͒-͑8d͒ with b 7 = b 9 = 0 the Navier-Stokes system. 52,[56][57][58][59] An example of the difference between the full fluiddynamic-type system and the Navier-Stokes system is demonstrated in Fig. 8.…”
Section: B Numerical Resultsmentioning
confidence: 99%
“…͑5a͒-͑5e͒ with ⌼ 1 = ⌼ 2 = ⌼ 3 = ⌼ 4 = ⌼ 5 = 0 and boundary conditions ͑8a͒-͑8d͒ with b 7 = b 9 = 0 the Navier-Stokes system. 52,[56][57][58][59] An example of the difference between the full fluiddynamic-type system and the Navier-Stokes system is demonstrated in Fig. 8.…”
Section: B Numerical Resultsmentioning
confidence: 99%
“…As indicated by Eqs. (20) and (21), a decrease in T W results in decreased ability of the gas to absorb moisture and causes the vapor to release increased amounts of condensate film, as determined by Siow et al [21,22]. These trends indicate that increased heat transfer is associated with decreased T W .…”
Section: Influence Of Inlet Conditions On Local Film Thickness and Lomentioning
confidence: 88%
“…Siow et al [140] compared the use of the two-phase flow model of steam/air and R134a/air for film condensation heat transfer in horizontal channels. They found that R134a/air condensation heat transfer liquid film was thicker, the heat transfer rate was lower, and the pressure drop was smaller.…”
Section: Diffusion Layer Modelmentioning
confidence: 99%