par Gatapova, Elizaveta 
;Kabov, Oleg
Référence International Journal of Heat and Mass Transfer, 51, 19-20, page (4797-4810)
Publication Publié, 2008
;Kabov, Oleg Référence International Journal of Heat and Mass Transfer, 51, 19-20, page (4797-4810)
Publication Publié, 2008
Article révisé par les pairs
| Résumé : | This paper considers the flow of a liquid film sheared by gas flow in a channel with a heater placed at the bottom wall. A one-sided 2D model is considered for weakly heated films. The heat and mass transfer problem is also investigated in the framework of a two-sided model. The exact solution to the problem of heat transfer is obtained for a linear velocity profile. The double effect of Marangoni forces is demonstrated by the formation of a liquid bump in the vicinity of the heater's upper edge and film thinning in the vicinity of the lower edge. The criterion determining the occurrence of "ripples" on the film surface upstream from the bump is found. Numerical analysis reveals that evaporation dramatically changes the temperature distribution, and hence, thermocapillary forces on the gas-liquid interface. All transport phenomena (convection to liquid and gas, evaporation) are found to be important for relatively thin films, and the thermal entry length is a determining factor for heaters of finite length. The thermal entry length depends on film thickness, which can be regulated by gas flow rate or channel height. The influence of the convective heat transfer mechanism is much more prominent for relatively high values of the liquid Reynolds number. The liquid-gas interface Biot number is shown to be a sectional-hyperbolic function of a longitudinal axis variable. Some qualitative and quantitative comparisons with experimental results are presented. © 2008 Elsevier Ltd. All rights reserved. |
