Effects of inlet conditions on film evaporation along an inclined plate

Abstract The evaporation of falling water liquid film in air flow is used in different solar energy applications as drying, distillation and desalination, and desiccant systems. The good understanding of the hydrodynamics and heat exchange in falling liquid film and gas flow, with interfacial heat and mass transfer, can be applied in improving solar systems performance. The solar system performance is dependent on the operating conditions, system conception and related to several physical parameters, where the effects of some of these parameters are not completely clarified. In the present numerical study, we examine the effects of inlet conditions on the evaporation processes along the gas–liquid interface. The liquid film streams over an inclined plate subjected to different thermal conditions. Liquid and gas flows are approached by two coupled laminar boundary-layers. The numerical solution is obtained by utilizing an implicit finite-difference box method. In this analysis an air–water system is considered and the coupled effects of inclination, inlet liquid mass flow rate and gas velocity are examined. The results show that, for imposed heat flux or uniform wall temperature, the effect of inclination is highly dependent on the liquid mass flow rate and gas velocity. An increase in the liquid mass flow rate causes an enhancement of the effect of inclination on the heat and mass transfer. The inclination affects the heat and mass transfer, especially at lower gas velocities. In the range of inclination angles of 0–10°, an increase in the inclination improves the evaporation by increasing the vapor mass flow rate. The maximum effect of inclination is nearly achieved at an inclination angle of 10°.

[1]  M. Daguenet,et al.  Étude numérique de l'évaporation dans un courant d'air humide laminaire d'un film d'eau ruisselant sur une plaque inclinée , 2000 .

[2]  F. Thiele,et al.  ON THE CALCULATION OF MOMENTUM, HEAT, AND MASS TRANSFER IN LAMINAR AND TURBULENT BOUNDARY LAYER FLOWS ALONG A VAPORIZING LIQUID FILM , 1983 .

[3]  L. C. Chow,et al.  Evaporation of water into a laminar stream of air and superheated steam , 1983 .

[4]  Anil K. Rajvanshi,et al.  A scheme for large scale desalination of sea water by solar energy , 1980 .

[5]  Mousa K. Abu Arabi,et al.  Performance evaluation of desalination processes based on the humidification/dehumidification cycle with different carrier gases , 2003 .

[6]  R. A. Seban,et al.  Heat Transfer to Evaporating Liquid Films , 1971 .

[7]  W. Yan,et al.  Convective heat and mass transfer along an inclined heated plate with film evaporation , 1995 .

[8]  Frank Thiele,et al.  Heat and Mass Transfer in Evaporating Two-Component Liquid Film Flow , 1990 .

[9]  W. Worek,et al.  Method of heat and mass transfer enhancement in film evaporation , 1996 .

[10]  Michel Daguenet,et al.  EVAPORATION EN CONVECTION FORCEE D'UN FILM MINCE S'ECOULANT EN REGIME PERMANENT, LAMINAIRE ET SANS ONDE, SUR UNE SURFACE PLANE INCLINEE , 1994 .

[11]  T. R. Shembharkar,et al.  Prediction of film cooling with a liquid coolant , 1986 .

[12]  Robert E. Foster,et al.  SOLAR DISTILLATION PROVIDING POTABLE WATER FOR BORDER COLONIAS , 2002 .

[13]  Lourdes García-Rodríguez,et al.  Preliminary design and cost analysis of a solar distillation system , 1999 .

[14]  Tsing-Fa Lin,et al.  Combined heat and mass transfer in natural convection between vertical parallel plates with film evaporation , 1990 .