An analytical investigation into filmwise condensation on a horizontal tube in a porous medium with suction at the tube surface

An analytical investigation is performed into the problem of steady filmwise condensation flow over the outside surface of a horizontal tube embedded in a porous medium with suction at the tube surface. As in classical film condensation problems, an assumption is made that the condensate and vapor layers meet at a common boundary rather than being separated by an intermediary two-phase zone. Furthermore, it is assumed that the condensate film has constant properties and conforms to Darcy’s law within the porous medium. By introducing an effective suction function to represent the effect of the wall suction on the thickness of the liquid film, both the local condensate film thickness and the local Nusselt number are derived using a simple numerical shooting method. The analytical results indicate that the mean Nusselt number depends on the Darcy number, the Jakob number, the Rayleigh number and the suction parameter. Furthermore, it is found that the local Nusselt number has a maximum value at the upper surface of the horizontal tube and reduces toward zero at the lower surface as a result of the finite thickness of the condensate layer.

[1]  J. Chiou,et al.  FILMWISE CONDENSATION ON A HORIZONTAL ELLIPTICAL TUBE EMBEDDED IN POROUS MEDIA , 1994 .

[2]  Herman Merte,et al.  Condensation heat transfer , 1973 .

[3]  D. K. Chui,et al.  Transient film condensation on a vertical surface in a porous medium , 1984 .

[4]  J. L. Gregg,et al.  LAMINAR CONDENSATION HEAT TRANSFER ON A HORIZONTAL CYLINDER , 1959 .

[5]  P. Cheng,et al.  Film condensation along an inclined surface in a porous medium , 1981 .

[6]  J. W. Yang Laminar Film Condensation on a Sphere , 1973 .

[7]  Yue-Tzu Yang,et al.  Steady filmwise condensation with suction on a finite-size horizontal flat plate embedded in a porous medium based on Brinkman and Darcy models , 2006 .

[8]  D. Poulikakos,et al.  Freezing of a water-saturated inclined packed bed of beads , 1993 .

[9]  M. Kaviany Principles of heat transfer in porous media , 1991 .

[10]  M. A. Al-Nimr,et al.  Transient Film Condensation on a Vertical Plate Imbedded in Porous Medium , 2000 .

[11]  Chen Cha'o-Kuang,et al.  Role of surface tension and ellipticity in laminar film condensation on a horizontal elliptical tube , 1993 .

[12]  Cha'o-Kuang Chen,et al.  Film condensation on a finite-size horizontal wavy plate bounded by a homogenous porous layer , 2005 .

[13]  M. M. Chen,et al.  An Analytical Study of Laminar Film Condensation: Part 1—Flat Plates , 1961 .

[14]  Tong-Bou Chang EFFECTS OF SURFACE TENSION ON LAMINAR FILMWISE CONDENSATION ON A HORIZONTAL PLATE IN A POROUS MEDIUM WITH SUCTION AT THE WALL , 2008 .

[15]  Tong-Bou Chang Laminar Filmwise Condensation on Horizontal Disk Embedded in Porous Medium With Suction at Wall , 2008 .

[16]  Kent S. Udell,et al.  Heat transfer in porous media considering phase change and capillarity—the heat pipe effect , 1985 .

[17]  M. Al-Nimr,et al.  Film condensation on a vertical plate imbedded in a porous medium , 1997 .

[18]  Han-Taw Chen,et al.  Conjugate mixed convection laminar non-Darcy film condensation along a vertical plate in a porous medium , 2001 .

[19]  B. Nimmo,et al.  Laminar film condensation on a finite horizontal surface , 1968 .

[20]  Tong-Bou Chang,et al.  Mixed-convection film condensation along outside surface of vertical tube in saturated vapor with forced flow , 2008 .