Three-Dimensional Numerical Simulation for Annular Condensation in Rectangular Microchannels

A three-dimensional model in rectangular microchannels with constant heat flux is developed to predict steady annular condensation. The condensate flow field on the side wall, which is dominated by surface tension, is divided into two regions: the thin–film region and the meniscus region. The momentum and mass equations, in both the vapor and meniscus regions, along with the film thickness equation in thin–film region are solved numerically. The distribution of the meniscus curvature radius, thickness of the condensate film, heat transfer coefficient, and wall temperature are all determined. The results indicate that with the development of condensation, the condensate in the thin–film assumes a convex profile shape at the side wall, with the crest located at the midpoint of the side wall. The film thickness in the thin-film region increases at upstream locations and decreases as the flow moves downstream. The average heat transfer coefficient in the thin-film region is much larger than that occurring in the meniscus region. And the highest local heat transfer coefficient occurs at the intersection of the thin-film region and the meniscus on a cross section where the maximum wall temperature exists. The circumferential average heat transfer coefficient decreases drastically upstream to a lower value. After that, it remains nearly constant until close to the end of the annular flow, where it again begins to decrease.

[1]  Shimon Haber,et al.  A steady state, one dimensional, model for boiling two phase flow in triangular micro-channel , 2000 .

[2]  Mark Davies,et al.  Direct Comparison between Five Different Microchannels, Part 1: Channel Manufacture and Measurement , 2005 .

[3]  Srinivas Garimella,et al.  Condensation Flow Mechanisms in Microchannels: Basis for Pressure Drop and Heat Transfer Models , 2004 .

[4]  J. Rose,et al.  Film Condensation in Horizontal Microchannels: Effect of Channel Shape , 2005 .

[5]  G. P. Peterson,et al.  Condensation in Microchannels , 2008 .

[6]  Vincent Platel,et al.  Experimental study of flow characteristics during condensation in narrow channels: the influence of the diameter channel on structure patterns , 2004 .

[7]  Tianshou Zhao,et al.  Analysis of film condensation heat transfer inside a vertical micro tube with consideration of the meniscus draining effect , 2003 .

[8]  Xiaoze Du,et al.  Condensation on the outside surface of a small/mini diameter tube for vapor flowing through a horizontal annulus surround by an adiabatic concentric tube , 2000 .

[9]  Amir Faghri,et al.  Heat Transfer During Evaporation on Capillary-Grooved Structures of Heat Pipes , 1995 .

[10]  H. Honda,et al.  A Theoretical Model of Film Condensation in Square Section Horizontal Microchannels , 2004 .

[11]  G. G. Stokes "J." , 1890, The New Yale Book of Quotations.

[12]  P. Cheng,et al.  Condensation of steam in silicon microchannels , 2005 .

[13]  C. Perret,et al.  Analytic modeling, optimization, and realization of cooling devices in silicon technology , 2000 .

[14]  Tian-yang Zhao,et al.  Theoretical analysis of film condensation heat transfer inside vertical mini triangular channels , 2002 .

[15]  Jonathan Rose,et al.  A Theory of Film Condensation in Horizontal Noncircular Section Microchannels , 2005 .

[16]  K. Hosokawa,et al.  Interface motion of capillary-driven flow in rectangular microchannel. , 2004, Journal of colloid and interface science.

[17]  Srinivas Garimella Condensation Flow Mechanisms in Microchannels: Basis for Pressure Drop and Heat Transfer Models , 2003 .

[18]  Srinivas Garimella,et al.  Characterization of two-phase flow patterns in small diameter round and rectangular tubes , 1999 .

[19]  G. P. Peterson,et al.  Numerical simulation for steady annular condensation flow in triangular microchannels , 2008 .

[20]  Yongping Chen,et al.  Review of Condensation Heat Transfer in Microgravity Environments , 2006 .

[21]  Romano Gregorig,et al.  Hautkondensation an feingewellten Oberflächen bei Berücksichtigung der Oberflächenspannungen , 1954 .

[22]  R. Shah Laminar flow friction and forced convection heat transfer in ducts of arbitrary geometry , 1975 .