The paper presents a theoretical model to predict film condensation heat transfer from a vapor flowing in horizontal square and equilateral triangular section minichannels or microchannels. The model is based on fundamental analysis which assumes laminar condensate flow on the channel walls and takes account of surface tension, interfacial shear stress, and gravity. Results are given for channel sizes (side of square or triangle) in the range of 0.5–5 mm and for refrigerants R134a, R22, and R410A. The cases considered here are where the channel wall temperature is uniform and the vapor is saturated at the inlet. The general behavior of the condensate flow pattern (spanwise and streamwise profiles of the condensate film), as well as streamwise variation of local mean (over section perimeter) heat-transfer coefficient and vapor mass quality, are qualitatively in accord with expectations on physical grounds. The magnitudes of the calculated heat-transfer coefficients are in general agreement with experimental data for similar, but nonidentical, channel geometry and flow parameters.
Issue Section:
Micro/Nanoscale Heat Transfer
Keywords:
film flow,
condensation,
two-phase flow,
microfluidics,
channel flow,
heat transfer,
laminar flow,
surface tension,
gravity waves,
refrigerants,
pattern formation,
Condensation,
Heat Transfer Enhancement,
Microchannel,
Noncircular Tube,
Theory,
Surface Tension,
R134a,
R22,
R410A,
Refrigerant
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NIST Thermodynamic and Transport Properties of Refrigerants and Refrigerants Mixtures—REFPROP, Version 6.0
.Copyright © 2005
by American Society of Mechanical Engineers
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