Based on the two-phase separated model, a detailed one-dimensional mod
el for binary mixtures had been proposed to study the in-tube evaporat
ion in a horizontal tube. The present model can predict the detailed v
ariation of the composition, temperature, heat transfer rate and press
ure drop of various binary mixtures under constant heat flux, counter-
flow, or parallel-flow conditions. The predicted results agree favorab
ly with the Takamatsu et al. [Int. J. Neat Mass Transfer 36, 3555-3563
(1993)] and Jung et al. [Exp. Heat Transfer 2, 237-255 (1989)] experi
mental data. Also, it is found that the full evaporation of the non-az
eotropic refrigerants may require a corresponding temperature higher t
han the saturation temperature of the less volatile component. The non
-linear variation of the property plays an important role in the heat
transfer and pressure drop characteristics of the refrigerant mixtures
. Copyright (C) 1996 Elsevier Science Ltd.