dc.description.abstract | Experimental evidence available in the literature indicates that the pool boiling heat
transfer with binary mixtures is lower than the respective mole- or mass-fraction averaged
value. Although a few investigators have presented analytical work to model
this phenomenon, empirical methods and correlations are used extensively. In the
present work, a theoretical analysis is presented to estimate the mixture effects on
heat transfer. The ideal heat transfer coefficient used currently in the literature to
represent the pool boiling heat transfer in the absence of mass diffusion effects is
based on empirical considerations, and has no theoretical basis. In the present work,
a new pseudo-single component heat transfer coefficient is introduced to account for
the mixture property effects more accurately. The liquid composition and the interface
temperature at the interface of a growing bubble are predicted analytically and their
effect on the heat transfer is estimated. The present model is compared with the
theoretical model of Calus and Leonidopoulos (1974), and two empirical models,
Calus and Rice (1972) and Fujita et al. (1996). The present model is able to predict
the heat transfer coefficients and their trends in azeotrope forming mixtures (benzene/
methanol, R-23/R-13 and R-22/R-12) as well as mixtures with widely varying boiling
points (water/ethylene glycol and methanol/water). | en_US |