화학공학소재연구정보센터
Fluid Phase Equilibria, Vol.260, No.2, 177-182, 2007
Vapor pressure of R227ea+ethanol at 343.13 K by molecular simulation
A new molecular model for 1,1,1,2,3,3,3-heptafluoropropane (R227ea) was developed on the basis of quantum chemical calculations and optimized using experimental vapor pressure and bubble density data. In combination with an existing model for ethanol, a molecular model for the binary mixture R227ea + ethanol was defined, using the Lorentz-Berthelot combining rule. It was validated at 283.17 K, where, considering the statistical uncertainties, it agrees to the experimental vapor pressure. The vapor-liquid equilibrium, comprising both bubble line and dew line data, was predicted at 343.13 K by molecular simulation. The Peng-Robinson equation of state fails for this system. (C) 2007 Elsevier B.V. All rights reserved.