Investigation of the thermodynamic properties o f (furfuryl alcohol + toluene), (furfuryl alcohol + ethanol), or + (furfural + toluene) binary mixtures at several temperatures

Abstract

Vapor-liquid equilibrium (VLE) data are essential for the design of separation processes and equipment as well as for the extension of thermodynamic models Vapor-liquid equilibrium (VLE) data are essential for the design of separation processes and equipment as well as for the extension of thermodynamic models