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Vapor-Uquid Equilibrium VLE

Duran-Valencia, C. Pointurier, G. Valtz, A. Guilbot, P. Richon, D. Vapor-Uquid equilibrium (VLE) data for the carbon... [Pg.932]

Experimental data including the acidic species in the vapor phase within the above concentration range are scarce. Only very few publications of VLE data in that range are available [168, 173]. In contrast, numerous vapor pressure curves are accessible in literature. Chemical equilibrium data for the polycondensation and dissociation reaction in that range (>100 wt%) are so far not published [148]. However, a starting point to describe the vapor-Uquid equilibrium at those high concentratirMis is given by an EOS which is based on the fundamentals of the perturbation theory of Barker [212, 213]. Built on this theory, Sadowski et al. [214] have developed the PC-SAFT (Perturbed Chain Statistical Associated Fluid Theory) equation of state. The PC-SAFT EOS and its derivatives offer the ability to be fuUy predictive in combination with quantum mechanically based estimated parameters [215] and can therefore be used for systems without or with very little experimental data. Nevertheless, a model validation should be undertaken. Cameretti et al. [216] adopted the PC-SAFT EOS for electrolyte systems (ePC-SAFT), but the quality for weak electrolytes as phosphoric... [Pg.407]

Blanco, A. M. Ortega, J. Densities and vapor-Uquid equilibrium values for binary mixtures composed of methanol -1- an ethyl ester at 141.3 kPa with apphcation of an extended correlation equation for isobaric VLE data. J. Chem. Eng. Data 1998, 43, 638-645. [Pg.3809]


See other pages where Vapor-Uquid Equilibrium VLE is mentioned: [Pg.722]    [Pg.397]    [Pg.116]    [Pg.722]    [Pg.397]    [Pg.116]    [Pg.176]   


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