A model-free method for calculating vapor-liquid equilibria for multicomponent systems from total-pressure or boiling-point data
Author:
Publisher
Elsevier BV
Subject
Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering
Reference40 articles.
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3. A review of Barker’s activity coefficient method and VLE data reduction;The Journal of Chemical Thermodynamics;2012-01
4. Measurements of isothermal vapor–liquid equilibrium of binary methanol/dimethyl carbonate system under pressure;Fluid Phase Equilibria;2005-07
5. Experimental data, correlation and prediction of isobaric VLE for the ternary mixture (2-butanol + n-hexane + 1-chlorobutane) at 101.3 kPa;Fluid Phase Equilibria;2003-09
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