Model-free methods for vapor—liquid equilibria calculations Binary systems
- 31 December 1980
- journal article
- Published by Elsevier in Chemical Engineering Science
- Vol. 35 (11) , 2247-2256
- https://doi.org/10.1016/0009-2509(80)87002-3
Abstract
No abstract availableThis publication has 25 references indexed in Scilit:
- Multicomponent vapor-liquid equilibrium: Direct integration of the Gibbs-Duhem equationChemical Engineering Science, 1978
- Measurement of vapor‐liquid equilibria using a semi‐continuous total pressure static equilibrium stillThe Canadian Journal of Chemical Engineering, 1976
- Excess Gibbs energies of binary systems of isopentanol and n-pentanol with hexane isomers at 25.deg.C: measurement and prediction by analytical group solution modelJournal of Chemical & Engineering Data, 1976
- Computation of Vapor-Liquid Equilibrium Data from Binary and Ternary Vapor Pressure and Boiling Point MeasurementsIndustrial & Engineering Chemistry Process Design and Development, 1974
- A direct method for calculating ternary vapor compositions from total‐pressure measurementsThe Canadian Journal of Chemical Engineering, 1974
- Calculation of binary vapor composition from solution vapor pressureThe Canadian Journal of Chemical Engineering, 1970
- An extension of the spline fit technique and applications to thermodynamic dataAIChE Journal, 1967
- Computation of Vapor-Liquid Equilibrium Data from Solution Vapor Pressure MeasurementsIndustrial & Engineering Chemistry Fundamentals, 1965
- How to Compute Binary Vapor-Liquid Equilibrium Compositions from Experimental P-x or t-x DataIndustrial & Engineering Chemistry, 1961
- Activity coefficients at infinite dilutionAIChE Journal, 1955