PRSV2: A cubic equation of state for accurate vapor—liquid equilibria calculations
- 1 October 1986
- journal article
- research article
- Published by Wiley in The Canadian Journal of Chemical Engineering
- Vol. 64 (5) , 820-826
- https://doi.org/10.1002/cjce.5450640516
Abstract
No abstract availableKeywords
This publication has 15 references indexed in Scilit:
- An Improved Cubic Equation of StatePublished by American Chemical Society (ACS) ,1986
- Excess thermodynamic functions for ternary systems. 6. Total-pressure data and GE for acetone-ethanol-water at 50.degree.CJournal of Chemical & Engineering Data, 1980
- Excess thermodynamic functions for ternary systems. 5. Total-pressure data and GE for 1,4-dioxane-ethanol-water at 50.degree.CJournal of Chemical & Engineering Data, 1979
- New mixing rules in simple equations of state for representing vapour-liquid equilibria of strongly non-ideal mixturesFluid Phase Equilibria, 1979
- Thermodynamic properties of aqueous non-electrolyte mixtures II. Vapour pressures and excess Gibbs energies for water + ethanol at 303.15 to 363.15 K determined by an accurate static methodThe Journal of Chemical Thermodynamics, 1978
- A New Two-Constant Equation of StateIndustrial & Engineering Chemistry Fundamentals, 1976
- Statistical thermodynamics of liquid mixtures: A new expression for the excess Gibbs energy of partly or completely miscible systemsAIChE Journal, 1975
- Liquid-vapour equilibrium. IL. Phase equilibria in the ternary system ethyl acetate-ethanol-waterCollection of Czechoslovak Chemical Communications, 1972
- The use of Chebyshev polynomials for the representation of vapour pressures between the triple point and the critical pointThe Journal of Chemical Thermodynamics, 1970
- Local compositions in thermodynamic excess functions for liquid mixturesAIChE Journal, 1968