Calculation of vapor—liquid equilibria at elevated pressures by means of an equation of state incorporating association
- 31 December 1989
- journal article
- Published by Elsevier in Chemical Engineering Science
- Vol. 44 (3) , 713-725
- https://doi.org/10.1016/0009-2509(89)85046-8
Abstract
No abstract availableKeywords
This publication has 36 references indexed in Scilit:
- An equation of state for the description of phase equilibria and caloric quantities on the basis of the “chemical theory”Fluid Phase Equilibria, 1986
- Gas-liquid equilibrium in mixtures of carbon dioxide + toluene and carbon dioxide + m-xyleneJournal of Chemical & Engineering Data, 1980
- Computational Methods for High-Pressure Phase Equilibria and Other Fluid-Phase Properties Using a Partition Function. 2. MixturesIndustrial & Engineering Chemistry Process Design and Development, 1980
- Equilibrium phase properties of the toluene-hydrogen sulfide and heptane-hydrogen sulfide binary systemsJournal of Chemical & Engineering Data, 1980
- Liquid-vapor equilibriums at 270.00 K for systems containing nitrogen, methane, and carbon dioxideJournal of Chemical & Engineering Data, 1978
- The equilibrium phase properties of the ethane-hydrogen sulfide system at subambient temperaturesJournal of Chemical & Engineering Data, 1977
- A New Two-Constant Equation of StateIndustrial & Engineering Chemistry Fundamentals, 1976
- Isothermal vapor-liquid equilibrium data for binary systems containing carbon dioxide at high pressures: methanol-carbon dioxide, n-hexane-carbon dioxide, and benzene-carbon dioxide systemsJournal of Chemical & Engineering Data, 1976
- Liquid-vapor equilibria at 250.00.deg.K for systems containing methane, ethane, and carbon dioxideJournal of Chemical & Engineering Data, 1976
- Phase relations of binary systems that form azeotropes: I. The ammonia–n‐Butane systemAIChE Journal, 1958