Solubilities of carbon dioxide in methanol and methanol-water at high pressures: experimental data and modeling
- 31 December 1985
- journal article
- Published by Elsevier in Fluid Phase Equilibria
- Vol. 23 (2-3) , 243-258
- https://doi.org/10.1016/0378-3812(85)90009-3
Abstract
No abstract availableThis publication has 19 references indexed in Scilit:
- A versatile phase equilibrium equation of stateIndustrial & Engineering Chemistry Process Design and Development, 1983
- Use of the Soave modification of the Redlich-Kwong equation of state for phase equilibrium calculations. Systems containing methanolIndustrial & Engineering Chemistry Process Design and Development, 1983
- Correlation of K-factors for mixtures of hydrogen and heavy hydrocarbonsChemical Engineering Science, 1980
- Determination of the equilibrium constants of water-methanol deuterium exchange reactions from vapour pressure measurementsAustralian Journal of Chemistry, 1980
- Prediction of Phase Equilibria in Sour Natural Gas Systems Using the Soave-Redlich-Kwong Equation of StateIndustrial & Engineering Chemistry Process Design and Development, 1979
- New mixing rules in simple equations of state for representing vapour-liquid equilibria of strongly non-ideal mixturesFluid Phase Equilibria, 1979
- A Modified Soave Equation of State for Phase Equilibrium Calculations. 1. Hydrocarbon SystemsIndustrial & Engineering Chemistry Process Design and Development, 1978
- Isothermal liquid-vapor equilibriums for system methanol-waterJournal of Chemical & Engineering Data, 1976
- ISOTHERMAL VAPOR-LIQUID EQUILIBRIA OF ACETONE-CARBON DIOXIDE AND METHANOL-CARBON DIOXIDE SYSTEMS AT HIGH PRESSURESJOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1975
- Compressibility, fugacity, and water-solubility of carbon dioxide in the region 0–36 atm. and 0–100°cChemical Engineering Science, 1957