Solubilities of carbon dioxide, hydrogen sulfide and nitrogen mixtures in methanol
- 1 July 1981
- journal article
- research article
- Published by Wiley in AIChE Journal
- Vol. 27 (4), 605-613
- https://doi.org/10.1002/aic.690270411
Abstract
No abstract availableKeywords
This publication has 11 references indexed in Scilit:
- Estimation of Partial Molar Volume and Fugacity Coefficient of Components in Mixtures from the Soave and Peng-Robinson Equations of StateIndustrial & Engineering Chemistry Process Design and Development, 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
- A Modified Soave Equation of State for Phase Equilibrium Calculations. 2. Systems Containing CO2, H2S, N2, and COIndustrial & Engineering Chemistry Process Design and Development, 1978
- ISOTHERMAL VAPOR-LIQUID EQUILIBRIA OF ACETONE-CARBON DIOXIDE AND METHANOL-CARBON DIOXIDE SYSTEMS AT HIGH PRESSURESJOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1975
- Solubility of methanol in compressed nitrogen, argon, methane, ethylene, ethane, carbon dioxide, and nitrous oxide. Evidence for association of carbon dioxide with methanol in the gas phaseThe Journal of Physical Chemistry, 1972
- Equilibrium constants from a modified Redlich-Kwong equation of stateChemical Engineering Science, 1972
- A Correlation of Vaporization Equillbrium Ratios for Gas Processing SystemsIndustrial & Engineering Chemistry Process Design and Development, 1971
- Application of the Wohl equation to ternary liquid‐vapor equilibriaAIChE Journal, 1966
- Vapor-Liquid Phase Equilibrium in the CO2-112, C O2-N2 and CO2-02 SystemsThe Journal of the Society of Chemical Industry, Japan, 1966
- Heterogeneous phase equilibria of the hydrogen sulfide–carbon dioxide systemAIChE Journal, 1959