BINARY AND MULTICOMPONENT VAPOR-LIQUID EQUILIBRIA OF SYNTHESIS GAS COMPONENTS, METHANOL AND WATER WITH TETRA ETHYLENE GLYCOL DIMETHYL ETHER (TETRAGLYME)
- 1 April 1991
- journal article
- Published by Taylor & Francis in Chemical Engineering Communications
- Vol. 102 (1) , 35-46
- https://doi.org/10.1080/00986449108910847
Abstract
No abstract availableKeywords
This publication has 12 references indexed in Scilit:
- Solubilities of synthesis gas components in a paraffinic oil under methanol synthesis conditionsJournal of Chemical & Engineering Data, 1987
- Fluid mixtures at high pressures IV. Isothermal phase equilibria in binary mixtures consisting of (methanol + hydrogen or nitrogen or methane or carbon monoxide or carbon dioxide)The Journal of Chemical Thermodynamics, 1987
- Binary vapour—liquid equilibria of methanol with sulfolane. Tetraethylene glycol dimethyl ether and 18-crown-6Published by Elsevier ,1986
- Revised procedures for phase equilibrium calculations with the Soave equation of stateIndustrial & Engineering Chemistry Process Design and Development, 1985
- Solubility and mass transfer of CO and H2 in Fischer—Tropsch liquids and slurriesThe Chemical Engineering Journal, 1984
- Solubilities of inert gases and methane in H2O and in D2O in the temperature range of 300 to 600 KThe Journal of Chemical Physics, 1982
- Phase equilibria in the H2CO system at temperatures from 70 to 125 K and pressures to 53 MPaFluid Phase Equilibria, 1981
- Correlation of the Phase Behavior in the Systems Hydrogen Sulfide-Water and Carbon Dioxide-WaterIndustrial & Engineering Chemistry Process Design and Development, 1976
- Equilibrium constants from a modified Redlich-Kwong equation of stateChemical Engineering Science, 1972
- Determination of Activity Coefficients from total pressure measurementsAustralian Journal of Chemistry, 1953