A single parameter equation for the prediction of multicomponent vapor‐liquid data from binary isobaric data
- 1 August 1972
- journal article
- research article
- Published by Wiley in The Canadian Journal of Chemical Engineering
- Vol. 50 (4), 511-514
- https://doi.org/10.1002/cjce.5450500412
Abstract
No abstract availableKeywords
This publication has 19 references indexed in Scilit:
- A single‐parameter equation for isothermal vapor‐liquid equilibrium correlationsAIChE Journal, 1971
- Binary and ternary vapor-liquid equilibriums of methanol-acetone-2,3-dimethylbutaneJournal of Chemical & Engineering Data, 1970
- PREDICTION OF TERNARY VAPOR-LIQUID EQUILIBRIA FROM BINARY DATAIndustrial & Engineering Chemistry, 1970
- Multicomponent vapor-liquid equilibriums in systems of mixed positive and negative deviationsJournal of Chemical & Engineering Data, 1969
- Prediction of Vapor Compositions in Vapor-Liquid SystemsIndustrial & Engineering Chemistry Process Design and Development, 1968
- MULTICOMPONENT EQUILIBRIA—THE WILSON EQUATIONIndustrial & Engineering Chemistry, 1965
- Vapor-Liquid Equilibrium. XI. A New Expression for the Excess Free Energy of MixingJournal of the American Chemical Society, 1964
- Methanol-Ethanol-AcetoneIndustrial & Engineering Chemistry, 1956
- Composition of Vapors from Boiling Solutions. Systems Containing Acetone, Chloroform,and Methyl Isobutyl KetoneIndustrial & Engineering Chemistry, 1951
- Composition of Vapors from Boiling Binary SolutionsIndustrial & Engineering Chemistry, 1943