The treatment of binary and ternary vapour‐liquid equilibrium data on systems with more than one liquid phase
- 1 January 1952
- journal article
- research article
- Published by Wiley in Journal of Chemical Technology & Biotechnology
- Vol. 2 (1) , 19-23
- https://doi.org/10.1002/jctb.5010020106
Abstract
No abstract availableKeywords
This publication has 11 references indexed in Scilit:
- A new method for the interpolation of ternary vapour‐liquid equilibrium dataJournal of Chemical Technology & Biotechnology, 1952
- Application of the Gibbs-Duhem Equation to Ternary and Multicomponent SystemsJournal of the American Chemical Society, 1950
- Vapor-Liquid Equilibrium Still for Partially Miscible LiquidsIndustrial & Engineering Chemistry, 1949
- Azeotrope Formation between Thiols and HydrocarbonsIndustrial & Engineering Chemistry, 1949
- Fractional distillation. II. The use of dilute solutions of thiophene in benzene as test mixtures and a comparison with mixtures of benzene and ethylene dichlorideTransactions of the Faraday Society, 1948
- Fractional distillation. I. The selection of test mixtures for estimating the efficiency of fractionating columnsTransactions of the Faraday Society, 1948
- A Thermodynamic Test for the Internal Consistency of Experimental Data on Volatility RatiosNature, 1947
- Binary Mixtures for Testing Fractionating Columns. CorrespondenceIndustrial & Engineering Chemistry, 1942
- Vapor-Liquid Equilibria of Nonideal SolutionsIndustrial & Engineering Chemistry, 1942
- Vapor-Liquid Equilibria and Boiling-Point Composition Relations for Systems n-Butanol–Water and Isobutanol–Water1,2Industrial & Engineering Chemistry, 1931