Concepedia

Vapor–liquid equilibria for the ternary systems of methyl tert-butyl ether + methanol + benzene and methyl tert-butyl ether + methanol + toluene and constituent binary systems at 313.15 K

Jong-Hyeok Oh, Kyu-Jin Han, Dong-Bok Won, So-Jin Park

Fluid Phase Equilibria · 2003 · 20 citations · 13 references

DOI

Concepts

References

13

Equilibrium constants from a modified Redlich-Kwong equation of state

Giorgio Soave · Chemical Engineering Science · 1972 · 6.2K citations

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Algebraic Representation of Thermodynamic Properties and the Classification of Solutions

O. Redlich, A. T. Kister · Industrial & Engineering Chemistry · 1948 · 5.8K citations

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A modified UNIFAC model. 2. Present parameter matrix and results for different thermodynamic properties

Juergen Gmehling, Jiding Li, Martin Schiller · Industrial & Engineering Chemistry Research · 1993 · 1.4K citations

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A Modified UNIFAC (Dortmund) Model. 3. Revision and Extension

Jürgen Gmehling, Jürgen Lohmann, Antje Jakob et al. · Industrial & Engineering Chemistry Research · 1998 · 311 citations

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Isothermal Vapor−Liquid Equilibria at 333.15 K and Excess Molar Volumes at 298.15 K of Ethyl <i>tert</i>-Butyl Ether (ETBE) + Alcoh-1-ol (C<sub>1</sub>−C<sub>4</sub>) Mixtures

Jong-Hyeog Oh, So-Jin Park · Journal of Chemical & Engineering Data · 1998 · 65 citations

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