Predicting the excess enthalpies and vapor–liquid equilibria of multicomponent systems containing ether and hydrocarbons
Author:
Publisher
Elsevier BV
Subject
Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering
Reference43 articles.
1. Review of thermophysical property measurements on mixtures containing MTBE, TAME, and other ethers with non-polar solvents
2. Calculation of Isothermal Vapor-Liquid Equilibrium Data for Binary Mixtures from Heats of Mixing
3. The Prediction of Vapor-Liquid Equilibrium from Heat of Mixing Data for Binary Hydrocarbon-Alcohol Mixtures
4. Prediction of isobaric vapour–liquid equilibrium from excess enthalpies for (methyl tert -butyl ether + alkane(s)) mixtures
5. Estimation of the Excess Gibbs Free Energy and Enthalpy of Mixing of Binary Nonassociated Mixtures
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1. Measurement and correlation of (vapor+liquid) equilibrium data for {α-pinene+p-cymene+(S)-(−)-limonene} ternary system at atmospheric pressure;The Journal of Chemical Thermodynamics;2013-03
2. Excess Molar Enthalpies of Dipropyl Ether + Dibutyl Ether + (1-Hexene or Tetrahydrofuran) at 298.15 K;Journal of Chemical & Engineering Data;2010-11-02
3. Liebermann‐fried model parameters for calculating vapour‐liquid equlibria of oxygenate and hydrocarbon mixtures;Journal of the Chinese Institute of Engineers;2005-10
4. Excess enthalpies of { ethyl tert -butylether + hexane + heptane, or octane } at the temperature 298.15 K;The Journal of Chemical Thermodynamics;2001-09
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