Phase equilibria properties of binary and ternary systems containing di-isopropyl ether+isobutanol+benzene at 313.15K
Author:
Publisher
Elsevier BV
Subject
Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering
Reference21 articles.
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3. Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons. 1. Total-pressure data and GE for methyl tert-butyl etherbenzenecyclohexane at 313.15 K
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1. Abraham model correlations for describing solute transfer into diisopropyl ether;Physics and Chemistry of Liquids;2014-10-29
2. Phase equilibrium properties of the ternary mixture dibutyl ether+toluene+heptane at 313.15K;Fluid Phase Equilibria;2012-03
3. Experimental and predicted excess molar enthalpies of binary mixtures containing 2,2′-oxybis[propane], benzene, butan-1-ol, 2-methylpropan-1-ol, 2-methyl-2-ene-1-propanol at 303.15K;Fluid Phase Equilibria;2010-12
4. Thermodynamic Properties of Binary and Ternary Mixtures Containing Di-isopropyl Ether, 2-Propanol, and Benzene at T = 313.15 K;Journal of Chemical & Engineering Data;2010-04-13
5. Recommended Reference Materials for Realization of Physicochemical Properties;Pure and Applied Chemistry;1977-01-01
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