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Modeling And Parameters Fitting Of Chemical And Phase Equilibria In Reactive Systems For Biodiesel Production
(PERGAMON-ELSEVIER SCIENCE LTDOXFORD, 2015)
Fractionation of lemon essential oil by solvent extraction: Phase equilibrium for model systems at T=298.2 K
(ACADEMIC PRESS LTD- ELSEVIER SCIENCE LTDLONDON, 2012)
The fractioning of lemon essential oil can be performed by liquid-liquid extraction using hydrous ethanol as a solvent. A quaternary mixture composed of limonene, gamma-terpinene, beta-pinene, and citral was used to simulate ...
Using Ionic Liquids To Break the Ethanol−Ethyl Acetate Azeotrope
(American Chemical Society, 2015-11-05)
Systems that form azeotropes or have relative volatilities close to 1.0 represent very little energy and capital intensive separations. Ionic liquids (ILs) can serve as nonvolatile entrainers to break azeotropes and enable ...
(Liquid plus liquid) equilibria in {water plus acrylic acid + (1-butanol, or 2-butanol, or 1-pentanol)} systems at T=293.2 K, T=303.2 K, and T=313.2 K and atmospheric pressure
(Academic Press Ltd- Elsevier Science LtdLondonInglaterra, 2011)
Liquid-liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate plus aromatic plus aliphatic
(Elsevier Science BvAmsterdamHolanda, 2008)
Liquid-liquid equilibrium of water plus PEG 8000 plus magnesium sulfate or sodium sulfate aqueous two-phase systems at 35 degrees C: Experimental determination and thermodynamic modeling
(Brazilian Soc Chemical EngSao PauloBrasil, 2005)