Standard

Solubility, liquid–liquid equilibrium and critical states for the quaternary system acetic acid–ethanol–ethyl acetate–water at 293.15 K. / Trofimova, Maya; Toikka, Maria; Toikka, Alexander.

In: Fluid Phase Equilibria, Vol. 313, 2012, p. 46-51.

Research output: Contribution to journal › Article

Harvard

Trofimova, M, Toikka, M & Toikka, A 2012, 'Solubility, liquid–liquid equilibrium and critical states for the quaternary system acetic acid–ethanol–ethyl acetate–water at 293.15 K', Fluid Phase Equilibria, vol. 313, pp. 46-51. https://doi.org/10.1016/j.fluid.2011.09.035

APA

Trofimova, M., Toikka, M., & Toikka, A. (2012). Solubility, liquid–liquid equilibrium and critical states for the quaternary system acetic acid–ethanol–ethyl acetate–water at 293.15 K. Fluid Phase Equilibria, 313, 46-51. https://doi.org/10.1016/j.fluid.2011.09.035

Vancouver

Trofimova M, Toikka M, Toikka A. Solubility, liquid–liquid equilibrium and critical states for the quaternary system acetic acid–ethanol–ethyl acetate–water at 293.15 K. Fluid Phase Equilibria. 2012;313:46-51. https://doi.org/10.1016/j.fluid.2011.09.035

Author

Trofimova, Maya ; Toikka, Maria ; Toikka, Alexander. / Solubility, liquid–liquid equilibrium and critical states for the quaternary system acetic acid–ethanol–ethyl acetate–water at 293.15 K. In: Fluid Phase Equilibria. 2012 ; Vol. 313. pp. 46-51.

BibTeX

@article{dfbe147b884d48ecb55e5ab08eee0a05,
title = "Solubility, liquid–liquid equilibrium and critical states for the quaternary system acetic acid–ethanol–ethyl acetate–water at 293.15 K",
abstract = "Solubility, critical states and liquid–liquid equilibrium (LLE) data for the quaternary system acetic acid–ethanol–ethyl acetate–water and for the ternary sub-systems acetic acid–ethyl acetate–water and ethanol–ethyl acetate–water were obtained at 293.15 K and atmospheric pressure. Binodal curves, tie-lines and compositions of critical points were determined. In order to construct the binodal surface and critical curve of the quaternary system, three quaternary sectional planes with several ratios of acetic acid and ethanol were studied. Experimental LLE data were compared with the values calculated by UNIFAC model and it was found that the experimental and calculated data are in a good agreement.",
keywords = "Liquid–liquid equilibria, Quaternary reacting systems, Critical states",
author = "Maya Trofimova and Maria Toikka and Alexander Toikka",
year = "2012",
doi = "10.1016/j.fluid.2011.09.035",
language = "English",
volume = "313",
pages = "46--51",
journal = "Fluid Phase Equilibria",
issn = "0378-3812",
publisher = "Elsevier",

}

RIS

TY - JOUR

T1 - Solubility, liquid–liquid equilibrium and critical states for the quaternary system acetic acid–ethanol–ethyl acetate–water at 293.15 K

AU - Trofimova, Maya

AU - Toikka, Maria

AU - Toikka, Alexander

PY - 2012

Y1 - 2012

N2 - Solubility, critical states and liquid–liquid equilibrium (LLE) data for the quaternary system acetic acid–ethanol–ethyl acetate–water and for the ternary sub-systems acetic acid–ethyl acetate–water and ethanol–ethyl acetate–water were obtained at 293.15 K and atmospheric pressure. Binodal curves, tie-lines and compositions of critical points were determined. In order to construct the binodal surface and critical curve of the quaternary system, three quaternary sectional planes with several ratios of acetic acid and ethanol were studied. Experimental LLE data were compared with the values calculated by UNIFAC model and it was found that the experimental and calculated data are in a good agreement.

AB - Solubility, critical states and liquid–liquid equilibrium (LLE) data for the quaternary system acetic acid–ethanol–ethyl acetate–water and for the ternary sub-systems acetic acid–ethyl acetate–water and ethanol–ethyl acetate–water were obtained at 293.15 K and atmospheric pressure. Binodal curves, tie-lines and compositions of critical points were determined. In order to construct the binodal surface and critical curve of the quaternary system, three quaternary sectional planes with several ratios of acetic acid and ethanol were studied. Experimental LLE data were compared with the values calculated by UNIFAC model and it was found that the experimental and calculated data are in a good agreement.

KW - Liquid–liquid equilibria

KW - Quaternary reacting systems

KW - Critical states

U2 - 10.1016/j.fluid.2011.09.035

DO - 10.1016/j.fluid.2011.09.035

M3 - Article

VL - 313

SP - 46

EP - 51

JO - Fluid Phase Equilibria

JF - Fluid Phase Equilibria

SN - 0378-3812

ER -

ID: 5242918