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High pressure phase behavior of the binary system (ethyl lactate + carbon dioxide)

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High pressure phase behavior of the binary system (ethyl lactate + carbon dioxide). / B. Paninho, Ana; V. M. Nunes, Ana; Paiva, Alexandre et al.
In: Fluid Phase Equilibria, Vol. 360, 25.12.2013, p. 129–133.

Research output: Contribution to Journal/Magazine › Journal article › peer-review

Harvard

B. Paninho, A, V. M. Nunes, A, Paiva, A & Najdanovic-Visak, V 2013, 'High pressure phase behavior of the binary system (ethyl lactate + carbon dioxide)', Fluid Phase Equilibria, vol. 360, pp. 129–133. https://doi.org/10.1016/j.fluid.2013.09.024

APA

B. Paninho, A., V. M. Nunes, A., Paiva, A., & Najdanovic-Visak, V. (2013). High pressure phase behavior of the binary system (ethyl lactate + carbon dioxide). Fluid Phase Equilibria, 360, 129–133. https://doi.org/10.1016/j.fluid.2013.09.024

Vancouver

B. Paninho A, V. M. Nunes A, Paiva A, Najdanovic-Visak V. High pressure phase behavior of the binary system (ethyl lactate + carbon dioxide). Fluid Phase Equilibria. 2013 Dec 25;360:129–133. doi: 10.1016/j.fluid.2013.09.024

Author

B. Paninho, Ana ; V. M. Nunes, Ana ; Paiva, Alexandre et al. / High pressure phase behavior of the binary system (ethyl lactate + carbon dioxide). In: Fluid Phase Equilibria. 2013 ; Vol. 360. pp. 129–133.

Bibtex

@article{5a4528783e7c4896a651530c8cbb875f,
title = "High pressure phase behavior of the binary system (ethyl lactate + carbon dioxide)",
abstract = "In this work the phase behavior of the binary system (ethyl lactate + CO2) was studied in the pressure range 0.4–17 MPa and at temperatures of 313.2, 333.2, 353.2, 373.2 and 393.2 K. Experiments were performed using the static synthetic method in a high pressure variable–volume view cell. Equilibrium data were correlated with the Peng–Robinson equation of state combined with the Mathias–Klotz–Prausnitz mixing rule. Additionally, density-based correlations, namely Chrastil's and Fornari's equations were used in order to correlate solubilities in both liquid and vapor phases.",
keywords = "Density-based correlations, Chrastil, Supercritical, Solubility, Green solvent",
author = "{B. Paninho}, Ana and {V. M. Nunes}, Ana and Alexandre Paiva and Vesna Najdanovic-Visak",
year = "2013",
month = dec,
day = "25",
doi = "10.1016/j.fluid.2013.09.024",
language = "English",
volume = "360",
pages = "129–133",
journal = "Fluid Phase Equilibria",
issn = "0378-3812",
publisher = "Elsevier",

}

RIS

TY - JOUR

T1 - High pressure phase behavior of the binary system (ethyl lactate + carbon dioxide)

AU - B. Paninho, Ana

AU - V. M. Nunes, Ana

AU - Paiva, Alexandre

AU - Najdanovic-Visak, Vesna

PY - 2013/12/25

Y1 - 2013/12/25

N2 - In this work the phase behavior of the binary system (ethyl lactate + CO2) was studied in the pressure range 0.4–17 MPa and at temperatures of 313.2, 333.2, 353.2, 373.2 and 393.2 K. Experiments were performed using the static synthetic method in a high pressure variable–volume view cell. Equilibrium data were correlated with the Peng–Robinson equation of state combined with the Mathias–Klotz–Prausnitz mixing rule. Additionally, density-based correlations, namely Chrastil's and Fornari's equations were used in order to correlate solubilities in both liquid and vapor phases.

AB - In this work the phase behavior of the binary system (ethyl lactate + CO2) was studied in the pressure range 0.4–17 MPa and at temperatures of 313.2, 333.2, 353.2, 373.2 and 393.2 K. Experiments were performed using the static synthetic method in a high pressure variable–volume view cell. Equilibrium data were correlated with the Peng–Robinson equation of state combined with the Mathias–Klotz–Prausnitz mixing rule. Additionally, density-based correlations, namely Chrastil's and Fornari's equations were used in order to correlate solubilities in both liquid and vapor phases.

KW - Density-based correlations

KW - Chrastil

KW - Supercritical

KW - Solubility

KW - Green solvent

U2 - 10.1016/j.fluid.2013.09.024

DO - 10.1016/j.fluid.2013.09.024

M3 - Journal article

VL - 360

SP - 129

EP - 133

JO - Fluid Phase Equilibria

JF - Fluid Phase Equilibria

SN - 0378-3812

ER -